Chemical engineering education

Material Information

Chemical engineering education
Alternate Title:
Abbreviated Title:
Chem. eng. educ.
American Society for Engineering Education -- Chemical Engineering Division
Place of Publication:
Storrs, Conn
Chemical Engineering Division, American Society for Engineering Education
Publication Date:
Annual[ FORMER 1960-1961]
Physical Description:
v. : ill. ; 22-28 cm.


Subjects / Keywords:
Chemical engineering -- Study and teaching -- Periodicals ( lcsh )
serial ( sobekcm )
periodical ( marcgt )


Chemical abstracts
Additional Physical Form:
Also issued online.
Dates or Sequential Designation:
1960-June 1964 ; v. 1, no. 1 (Oct. 1965)-
Numbering Peculiarities:
Publication suspended briefly: issue designated v. 1, no. 4 (June 1966) published Nov. 1967.
General Note:
Title from cover.
General Note:
Place of publication varies: Rochester, N.Y., 1965-1967; Gainesville, Fla., 1968-

Record Information

Source Institution:
University of Florida
Rights Management:
All applicable rights reserved by the source institution and holding location.
Resource Identifier:
01151209 ( OCLC )
70013732 ( LCCN )
0009-2479 ( ISSN )
TP165 .C18 ( lcc )
660/.2/071 ( ddc )

UFDC Membership

Chemical Engineering Documents


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Department of Chemical Engineering
University of Florida
Gainesville, Florida 32611

Editor: Ray Fahien (904) 392-0857
Consulting Editor: Mack Tyner
Managing Editor:
Carole C. Yocum (904) 392-0861
Publications Board and Regional
Advertising Representatives:
Lee C. Eagleton
Pennsylvania State University

Past Chairman:
Klaus D. Timmerhaus
University of Colorado

Richard Felder
North Carolina State University
Jack R. Hopper
Lamar University
James Fair
University of Texas
Gary Poehlezn
Georgia Tech

Robert F. Anderson
UOP Process Division
Lowell B. Koppel
Purdue University

Frederick H. Shair
California Institute of Technology
Angelo J. Perna
New Jersey Institute of Technology
Stuart W. Churchill
University of Pennsylvania
Raymond Baddour
A. W. Westerberg
Carnegie-Mellon University

Charles Sleicher
University of Washington
Leslie W. Shemilt
McMaster University
Thomas W. Weber
State University of New York

Chemical Engineering Education

The Educator
110 Dendy Sloan of the Colorado School of Mines,
Brodie Farquhar
114 The University of Utah, Norman W. Ryan
Views and Opinions
120 Are We Participants or Victims?, James Wei
162 Adjunct Position: One Way to Keep Up With
Technology and Education, Richard D. Noble
121 The Teaching of Process Design, T. K. Sherwood
132 Improvements in the Teaching of Staged Operations,
Maryam Golnaraghi, Paulette Clancy, Keith E.
148 Estimation of Fluid Properties and Phase Equilibria,
M. Herskowitz
156 Fundamentals of Chemical Processes,
William R. Moser
124 A Junior Year ChE Laboratory, W. R. Paterson
136 Recycle With Heating: A Laboratory Experiment,
A. Foord, G. Mason
150 An Innovative ChE Process Laboratory, Skip
Rochefort, Stanley Middleman, Pao C. Chau
128 Basic Information Science Training for Chemical
Engineers, O. M. Kut, R. Queralt, L. M. Rose
144 Impact of Packaged Software for Process Control
on Chemical Engineering Education and
Research, Brian Buxton
Class and Home Problems
140 One Month Problem: An Exercise in Modelling,
V. Ravichandran
113 Positions Available
118 Book Review
119 Division Activities
135 Letter to the Editor

CHEMICAL ENGINEERING EDUCATION is published quarterly by Chemical
Engineering Division, American Society for Engineering Education. The publication
is edited at the Chemical Engineering Department, University of Florida. Second-class
postage is paid at Gainesville, Florida, and at DeLeon Springs, Florida. Correspondence
regarding editorial matter, circulation and changes of address should be addressed
to the Editor at Gainesville, Florida 32611. Advertising rates and information are
available from the advertising representatives. Plates and other advertising material
may be sent directly to the printer: E. O. Painter Printing Co., P. O. Box 877,
DeLeon Springs, Florida 32028. Subscription rate U.S., Canada, and Mexico is $20 per
year, $15 per year mailed to members of AIChE and of the ChE Division of ASEE.
Bulk subscription rates to ChE faculty on request. Write for prices on individual
back copies. Copyright 1985 Chemical Engineering Division of American Society
for Engineering Education. The statements and opinions expressed in this periodical
are those of the writers and not necessarily those of the ChE Division of the ASEE
which body assumes no responsibility for them. Defective copies replaced if notified
within 120 days.
The International Organization for Standardization has assigned the code US ISSN
0009-2479 for the identification of this periodical.


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Colorado School of Mines

Colorado School of Mines
Golden, CO 80401

T DENDY SLOAN IS AN academic man for all
Seasonss" said Art Kidnay, department
head of Chemical Engineering and Petroleum Re-
fining at the Colorado School of Mines. "He
is one of those rare individuals who does every-
thing well."
Professor Sloan is a renaissance figure, on a
campus and in a discipline dominated by special-
ists. "Dendy is the most balanced, well-rounded
faculty member I know," said Kidnay. "That is
what sets him apart. Other faculty on campus
and around the nation are equally competent in
areas like teaching, committee assignments, re-
search, engineering education research, and work
in the professional societies-but I don't know
anyone quite as good in all areas."
The shelves in Sloan's office contain the usual
and the unexpected. Chemical engineering texts
and journals dominate, as do two large models of
hydrate molecules. What is different is the strong
presence of books of philosophy and literature.
Books like Zen and the Art of Motorcycle Main-
tenance by Robert Persig, and Whitehead's The
Aims of Education nestle with books by William
Shakespeare, Herman Hesse and Robert Frost.
The hydrate molecular models represent the
specialization Sloan has sought, while the philoso-

"We're still teaching like Saint
Thomas Aquinas in the Thirteenth Century,
lecturing in front of a group of students.
How do we integrate new tools like computers? They
are no panacea, yet I believe that the key is
in experiential learning, case studies,
and real-life problem solving."

Copyright ChE Division, ASEE, 1985

phy and literature books represent a curiosity
that has never been satisfied with the comfort of
settling into a familiar niche.
"Dendy teaches a variety of courses," said
Kidnay, "and by next year, he will have taught
every undergraduate course in our department.
He's done this voluntarily. Very few faculty can or
would do something like that-most prefer to
specialize near their own research interests,
which makes it easier to teach. I know that some
schools have a policy to force faculty to rotate
through the curriculum in the interest of balance
and keeping up with all areas of your discipline.
We don't have that policy, simply because most
of us don't have the time. Dendy is the only one
I know who could pull it off."
Born in Seneca, South Carolina, in 1944,
Dendy developed an early interest in math,
science, chemistry, and physics in high school.
He earned his BS in chemical engineering from
Clemson University in 1965 and worked five years
for duPont, working in Tennessee, Delaware,
West Virginia, and South Carolina. "In the course
of those four jobs with duPont," said Sloan, "I
discovered that I enjoyed opportunities to be
entirely self-motivated and directed. Teaching
seemed like a good way to do that."


In light of his later professional accomplish-
ments, getting into graduate school should not
have been a problem. It was. "Dendy did not
have outstanding grades as an undergraduate,"
said his Clemson uppergraduate advisor, Dr. Jo-
seph Mullins. "As I recall, he was active in a band
and still plays a pretty hot banjo. The depart-
ment chairman suggested he take some math
courses and reapply." Several night courses and
A's later, Sloan entered the graduate program
at Clemson.
"Dendy was the most organized student I've
ever had," said Mullins. "He came early and
stayed late and ran during the lunch hour. Pretty
soon he had most of the grad students chugging
away, running with him." (Sloan has run 12
marathons and typically has put in 40 miles per
week over the past 20 years.)
It was at Clemson University that Sloan's role
models for teaching made their impact on his
career. "Clemson had an unusually strong focus
on education," said Sloan. "People like Joe
Mullins, Dick Harshman, and department chair-
man Charles Littlejohn had a real impact. As I
got into graduate education, I realized that this
was what I wanted to do with my life."
Sloan earned his MS from Clemson in 1972,
with the thesis title of "The Combined Effects of
Natural and Forced Convection in a Dual Mem-
brane, Horizontal Parallel Plate Ultrafilter"; and
his PhD in 1974, with the thesis title of "Non-
ideality of Binary Adsorbed Mixtures of Benzene
and Freon-11 on Highly Graphitized Carbon at
298.15 K and Pressures below 10 Torr."
"I advised Dendy to get his PhD elsewhere,"
said Mullins, "but he insisted on getting it here.
I did persuade him on the wisdom of doing post-
doctoral work elsewhere." Elsewhere turned out
to be Rice University, where Sloan encountered
Dr. Riki Kobayashi and worked as a research
fellow on determining the water content of
natural gas in equilibrium with hydrates.
"It was a very high pressure time and environ-
ment," said Kobayashi. "Dendy was responsible
for measuring and setting the water content specs
for a high pressure natural gas pipeline, from
Alaska to the lower 48. Dendy, along with Jerry
Holder (currently at the University of Pitts-
burgh), is currently recognized as one of the
primary researchers (in addition to Dr. Koba-
yashi) in the area of hydrates. The energy crisis
really had us going-so much so that I bought a
rollaway bed for Dendy. He never complained."

Methane hydrates are a molecular bond of water
and natural gas, under pressure. Under certain
conditions, hydrates can build up in a pipeline
and plug it.
From that initial focus on hydrates as a prob-
lem, Sloan eventually branched out to explore
methane hydrates as an energy solution. Rich
fields of methane hydrates exist in deep oceans,
as well as in permafrost regions of Canada,
Alaska and Siberia. It is estimated that under
United States land and territorial waters alone,

"Once a student learns the process
of learning and solving real-world, open-ended
problems, he or she will never have to worry about
the half-life of his or her knowledge-
they'll be life-long learners."

there are enough hydrate deposits to provide
natural gas supplies for at least 150 years, or 15
times the known supply of conventional natural
gas. This unconventional form of natural gas is
currently thought of as a future resource, and
some of Sloan's research studies is currently spon-
sored by the U.S. Department of Energy.
Sloan came to the Colorado School of Mines
in 1976. Here he taught most of the undergradu-
ate courses, specializing in thermodynamics, phase
equilibria, and stagewise process design at the
graduate level. His research proceeded with
natural gas hydrates and included adsorption,
phase equilibria, and thermal conductivity. He
came for the professional opportunities, the high
caliber of students, and the high degree of lati-
tude Mines offers its faculty, who enjoy both
teaching and research. He has stayed for these
and other reasons.
"This is small town America," said Sloan, re-
ferring to his nine years in Golden. "You have
the friendliness of a small community-Cub
Scouts, a good church-and access to a big city.
This is a good family place." That's important
to Sloan and his wife, Marjorie, and his two sons
-Trey, 13 and Mark, 10. Sloan has been active
in the Scouting movement for six years and has
served as an elder in the Presbyterian Church.
Marjorie is a second year law student at the Uni-
versity of Colorado. "I've had offers for other
positions, yet I haven't been able to convince my-
self that I'd be happier elsewhere," said Sloan.
Has he noticed any similarities between Cub
Scouts and college students? "Eight- to ten-year-
olds are bundles of unchanneled energy. You've


got to plan things that will hold their interest;
otherwise they climb the walls. Students 18-22
years old are generally very bright and very
channeled," said Sloan. "Graduate student per-
sonalities typically mirror those of the professor,
but undergraduates can be a substantially differ-
ent challenge. Working with undergraduates is
one of the best motivators for coming into this
profession, and when a school has as good

Sloan and his Cub Scout
big race.

troop getting ready for the

students as CSM does, it makes teaching doubly
Evidently, his ability to hold an eight-year-
old's attention has rubbed off on his college teach-
ing style. Students consistently rank him as one
of the best teachers on campus, year after year.
His peers have also recognized his teaching skills
by honoring him with the AMOCO Teaching Ex-
cellence Award at CSM, and with the Western
Electric Award from ASEE.
Currently, Sloan works with eleven graduate
students in research focused on natural gas
hydrates, vapor liquid equilibrium, and thermal
conductivity. In 1982, Dr. Sloan acquired the first
Western sample of methane hydrates when the
Glomar Challenger brought up samples from the
ocean floor off the coast of Guatemala. Shipped
in chilled and pressurized containers to Sloan, the
"dirty snowballs" have been divided up among
laboratories at CSM and other schools. Sloan and
his graduate students are trying to determine
optimum in situ methods of releasing condensed
methane molecules from the water molecules
which surround them.
One of the frustrations of running a success-
ful research operation is lack of time for personal,

hands-on research. "We come in as researchers
and become research managers. There is no time
for lab work. I find time for some theoretical and
computer work, but I really miss working in the
lab," said Sloan.
In spite of these limitations, Sloan does find
time for a number of other activities. These in-
clude professional service in the ASEE and other
organizations, service on a variety of CSM com-
mittees, work with the innovative EPICS pro-
gram at Mines, plus pondering philosophies of
engineering education. He even finds time to study
the personalities of faculty and students, correlat-
ing results with their career tracks.
Within the ASEE itself, Sloan is currently
Chairman of the Educational Research and
Methods Division and is Chairman-Elect for the
Chemical Engineering Division. Within CSM,
Sloan has served as chairman of the Honors Hu-
manities Tutorial Committee, and served on the
Presidential Search Committee.
"EPICS" stands for Engineering Practices
Introductory Course Sequence. Because the best
method for mastery of any skill is regular
practice, EPICS has been designed by Sloan and
other CSM faculty as a unique lab-type course,
providing "real-world" environments to develop
and practice engineering skills. "The emphasis is
on the process of learning, not the content of engi-
neering facts and figures. All the facts, figures
and cookbook procedures we pound into students'
heads have a half-life, a limited time-span of
value, due to the explosion of information and re-
search. Once a student learns the process of learn-
ing and solving real-world, open-ended problems,
he or she will never have to worry about the half-
life of his or her knowledge-they'll be life-long
learners," said Sloan.
"We're still teaching like Saint Thomas
Aquinas in the Thirteenth Century, lecturing in
front of a group of students. How do we inte-
grate new tools like computers? They are no
panacea, yet I believe that the key is in ex-
periential learning, case studies, and real-life
problem solving. Mines and Harvey Mudd are two
of the best places I know that are working toward
this new approach of engineering education," said
The shift from content to process will not
come easily, warned Sloan. "High school teachers
put a great deal of emphasis on content (students
regurgitating books and lectures), as do colleges,
yet we expect colleges to produce leaders and in-


novators. Giving up emphasis on content is very
threatening. It forces teachers to continually
learn new materials, use new tools, and to do re-
search. It forces us to think."
It also forces educators to look closely at how
students feel about the process of learning. "I'm
convinced that if a student leaves a course or a
school feeling badly, then we've done permanent
damage to that student. He/she won't be as good
an engineer as someone who left a course or school
excited about what they learned. As a profession,
we're not doing a good job of addressing this
Sloan enjoys reading philosophy and does not
see the discrepancy between the "real world" and
the "world of ideas." For Sloan, engineering and
philosophy are both concerned with open-ended
problems. "I try to see things as part of a spec-
trum, not as different or isolated from the whole.
Take Robert Persig's Zen and the Art of Motor-
cycle Maintenance. It presents the classic struggle
between objective science and intuitive romance
and shows that rather than being estranged from
each other, they can be part of a whole," said
Personality types fit into this world view.
Using the Myers-Briggs Type Indicator (MBTI),
Sloan has found that different personalities have
different world views and are attracted to differ-
ent disciplines (see "Applications of Psychologi-
cal Types in Engineering Education", February
1983, Engineering Education).
Some people are attuned to the practical,
hands-on, common-sense view of events, while
others are more attuned to the complex inter-
actions, theoretical implications or new possi-
bilities of events. These two styles of information
gathering, or perception, are known as Sensing
and Intuition, respectively.
"Since faculty are predominantly intuitive,"
said Sloan, "and students are evenly split, I'm
concerned that we may be awarding grades based
on personality characteristics, rather than per-
formance." Intuitives do better on exams prepared
by intuitive type faculty, while sensing types do
less well-usually because they re-read every test
problem in the interest of accurate compre-
hension, and run out of time.
For Sloan, balance or integration is a key con-
cept. Just as a mature personality should be able
to integrate intuitive and sensing methods of
learning, a mature profession (engineering edu-
cation) should be able to integrate content and

Chemical Engineering .. Tenure system faculty positions.
Doctorate in Chemical Engineering or closely related field.
A strong commitment to teaching and the ability to de-
velop a quality research program is expected. Preference
will be given to candidates with research interests in the
areas of Biochemical Engineering, Surface Science, Solid
State Phenomena, or Polymeric Materials. However, ap-
plicants with outstanding credentials and research interests
in other fields related to Chemical Engineering are en-
couraged to apply. Teaching and/or industrial experience
desirable but not essential. Michigan State University is
an affirmative action-equal opportunity employer and wel-
comes applications from women and minority groups. Send
applications and names of references to Chairperson,
Faculty Search Committee, Department of Chemical Engi-
neering, Michigan State University, East Lansing, Michi-
gan 48824-1226.

CAL INSTITUTE Assistant/Associate/ Full Professor
(full year, full time, tenure system). Biochemical engineer-
ing positions and Distinguished Research Professorship.
The Chemical Engineering Department and the Michigan
Biotechnology Institute have joint tenure system positions
open. Rank, salary and incentives commensurate with
qualifications. Applicants should have demonstrated ability
in one or more of the following areas. Bioreactor Design
and Scale-up; Product Separation and Recovery from Cell
Culture Broths; Sensors, Controls and Computer Inter-
facing of Biological Processes; and Renewable Resource
Technology. Strong commitment to applied research plus
teaching limited to graduate training in biotechnology ex-
pected. Applicants with outstanding credentials and an
active research program are encouraged to apply. The
positions offer the excitement of sharing in both the
understanding and rewards of developing new technology.
Qualified women and minorities are encouraged to apply.
Apply in writing to: Donald K. Anderson, Chairperson,
Biotechnology Search and Selection Committee, Michigan
State University, 173 Engineering Building, East Lansing,
MI 48824-1226. Applications are requested by September
1, 1985, but will be accepted as long as necessary to fill
the positions.

PROJECT ENGINEERS, Specialty Chemical Manufactur-
ing Company in Southwest Pennsylvania seeks candidates
to direct all process development activities for Emulsion
Polymer project. Requirements: Resume, PhD Chemical
Engineering plus 2 years experience as Project Engineer
or Chemical Research Engineer, PhD and employment ex-
perience must be in polymer rheology and engineering.
$47,088/year. Full time. Send resume to Charles A. Wilson,
Office of Employment Security, 300 Liberty Avenue, Room
1302, Pittsburgh, PA 15222. Job Order #3990818 DOT

process methods of teaching. To all who know him,
Dendy Sloan exemplifies a sense of balance and
wholeness, as an individual and as a professional
educator. O


The central part of the University of Utah campus viewed from the northwest.
The Merrill Engineering building, glass and aluminum, is below and left of center.

IN department



University of Utah
Salt Lake City, UT 84112

T HE UNIVERSITY OF UTAH, located in Salt Lake
City, occupies 1,500 acres and is bounded on
the east by the Wasatch Mountains. Founded in
1850, it is the oldest and, with a student popula-
tion of about 25,000, the largest institution in
Utah's system of higher education. Its essential
functions are served by a faculty of about 3,500,
with roughly half being regular teaching faculty
and half being adjunct, research, clinical, and
visiting faculty. The governance of the university
includes a Board of Regents and an Institutional
Council (both appointed by the governor) to
whom the university president reports.
The university is a complete university in the

sense that it contains a good library and a set of
professional colleges (including a renowned medi-
cal school) with supporting general education and
scholarly departments, housed mostly in the
colleges of science, humanities, and fine arts. This
proximity allows interesting collaboration among
the diverse professionals and scholars. The Col-
lege of Engineering is one of the eleven academic
colleges and consists of seven departments, one
being the Department of Chemical Engineering.
All seven departments of the college are pres-
ently housed in the Merrill Engineering Building
except for what has spilled over as the college has
outgrown its building space. Research has ex-
panded to fill the newly completed Energy and
Minerals Research Laboratory Building, and a
new classroom building (to be shared with an-
Copyright ChE Division, ASEE, 1985


other college) will be available in about a year.
The spillover will be reabsorbed, and current
needs met.
There are rumors about hazards said to exist
in associating with the University of Utah; name-
ly, the seductiveness of the easily accessible out-
door life in mountains, canyonlands, and deserts.
Other enticements to postpone one's urgent duties
are afforded by the performances of a symphony
orchestra, a ballet company, an opera company, a
modern dance company, and several small theatre
groups. All are resident in Salt Lake City, and
most trace their genesis to the university campus.
The locals tend to euphemize the risk of these
"hazards" by praising the character-building
effects of resisting temptation-but we tolerate
(as we practice) yielding with moderation.


For the present purpose, history is either
ancient (1905-1947) or modern (1947-present).
In 1905, a program in chemical engineering was
first listed among the offerings of the State School
of Mines. The first B.S. in chemical engineering
was awarded in 1907. By the middle 30's the
Chemistry Department was administering the
program, but the curriculum was still listed by
the School of Mines and Engineering.
In 1943 George W. Minard, the first chemical
engineer to be recruited, joined the chemistry
faculty to supervise the chemical engineering
program. Because Selective Service shanghaied
his clientele, he took leave to serve in a local
war industry, returning full time to graduate the
class of 1947, and then resigning.
Modern history begins in 1947 with the fission
of the College of Engineering and Mines into the
College of Engineering and the College of Mines
and Mineral Industries. E. B. Christiansen was
retained as head of the new department of chemi-
cal engineering and was given the choice of
affiliating with either of the two colleges. He chose
engineering and, despite the fact that some of the
top administrators withheld their blessings, hind-
sight has confirmed the wisdom of the choice.
Professor Christiansen, with some initial out-
side help in teaching, first concentrated on recruit-
ing faculty and building a projects laboratory.
Parts of the apparatus were assembled from war
surplus equipment and parts were designed and,
to a large extent, built by undergraduate chemical
engineering students. After two years the labora-

tory was creditable, two new faculty members
had joined the faculty, and 37 new BS degrees
and the first MS degree had been awarded. The
department was ready to apply for accreditation,
applied, and was accredited in 1952.
During "Modern" times, the regular faculty
has grown on the average of one every three years.
Of the 15 members signed aboard, only two have
left, one by resignation and the other by involun-
tary transcendental reassignment. Probably, un-
less the academic charter of the department is
altered, the faculty will not be increased much
more; future recruits will be replacing those who

There are rumors about
hazards said to exist in associating with the
University of Utah; namely, the seductiveness of the
easily accessible outdoor life in mountains,
canyonlands, and deserts.

The department has attained maturity. Its
corporate goals, internally generated, are being
acted on competently; its facilities, and now its
faculty, are in a steady state of evolution; and its
composite personality, which is both varied and
dynamic, is progressive.

There are thirteen live bodies on the active
faculty, eleven regular, one senior research pro-
fessor, and one emeritus still active in research.
Since part of the efforts of several are devoted to
nondepartmental duties, we report only about nine
full-time-equivalent faculty. The thirteen mem-
bers of the faculty (14 including a newly hired
Assistant Professor) have earned their doctor-
ates at ten respected universities. All have ex-
perience in industry and over half have taught
elsewhere at the university level.
With respect to professional recognition at the
national level, one of the faculty, a member of the
National Academy of Engineering, is a past presi-
dent of both the American Institute of Chemical
Engineers and the American Institute of Mining
and Metallurgical Engineers, two have been
awarded the AIChE Founders' Medal, three have
been directors of the AIChE, three are Fellows
of the Institute, and one was the annual Institute
Lecturer for the Institute's Diamond Jubilee year.
One has received the NSF "Young Presidential
Investigators" award.


The spirit has manifested itself in the last seven years in
student paper competition: first place five times, second
Student Chapter Award of Excellence has come to Utah

Two kinds of prized recognition within the
university are the awards for outstanding teach-
ing, five to ChE faculty members, and outstanding
research, three to ChE faculty members.
All but the newest recruits have served in the
less prestigious but important offices and com-
mittees, national or regional, of the Institute,
other professional societies, and governmental
agencies. As is appropriate in a university where
the principle of faculty governance of academic
matters is nominally respected (though some-
times needing defense), all faculty serve, or have
served, on policy, executive, and administrators'
advisory committees.
The present faculty members are: Richard C.
Aiken (Associate Professor), PhD, 1973, Prince-
ton University; Alva D. Baer (Professor), PhD,
1959, University of Utah; Richard H. Boyd (Pro-
fessor), PhD, 1955, MIT; E. B. Christiansen (Pro-
fessor), PhD, 1945, University of Michigan;
Donald A. Dahlstrom (Research Professor), PhD,
1949, Northwestern University; Noel de Nevers
(Professor), PhD, 1959, University of Michigan;
George R. Hill III (Eimco Professor), PhD,
1946, Cornell; Timothy Oolman (Assistant Pro-
fessor, beginning Autumn, 1985), PhD, 1985
University of California, (Berkeley); David W.
Pershing (Professor), PhD, 1976, University of
Arizona; Norman W. Ryan (Professor Emeri-
tus), ScD, 1949, MIT; Dale L. Salt (Professor),
PhD, 1959, University of Delaware; J. D. Seader
(Professor), PhD, 1952, University of Wisconsin;
Edward M. Trujillo (Associate Professor), PhD,
1975, University of Utah; and A. Lamont Tyler
(Professor and Chairman), PhD, 1965, Uni-
versity of Utah.

Aside from striving together for an education
focused on chemical engineering, our undergradu-
ate students rely little on the campus to cultivate
their social life. Most live off-campus, many have
part-time employment in the city, and a signifi-
cant fraction are married. Yet through their
shared experiences in classes and in the under-
graduate seminar, managed by the student AIChE
chapter officers, they develop an impressive esprit

the regional AIChE
place five times, third place four times. The
in seven of the last eight years.

de corps.
The spirit has manifested itself in the last
seven years in the regional AIChE student paper
competition: first place five times, second place
five times, third place four times. The national
Student Chapter Award of Excellence has come
to Utah in seven of the last eight years. The
chapter's advisor, A. L. Tyler, received one of the
National Outstanding Student Chapter Counselor
Awards in 1978 and again in 1983.
Other interesting sightings of the spirit are
made during the annual undergraduate student
vs faculty (plus drafted graduate students)
basketball game, the junior vs senior softball
game, the annual student vs faculty doubles tennis
match (in which the faculty remains undefeated),
and the spring luncheon at which the seniors are
guests of the faculty. On this last occasion the
faculty experiences (and sometimes provokes),
the students' traditional irreverence, which pass-
es from calmly suppressed to delicately expressed.
With respect to statistical demography, we
regularly graduate 35 to 40 students with the bac-
calaureate each year. The numbers of advanced
degrees awarded during the last ten years were
81 Master of Engineering, 27 Master of Science,
and 30 Doctor of Philosophy. Our present facili-
ties and faculty enable us to handle a greater flow
of graduate students.

That the curricula of all the chemical engi-
neering programs in the country are very similar
follows from the wide consensus among faculties
on the essential ingredients of the overall pro-
gram. Outside that core of consensus we find
differences in emphasis, depth, or diversity.
In Utah's chemical engineering, the most
notable instance of emphasis is seen in the three-
quarter senior projects laboratory. Two or three
students, as a team captained alternately by the
members, are assigned eight laboratory projects
during the senior year. An assignment is typical-
ly a design problem which requires that the team
operate laboratory equipment to generate the de-
sign data needed. With assignment in hand, the
team identifies appropriate equipment (or some-




times must assemble it), learns how to use it,
and determines what data to take. Next they
schedule a group oral examination by a faculty
supervisor, and when they persuade him that they
understand the project, they proceed to the final
frustrations: producing the data, using the data,
and writing the report.
In the course of the year's projects, the
student writes three detailed formal reports, and
his other five reports are technical notes or letter
reports. Every report is first read by a non-engi-
neer who grades it for the mechanics of com-
position and sometimes rejects it with sugges-
tions for improvement. When it finally passes
the preliminary reading, it goes to the faculty
supervisor who will judge its form and engineer-
ing content. A late report is downgraded sig-
nificantly. On the other hand, a report reflecting
unusual ingenuity in experiment or design is
awarded a grade bonus.
Another emphasis, perhaps its distinctiveness
already swept away by time's frantic broom, has
been our use of computers in homework and
laboratory instruction. In the laboratory, many
experiments are monitored or controlled by
microcomputers or minicomputers. In most de-
partmental courses, computer time is made avail-
able for the students on the computer center's
mainframe computer, and techniques requiring
its use have become an integral part of the course-
work. Of particular note has been leadership,
through J. D. Seader, in instruction in the use of
large process simulation programs such as
During the final quarter, each student is required
to complete a technical and economic design op-
timization using one of these tools.
We do not treat the diffusional processes col-
lectively as transport phenomena or under other
non-descriptive titles. Rather we share with me-
chanical and civil engineering departments the
teaching of common courses in engineering
thermodynamics, fluid mechanics, and heat trans-
fer. The students' class scheduling problems are
greatly reduced. The required mass transfer
courses are taught only in chemical engineering.
Many students desire some specialization, and
we try to guide them in choosing the appropriate
elective courses. To that end, we have established
several informal options such as living systems,
digital control, and management; or we may ap-
prove alternative schemes of electives proposed
by them.

Four advanced degrees are offered in the de-
partment: Master of Engineering (ME), Master
of Science (MS), Master of Philosophy (MPhil),
and Doctor of Philosophy (PhD). Each aspirant
is limited with respect to which of the degrees he
may apply for, depending on his performance in
a combination diagnostic and screening examina-
tion. This preliminary judgment may be appealed
later on the basis of the student's subsequent per-
The ME degree, design-oriented, is popular
with BS-ChE holders and graduates from related

View in the undergraduate Projects Laboratory.

fields who want advanced treatment of chemical
engineering, with opportunity for further study
in related fields or mathematics. Much the same
can be said for the MS degree, except that it is
research-oriented and it is sometimes a first step
to the PhD.
The PhD is a research degree for which
candidacy is deferred until the aspirant passes a
qualifying examination. That examination takes
the form of preparing and defending a research
proposal in which the prospective candidate is re-
quired to demonstrate originality and independent
thought. The dissertation, with very rare ex-
ceptions, must exhibit an essential experimental

Research in Utah's chemical engineering de-
partment is aimed at the education of degree
candidates, with the faculty's role being maximal-
ly advisory, minimally supervisory. The benefits
of the research in faculty development are regard-


ed as a bonus. Most (if not all) single-author
publications by the faculty have not been de-
signed to present new research findings, but
rather have been intended to be either pedagogi-
cal, critical, or entertaining.

A furnace used in research on air pollutant formation.

The line of research of greatest longevity in
the department has dealt with the rheology of
non-Newtonian fluids, both the characterization
of detailed fluid motion and its use in describing
bulk flow. Related but independent projects have
dealt with two-phase flow, with liquids and solids
distributed in gases, with solids and gases dis-
tributed in liquids, and with fluid mechanics and
heat transfer for flow in curved tubes with and
without chemical reaction. In addition, a study
of the fluctuating boundary layer in nominally
"steady-state flow" was made.
The research having the longest period of
continuous sponsorship, and consequently gener-
ating the largest number of advanced degrees, has
studied the combustion of condensed fuels. The
chief interest has been in the transients of ig-
nition, oscillating combustion, and extinguish-
ment. Much of the effort has involved the burning
of solid composite rocket fuels, and some, the
burning of the polymers and oxidants separate-
ly, with clear relevance to fires. This work quali-
fied the University of Utah to host the Thirteenth
Symposium (International) on Combustion on
our campus in 1970.
The combustion research activity just men-
tioned has diminished in intensity. Meanwhile,
another class of combustion projects has become
the most active. This research involves coupled
experimental and theoretical work on the control
of acid rain pollutants (primarily NO, NO2, SO2,
and SO,) under conditions typical of those found

in coal-fired industrial furnaces, boilers, and
kilns; the direct combustion of biomass fuels; and
the incineration of hazardous industrial wastes in
rotary kilns.
As one would expect in a university so situ-
ated, there is active research, though with a lesser
sense of urgency than expressed a few years ago,
on coals, oil shales, and tar sands. They are
characterized and variously processed to produce
liquid fuels.
A recent subject of research which has been
advanced notably in this department is computer-
aided process synthesis and design. Methods have
been developed for synthesizing multicomponent
separation systems based on considerations of
second-law analysis. Most recently, robust com-
putational procedures based on homotopy con-
tinuation have successfully been applied to inter-
linked separation systems, with the surprising
discovery of multiple solutions. O

If the reader has residual questions about
chemical engineering at the University of Utah,
he is invited to correspond with the chairman of
the department, Professor A. Lamont Tyler.

S9 book reviews

by F. D. Clark and A. B. Lorenzoni
Marcel Dekker, Inc., 368 pages, $32.50 (1985)
Reviewed by
James H. Black
University of Alabama
This book is a revised, updated, and expanded
version of a very successful (six printings) pre-
decessor. It is of particular use in explaining how
to develop and use cost estimating tools, how to
manage and use estimating data, how to avoid
estimating pitfalls, and how to solve estimating
problems. It also covers such topics as the use of
estimates for cost control functions during the
conceptual engineering, the detailed engineering,
and the construction stages of project develop-
ment. With the techniques described in this book,
one can find out how to measure and forecast pro-
ductivity and to control, rather than just report,
costs. The book emphasizes cost estimating and
Continued, next page.




The 1985 ASEE Chemical Engineering Di-
vision Lecturer was Dan Luss of the University of
Houston. The purpose of this award lecture is to
recognize and encourage outstanding achievement
in an important field of fundamental chemical
engineering theory or practice. The 3M Company
provides the financial support for this annual lec-
ture award.
Bestowed annually upon a distinguished engi-
neering educator who delivers the Annual Lecture
of the Chemical Engineering Division, the award
consists of $1,000 and an engraved certificate.
These were presented to this year's Lecturer at
the Annual Chemical Engineering Division Ban-
quet, held at the Georgia Institute of Technology.

A number of chemical engineering professors
have been recognized for their outstanding
achievements. Max Peters was the recipient of the
Fred Merryfield Design Award, given annually
to an engineering educator who exhibits excel-
lence in teaching engineering design, and the
Senior Research Award was presented to Robert
Brodkey in recognition of his significant contribu-
tions to engineering research. Friedrich G. Heffe-
rich, Richard D. Noble, and Richard M. Felder all
received AT&T Foundation Awards, honoring

them as outstanding engineering teachers, while
the Dow Outstanding Young Faculty Award was
presented to Marc Donohue, James M. Peterson,
and Mark E. Davis. The grade of ASEE Fellow
Member was conferred on Ray W. Fahien in
recognition of his outstanding achievements and
important contributions.

The award is made on an annual basis with
nominations being received through February 1,
1986. The full details for the award preparation
are contained in the Awards Brochure published
by ASEE. Your nominations for the 1985 lecture-
ship are invited. They should be sent to Professor
Angelo J. Perna, New Jersey Institute of Tech-
nology, Newark, NJ 07102 (201-596-3616).

The ChE Division officers are: Dendy Sloan,
Chairman; Deran Hanesian, Past Chairman;
Phillip C. Wankat, Chairman Elect; Bill Beckwith,
Secretary-Treasurer; and A. Lamont Tyler, Gary
Poehlein, and Carol Dedrick, Directors.

Two new Divisional awards have been es-
tablished and will be presented at the annual meet-
ing each year. One, the William H. Corcoran
Award, will honor an author for the most outstand-
ing paper published in Chemical Engineering
Education during the preceding year. The second,
the Joseph J. Martin Award, has been created to
recognize authorship of the best paper published
in the proceedings from the prior year.

cost control, two of the more important aspects
of the field of cost engineering.
This book would find application as an ad-
vanced undergraduate-graduate level text in such
courses as Process Design and Economics, Cost
Engineering, Cost Estimating, Project Manage-
ment, Project Control, and Construction Manage-
ment. The first edition has found application this
way since its appearance seven years ago, and this
revised edition will continue that tradition.
Practicing engineers, entering cost estimating for
the first time, would find this book an indispens-
able aid.
For convenience, the book has been divided
into three parts; namely, cost estimating, cost

control, and case studies. Part III, the case studies,
is a collection of ten examples to illustrate the
principles of cost engineering. These case studies
are designed to provide understanding of the
underlying principles discussed in the first two
parts of the book.
The new features of this book include, in ad-
dition to the case studies and the latest develop-
ments and improvements in cost estimating and
cost control, several new aspects of cost engi-
neering so that the book reflects recent advance-
ments in the field. A new chapter on control of
subcontracts has been added because of the in-
creased importance of this topic today. There are
Continued on page 161.



EDITOR'S NOTE: A controversy is brewing on the design content of the curriculum. The questions
are 1) how much design should be required, and 2) how does one define "design"? In order to air these
important questions, CEE is publishing the following two papers. Additional comments are solicited
from our readers.

J views and opinions


Massachusetts Institute of Technology
Cambridge, MA 02139

T HIS CONVERSATION, or something like it, took
place at the San Francisco AIChE meeting
among a group of distinguished professors and
department chairmen of research universities.
"They are making a mess at accreditation (or
choose one from: AIChE, NSF, ACS, ASEE,
NAE, etc.). They are just a bunch of bean count-
ers who do not understand that we should have in-
novations and diversity. And besides, who are
they to tell us that our program is below stand-
ards? Have they ever managed a first-rate depart-
ment themselves?"
"Why don't you do something about it, suggest
changes, organize a group, get involved?"
"I am much too busy with my students and
papers. Somebody else should do it." (i.e., some-
body else not as good as we are, say a politician
who cannot hack it in research and teaching.)
"But these are our own organizations that we
depend on. If we won't fix them, who else would
do it?"
"We can send them an ultimatum, that if they
do not shape up, we will quit."
"We need to send them a detailed blueprint
on how to reform their rotten organization. And
if they cannot do it, we will have to start a new
organization to administer accreditation, to set
up new rules, to train new visitors, and to evaluate
results. That would be even more work than re-
form from within."
"Of course not, that would take too much time
and effort."
"You are mad enough to complain, but not
enough to do something constructive-like volun-
teer for service. Shouldn't we take the time to fix
up our own organizations? No one else would
have the knowledge or motivation to fix them to

James Wei received his BChE from Georgia Tech in 1952 and
his ScD from M.I.T. in 1955. He graduated from the Advanced Man-
agement Program at the Harvard Business School in 1969. He is
presently Warren K. Lewis Professor and Department Head at the
Massachusetts Institute of Technology.

our specifications."
"But that would be politics."
"For instance, the AIChE Council of 17 con-
tains only two professors. The accreditation com-
mittee and the ad hoc visitor list have very few
professors from research universities. We believe
in a trial by a jury of peers, and our peers are
other research universities. If we will not sit on
juries, we cannot be tried by a jury of peers-who
understand us and are sympathetic to us. We
should run for AIChE Council, or volunteer for
ad hoc visitor in accreditation."
"I am much too busy, and I am not interested
in politics."
"But politics affects us, and it has us riled up.
If we are above politics, would we rather be
victims or participants?"
"Let us go to the Exxon suite to drown our
The moral of the story is that it is better to
be mugged than to participate in government, or
isn't it?

Copyright ChE Division, ASEE, 1985




EDITOR'S NOTE: The following paper, authored by the late T. K. Sherwood in 1959 while he was
a faculty member at M.I.T., was sent to CEE by W. H. (Bill) Manogue, a member of the AIChE Educa-
tion and Accreditation Committee. He credits E. L. Mongan, Principal Division Consultant in Du Pont's
Engineering Service Division, for bringing it to his attention.
Professor Emeritus J. Edward Vivian of M.I.T. has written Dr. Manogue that he and Professor Wei
(Head, Department of Chemical Engineering at M.I.T.) have reviewed the manuscript and "while he
agreed with me that Sherwood's conclusion is not current, he felt that as long as the publication ap-
peared with an Editor's note that this was a historical paper written in 1959, he had no objection to

publication of the complete original manuscript."
We are pleased to be able to share this historical

T. K. SHERWOOD (Deceased)
Former professor at
Massachusetts Institute of Technology
Cambridge, MA 02139

T IS SUGGESTED that engineering design can be
taught effectively by introducing design prob-
lems into various theoretical subjects. A sample
thermo problem is presented in detail as the best
means of explaining just how this approach can
be used in a course such as engineering thermo-
If this technique is to be more generally em-
ployed at M.I.T. it is necessary that a large
fraction of the engineering faculty be as inter-
ested and competent in the design aspects of
engineering as they are in the scientific or an-
alytical. The fraction so inclined is perhaps al-
ready too small and appears to be decreasing.

The typical engineering accomplishment of
importance results from a sequence of (a)
recognition of a social need or economic oppor-
tunity, (b) a conception of a plan as to how the
need may be met or the opportunity seized, (c)
an analysis of the merits of the conception and
of the consequences of proceeding with the plan,
(d) the building or construction of the machine,
plant or bridge as conceived, and (e) its opera-
tion. Item (c) is a sort of go no-go step; if the
Copyright ChE Division, ASEE, 1985

document with our readers, with the comments

analysis is discouraging, the conception step and
the analysis are repeated.
"Engineering science" is a phrase which has
come into use in recent years to describe the
analysis step. Good engineers today must be ex-
ceedingly proficient in analyzing a concept;
quantitative mathematical analysis based on first
principles is one of the good engineer's most
powerful tools. But it no more constitutes engi-
neering than any one of the other four activities
listed. In particular, it must be noted that con-
ception ("design") comes before analysis; the
analyst must have something to analyze.
As technology develops, it seems likely that
those engineers who can recognize social needs
or economic opportunities and who can conceive
and plan will be the men most sought after. They
will be the ones who will hire the analysts (engi-
neering scientists), the constructors, and the
operators. To a large degree this is true today.

The concept ("design") abilities of the
student may be developed in at least three ways:
(a) through design courses, planned to meet
the need directly through lectures and exercises
(this is the method used in architecture), (b) by
subjects in which design problems are inter-
woven with the teaching of basic theory, and (c)
by sticking to basic theory and the techniques of
analysis, letting the student develop his own skill
at inventive and conceptual thinking by exposure


The teaching method I have
in mind is best understood by studying
an actual problem assignment. The example chosen
is from engineering thermodynamics.

to the ideas and accomplishments of the great
creative scientists.
The teaching of design by method (a) has not
been well developed, except in connection with
machines, aircraft, and architecture. Method (c)
offers little promise for engineering. My thesis is
that the second method can and should be more
widely used in engineering education.

The teaching method I have in mind is best
understood by studying an actual problem assign-
ment. The example chosen is from engineering
thermodynamics, partly because I teach this sub-
ject, but also because thermodynamics is one of
the best examples of a subject that is often taught
with no element of engineering design. It is a theo-
retical subject involving many abstract ideas and
is normally expected to require rigorous thinking
and exact calculations.

The following is a typical problem assign-
ment to juniors about the middle of the first term
of a two-term course in chemical engineering

Problem 10
A gas well in New Mexico produces essential-
ly pure CO2 at 800 psia and 100'F. The pressure
is reduced to 200 psia by flow through a partially
closed ("cracked") valve and delivered by pipe
line to a plant several miles away. The flow rate is
steady at 10 million ft3/day (reported as ft3 at
60F and 1.0 atm).
The Joule-Thomson expansion through the
adiabatic valve causes the gas to cool. This cold
gas is used to provide refrigeration for a natural
gasoline plant located near the wellhead. The con-
denser to be cooled operates at 60F, and the
minimum temperature difference for heat ex-
change is 5F (i.e., the warmed CO2 leaves at
a) What is the temperature of the CO2 leav-
ing the valve?

b) What is the attainable refrigeration load,
expressed as BTU/hr?
(Comment-note how the instructor has made
this sound like a practical problem by the word-
ing. This is pure camouflage-the solution is
simple and straightforward. The student is not
asked to think-only to know how to use the first
law and the Mollier diagram for CO,.)

From the book, the first law flow equation is
found to be
Q-W,, = Ah
As applied to an adiabatic valve Q and W,
are zero, so the enthalpy leaving the valve is the
same as upstream. This is read from the Mollier
diagram to be 146 Btu/lb CO,. At 200 psia CO,
has this enthalpy at 5F, which is the answer to
At 55F and 200 psia the enthalpy is 158 Btu/
lb, as read from the chart. In the condenser Ah is
158-146 or 12 Btu/lb CO,. From the first law flow
equation as applied to the condenser
Q -0 = Ah
so the refrigeration amounts to 12 Btu/lb CO2
The specific volume of CO, at 60F and 1.0
atm is read from the chart as 9.2 ft3/lb, so the
CO, flow rate is
10,000,000/9.2(24) = 45,300 lb/hr
The refrigeration load is then
45,300(12) = 543,000 Btu/hr
This is the answer to (b).

Now consider the problem so reworded as to
invite the student to look at the design aspects of
the situation.
The CO, flow rate is specified to be the same
as before. The pipe line pressure is 200 psia, as
before. Cooling water is available which can be
used to cool the CO2 stream to 700F. The condens-
er to be cooled now operates at 20F; the cold
gas can be warmed only to 150F so as to maintain
the minimum temperature difference of 5F.
The student is now asked: how much refriger-
ation is attainable from the CO2 stream? How
would the necessary equipment be arranged (i.e.,


draw a flow sheet)?
The routine M.I.T. "A" or "B" student sees the
statement regarding available cooling water,
notes that the feed gas is the only thing capable
of being cooled to 70F, and so refigures the prob-
lem with gas entering the valve at 70F and 800
Enthalpy values from Mollier chart: feed gas,
146; gas at 800 psia, 70F, 126; gas at 200 psia,
150F, 148. Refrigeration is then

45,300(148-126) = 1,000,000 Btu/hr
45,300 (146 126) = 906,000 Btu/hr

are removed by the cooling water. The flow sheet
is shown in Fig. 1.


100 WATER 20F


A second student, probably a "B" or "C" man,
goes through this same calculation, but in doing
so notices that the CO, leaving the valve is
partly liquefied. This is evidently a good thing. If
all the CO2 could be liquefied, there would be a
very large amount of refrigeration. But avail-
able cooling water limits cooling to 70F. The
chart shows that CO2 could be liquefied at 70F
if the pressure were about 865 psia. The well
pressure is only 800 psia. But it should not take
much power to compress the feed gas to 865 psia;
the pump might be expensive because of the high
operating pressure, but would be physically small
because the gas density is high and the volu-
metric displacement low.
The second student's flow sheet is shown in
Fig. 2. The compressor is assumed to operate
adiabatically and reversibly, and the pressure
change is assumed to be isentropic. The first law
gives the flow work as -Ah, which is read from
the chart as approximately 2 Btu/lb. The theo-
retical power required is
45,300 (2)/3412 = 26.7 kw or 35.6 hp
which does not seem like much.
The CO2 now leaves the cooler completely
liquefied at 700F with an enthalpy of only 65
Btu/lb. Ah is zero through the valve, so the re-
frigeration attainable in the condenser is
45,300 (148- 65) = 3,760,000 Btu/hr


800 psia

The student does not know much about the
efficiency or cost of compressors, but he concludes
that even if the actual power were twice the theo-
retical, the compressor installation would appear
to be well worth while in view of the very large
increase in refrigeration attainable.
A third student follows the same reasoning
and makes the same calculations as the second,
but is troubled by the fact that the chart gives
extremely poor precision in reading the Ah of 2
Btu/lb in the compressor. He has learned that if
kinetic and potential energy terms are neglected,
Ah for reversible flow is given as


Reading the chart, he finds the specific volume

200 psa

of the feed gas to be 0.115 ft3/lb and that of the
gas compressed isentropically to 865 psia to be
about 0.105. An average value of 0.11 ft3/lb
cannot be more than 5% in error, so

Ah = 0.11(865- 800) (144/778) = 1.32 Btu/lb

from which he calculates the theoretical (adi-
abatic reversible) compressor power to be 17.5
A fourth student makes the same calculations
as the second or third student, but hates to see
the gas go to the pipe line at 15F. Cannot this
cold gas be useful? Water cooling to 70F certain-
ly was. Using the cold gas to partially cool the
feed gas would only save cooling water. The thing
to do, then, is to use the 15 gas to cool the liquid
CO, leaving the gas-water heat exchanger. His
flow sheet is shown in Fig. 3.
Continued on page 164.


) P.1 laboratory


University of Cambridge
Cambridge, England CB2 3RA

SOME EXPERIMENTS which the author ran in
1980-81 in the University of Edinburgh's
third year chemical engineering laboratory are
shown in Table 1. Fluid mechanics and thermo-
dynamics laboratories are taken separately. This
is the major chemical engineering formal lab,
since the student does research and design pro-
jects in the fourth year of the course. The students
work in pairs, starting at 10:00 a.m. and finish-
ing nominally at 5:00 p.m. (in practice, between
about 3:00 and 6:00 p.m.). The lab runs for two
terms. In the third term of the session the weekly
lab is omitted and there is a 'lab week' instead
where the students devote the whole of one week
to an open-ended short project, such as the de-
velopment of a new lab experiment. This paper
remarks on features of the experiments which
might make them attractive for wider use.

Good convective mass transfer experiments
are hard to find. This writer's experience with
wetted wall columns, for instance, has not been
happy. The purpose of this experiment is not the
study of simultaneous heat and mass transfer,
but the study separately of convective heat and
mass transfer in the same geometry, to allow the
j-factor analogy to be confirmed. The apparatus
was originally a commercial heat transfer experi-
ment, consisting of a 12.5 cm square duct with a
perspex test section, through which air is drawn
by a blower. Transverse rods of 1.25 cm diameter

The purpose of this experiment is not
the study of simultaneous heat and mass transfer,
but the study separately of convective heat and mass
transfer in the same geometry, to allow the
j-factor analogy to be confirmed.

Copyright ChE Division, ASEE, 1985

Topic: Principal Measurement Method; Ancillary
1. Plate Heat Exchanger: Thermocouple
2. Film and Nucleate boiling: Thermocouple; Ammeter
3. Double Pipe Heat Exchanger: Thermocouple; Weigh
4. Single Tube Condenser: Thermometer
5. Heat Transfer to a Jet: Liquid Crystal Sheet
6. Jacketed Pans: Thermometer; Weigh Tank
7. Process Control: Float; Micro-computer
8. Convective Mass and Heat Transfer: Balance, Thermo-
couple; Chart Recorder
9. Continuous Still: Densitometer
10. Continuous Liquid-Liquid Extraction: Titration
11. Drying: Continuous Weighing; Anemometer
12. Filtration: Volumetric Cylinder; Filter Leaf
13. Packed Tower Hydraulics: Manometer
14. Fluidised Beds: Manometer; Weigh Scales
15. Diffusion-Closed System: Gas Liquid Chromatography;
Recorder and Integrator
16. Diffusion-open system: Katharometer; Chart Recorder
17. Measurement of Surface Area of Alumina: B.E.T. Ap-
paratus; Liquid N2
18. Packed Bed Catalytic Reactor: Gas Liquid Chroma-
tography; Recorder and Integrator
19. Adiabatic Batch Reactor: Thermocouple; Micro-com-
20. Enzyme Catalysis: Polarimeter
21. C.S.T.R.: Spectrophotometer
22. Residence Time Distribution Study: Flame lonisation
Detector; Micro-computer
23. Coagulation: Pressure Transducer; Chart Recorder

are introduced through holes in the wall, to simu-
late up to four rows of a heat exchanger tube
bank: all the rods but one are perspex dummies.
The working rod is copper and has a thermo-
couple within it. This rod is heated electrically
and then inserted into place at the start of the ex-
periment. From its cooling curve the gas-rod heat
transfer coefficient is deduced, and the experi-
ment is repeated for different air velocities and
test-rod positions. Measured pressure drops are
also logged. Next, the mass transfer runs are per-
The adaption to mass transfer work exploits


method are reported elsewhere [3, 4].


Bill Paterson lectured at Edinburgh after taking his BSc and
PhD there. He has been a development manager with I.C.I. Petro-
chemicals Division and is now a University Lecturer in chemical
engineering and Director of Studies in chemical engineering at Corpus
Christi and Sidney Sussex Colleges, Cambridge. His research interests
include chemical reaction engineering, packed bed operations, flow-
sheet simulation and process synthesis.

Macleod's swollen polymer method [1, 2]. A thin
film of commercial silicone rubber is deposited on
the surface of the mass transfer working rod.
This is swollen to equilibrium with some suitable
volatile agent, e.g. ethyl salicylate. When the rod
is placed in the air stream the agent evaporates.
There is a constant rate drying period during
which the partial pressure of the swelling agent
immediately above the polymer is sensibly con-
stant, equal to its saturated vapour pressure at
the air temperature, and the controlling mass
transfer resistance is rod-gas convection; diffu-
sion through the polymer does not intrude. Inter-
mittent withdrawal and weighing of the rod both
establishes the mass transfer rate (and thus the
mass transfer coefficient, for the partial pressure
of swelling agent in the bulk gas is virtually zero)
and confirms that the test is within the constant
rate period. The rod can then be immersed in a
test-tube of swelling agent for re-swelling to
equilibrium, while a different test rod, ready pre-
pared, is used for the next run. Since saturated
vapour pressure is sensitive to temperature, it is
important to measure the air temperature with
more accuracy (e.g., 0.1C) than the heat
transfer experiment requires.
The transfer coefficients are then nondimen-
sionalised, to show that the restricted j factor
anology, j, = jH, holds, while the presence of form
drag falsifies the complete j factor analogy jD =
JH = f/2, where f is the friction factor. Alterna-
tive swelling agents, appropriate values of satur-
ated vapour pressure and diffusivity, and other
simple experiments using the swollen polymer

A flat horizontal sheet of plastic, of area A,
incorporating a commercial liquid-crystal temp-
erature-sensitive film, is heated from below by
direct contact with an electric heating mat. The
relation between sheet temperature and colour is
established in preliminary experiments. The mat
sits on insulating material so that all its power,
W, measured as current times voltage, passes
through the sheet. The sheet quickly reaches a
thermal steady state, so that, in still air, it has
a uniform colour. A round, laminar air jet is then
aimed at the centre of the sheet, normal to its
surface. Then, since the solid-air heat transfer

Good convective mass transfer
experiments are hard to find. This writer's
experience with wetted wall columns, for instance,
has not been happy.

coefficient, h, varies with position, r, so does the
surface temperature of the film, Ts, and coloured
rings appear on the film. The heat transfer co-
efficient, as a function of r, is calculated from
h(r) = W/A[T-T,(r)]
and compared with theory [5]
Nu(r) = 0.159 Prl/Rea/4(d/r) 5/4
where d is the diameter of the jet.
The experiment is repeated with a square jet
for which no theory exists, and the students ex-
plore the unexpected and interesting results. An
improved and abbreviated (two hour) form of
this experiment has been transplanted to the
second-year fluid mechanics and transport pro-
cesses lab in Cambridge. Details may be had by
writing to Mr. N. MacFadyen.

Usefully accurate gas diffusivity measure-
ments can readily be made in a Stefan experi-
ment [6] where evaporation rates are measured
from a long-necked flask. However, this experi-
ment does not involve the direct measurement of
concentration profiles and is consequently found
unsatisfactory by some students. The two ex-
periments used in this lab are selected to remedy
this defect, to show the difference between equi-
molecular counter-diffusion and diffusion through


a stagnant film, and to introduce the student to
some moderately heavy mathematics and to some
analytical instruments.
The counter-diffusion experiment is Cover's
[7]. About 5 ml of, e.g., acetone vapour is injected
through a septum near the bottom of a vertical,
lagged sealed glass tube (length ca. 60 cm, i.d.
2.5 cm) containing, as host gas, nitrogen traced
with 3% ethane. A subsequent series of analyses
of samples withdrawn (by 100 [l gas-tight
syringes) at two sample points each located at
one-sixth of a tube length from an end permits
determination of DAB, the diffusivity of the va-
pour in nitrogen. The acetone concentration in
counter-diffusion is described by the diffusion
equation (Fick's second law)
at DZ2
with t = 0, CA(Z) = CAO(Z)
Z = 0,L, ?CA/DZ = 0
where Z is the axial coordinate, t is time, and
L is the tube length. The solution for t > 0 is
obtained by separation of variables

CA(Z,t)=Ao+ Ak exp k DAt cos kZ
k=l L L
where the values of the coefficients Ao A. de-
pend on the initial concentration CA(Z), that
is, on the particular Z-wise concentration profile
set up on completion of injection (t = 0).
Taking the difference of concentration be-
tween two points at the same time, the even
terms cancel and the odd terms double. The lo-
cation of the sample points causes the term in A,
also to vanish, while the decaying exponential
factor causes the terms in A, and higher to be
negligible for all but the shortest times. Hence
[CA(1/6 L,t) -CA(5/6 L,t)]
is proportional to

exp[- -Z DABt]

Thus the slope of a plot of the logarithm of
that concentration difference against time yields
DAB. The unknown and unimportant A1 is includ-
ed in the intercept. Since a difference in vapour
concentration is required, considerable error
would result if the sample volumes were not
identical. The purpose of the ethane tracer is to
permit correction for differing sample volumes
by use of the areas of the ethane peaks from the

GLC. Note that calibration of the GLC is un-
necessary so long as peak area is proportional
to the moles of species in the sample, since ace-
tone peak areas (corrected using ethane peak
areas) may be used in place of molar concentra-
tions in the difference term above: the intercept
of the plot changes, but not its slope.
The stagnant film experiment is Crosby's [8].
Here the film is arranged to be very thick-it
occupies a diffusion cell about 0.4 m high. A pile
of discs with a hole in each is assembled on a
central pivot and can be arranged so that the holes
are in line to form a vertical tube. At the bottom
a reservoir carries a volatile liquid, e.g., acetone.
At the top a cap has a stream of nitrogen flowing
through it. It is assumed that the concentration
of vapour at the bottom is due to the vapour pres-
sure at room temperature; at the top it is always
zero. Starting with nitrogen only in the system,
vapour is allowed access at zero time. At any sub-
sequent time, t, vapour will have diffused towards
the top. At time, t, alternate discs are rotated to
isolate each section of the cell. A stream of nitro-
gen is used to flush out each section in turn and
a quantity proportional to the vapour mole frac-
tion is determined by a thermal conductivity cell
katharometerr) attached to a chart recorder. The
shape of the vapour concentration profile is thus
The only important modification from Crosby's
design is that 'O'-rings were recessed into the
horizontal faces of the dural discs to seal them
adequately. The mathematics is laid out in BSL
[9]. In contrast to the 'long time' analysis above,
the analysis here is for 'short' times so that there
is no breakthrough of acetone into the top cell.
Then a semi-infinite boundary condition is used
(Z = co, CA = 0), and solution is effected by
Boltzmann's transformation or by Laplace trans-
form. The text is careful to draw attention to the
error which could occur by naive application of
Fick's second law. The measured value of diffu-
sion coefficient may be compared with that from
the experiment above.


An exothermic batch reaction is performed
batchwise in a stirred Dewar flask, with progress
followed by measurement of temperature, as de-
scribed by Williams [10]. However, in addition
to the reactions he recommends (sodium thiosul-
fate with hydrogen peroxide, and acetic anhy-


dride hydrolysis), there is provision for study of
the acid-catalysed hydrolysis of propylene oxide
to the glycol [11]. Assuming that this reaction is
pseudo zero order in H20, which is in great excess,
and nth order in propylene oxide, the heat and
material balances yield the variation of tempera-
ture T with time t

1 dT C0 )-1 Aexp(-E/RT)
(Tf-T)" dt \T,-

where subscripts f and 0 imply final and initial.
For an assumed value of n, the values of the pre-
exponential factor, A, and the activation energy,
E, may now be estimated either by (a) numeri-
cal/graphical differentiation of the measured T
vs t curve followed by plotting the logarithm of
the L.H.S. versus 1/T [10] or (b) by a numerical
integration method [11] in which experimental
errors tend to be cancelled rather than amplified.
Both of these methods are readily programmed
for the microcomputer which logs the T vs t
curve (receiving a thermocouple signal ampli-
fied and digitised by a DVM). Also programmed
is an ordinary differential equation (o.d.e.) inte-
gration routine which permits integration of the
o.d.e. above with the estimated values of A and E
and the assumed value of n. Thus the student can
plot the predicted T vs t profile to compare with
the experimental values, and choose the value of
n (from, say, 0, 1/2, 1, 2) which gives the best fit.
It is also possible then to predict profiles for
different initial concentrations (Co) or tempera-
(To), and so to find initial values which will lead
to very different predictions of the profile for
different assumed values of n. A second experi-
ment allows easy discrimination of the best value
of n [11].
A particular advantage of this reaction is that
the order of reaction with respect to catalyst con-
centration, CH+, is easily found. From the o.d.e.,
writing A'CH+m for A,

J (Tf-T) exp(-E/RT)

Sf T A'C11 dt

( (o n-1 A'CH m t1
Ti To

Consider two runs using different values of CH+
but the same initial values Co, To, and hence the
same final temperature Tf. Choose some con-
venient intermediate temperature Ti and note
the corresponding values of ti for the two runs.
Now, the LHS is the same for both runs. So
(CH.+ ti)
is constant too, so that the two pairs (CH+, ti) im-
mediately yield the value of m. As far as is
known, this result is new. The values of n, m,
E, A' obtained agree well with the literature
[11, 12].

The packed tower hydraulics experiment is a
conventional study of loading and flooding in two
six-inch diameter towers, one packed with
Raschig rings and the other with glass helices.
However, it has one pleasing feature: the first
tower floods first at the top, followed by the flood-
ing moving downwards, whereas the second floods
at the bottom and the flooded zone grows up-
wards. The cause of the former is presumably
that the gas volumetric flow is highest at the top:
of the latter, that the helices compress readily,
so that the bed voidage is least at its base and
resistance to flow is highest there. A remarkable
number of students don't notice.
The packed bed catalytic reactor is used to
study the dehydration of 2-propanol to a mixture
of propylene and di (2-propyl) ether over an
alumina catalyst: this reaction is only mildly
endothermic so that reactor isothermality may be
assumed, the reactor and the feed preheater being
in an oven. Catalyst particles are so small that
pore diffusion limitations do not occur.
The enzyme catalysis experiment is performed
in a batch reactor made by modifying a spinning
catalyst basket reactor of the Carberry type.
Glucose is converted to fructose by an im-
mobilised enzyme "sweetzyme Q" manufactured
by Nova A. S. of Copenhagen, used at 60C and
pH = 8.5. The constants in the Michaelis-Menten
kinetic expression are determined. The rotational
speed of the basket can be varied from run to run
to permit investigation of external mass transfer
effects. El

This lab was assembled as a team effort, so
Cnotinued on page 160.





0. M. KUT1, R. QUERALT2,
1Swiss Federal Institute of Technology (E.T.H.)
Ziirich, Switzerland.
2Instituto Quimico de Sarria, Barcelona, Spain.

ITH THE INCREASING amount of published in-
formation and improved methods of assessing
this information, there is a new awareness within
chemical engineering that systematic information
retrieval from the literature is an important start-
ing point for any type of project. To match this
awareness (already prevalent in industry),
chemical engineering courses should include some
instruction in the subject of information science.
There is more to information retrieval than
simply knowing where the library is and knowing
how to use an index. It is possible to give students
a more thorough background in information
science in a comparatively short course-if it is
well organised. The objective of this paper is to
indicate the possible contents of such a course and
to relate some experiences already gained in teach-
ing the subject to chemical engineering students.

A modern information and documentation
course for chemical engineers should cover print-
ed bibliographic information, numerical data, and
methods of computer retrieval, both of numerical
and bibliographic data.

Available Printed Information
Traditional literature searching has always
concerned itself with searching the scientific
journals-the primary publications. Since chemi-
cal engineering is a mixed discipline, it is often

*This paper was commissioned by the European Federa-
tion of Chemical Engineering, Working Party on In-
formation and Documentation.

The objective of this paper
is to indicate the possible contents
of such a course and to relate some experiences
already gained in teaching the subject to
chemical engineering students.

worthwhile to look in other specialized areas for
relevant material-statistics, operations research,
chemistry, mechanical engineering, computing,
and electrical engineering all overlap with various
chemical engineering subjects, particularly at the
research level.
Primary literature goes beyond the published
journals; conference pre-prints, dissertations, and
patents all belong to the primary literature, but
are more difficult to obtain than the international
journals. The difficulty in obtaining these very im-
portant publications is overcome by the develop-
ment of the secondary publications.
The secondary publications are abstracts of
the primary literature, the most famous of which
is Chemical Abstracts. Chemical Abstracts is so
important to the chemical engineer that he should
be able to use it without difficulty, understanding
the concepts of its indexing and registry numbers
for components. Chemical engineering has some
lesser known abstracts of its own: Theoretical
Chemical Engineering Abstracts (POB 146, Liver-
pool, England), Chemical Engineering Abstracts,
(University, Nottingham, England), and DE-
CHEMA, (PF 970 146, D-6 Frankfurt-97, W.
Germany). Abstracts in overlapping fields
(INSPEC for mathematics and control, Engineer-
ing Index for heat exchange) can also be useful.
Under secondary publications one can also list
the Science Citation Index (SCI) which enables
forward searches to be made, and the ISI weekly
publication of contents pages of the scientific
journal, Current Contents, enabling the contents
of most of the recent journal issues to be effective-
Copyright ChE Division, ASEE, 1985






ly followed.
Finally there is the tertiary literature. This
is an organised summary of the literature in each
particular field: handbooks, monographs, data
collections, and textbooks. Perry is, of course, the
most important. Then there are the encyclo-
pedias of chemical technology of Kirk-Othmer and
Numerical data are very important to the
chemical engineer, and these are generally found
in the tertiary publications. General data con-
cerning chemicals are best covered by Beilstein
(organic) and Gmelin (inorganic). Though both
these works were in German, new editions are
now in English. Other publications concentrate
on particular properties.
Finally there are the monographs and text-
books. They often provide an excellent starting
point for any search by summarizing the particu-
lar technology up to a certain point in time-which
is often adequate for the needs of many problems.
The graduating chemical engineering student
should be aware of these facilities in his library.
He should be able to carry out searches in Chemi-
cal Abstracts, know where to obtain numerical
data, know how to use the subject and author
catalogues in the library, and know that the li-
brarian is a trained professional, there to help
him when he has difficulties.

Computer-Stored Information

Bibliographic Data Bases: The history of the
development of computer readable bibliographic
data bases is a fascinating opening to the subject

Oemer Muhan Kut received
his M.Sc. and Ph.D. degrees in
chemical engineering from the
Swiss Federal Institute of
Technology (ETH) in Zurich.
Since 1972 he has been a re-
search associate at ETH. His
major research interests are in
the areas of applied catalysis,
catalytic reaction engineering,
and modelling of multiphase
reactors. (L)
Rafael Queralt received his
diploma in chemical engineer-
ing from IQS and since 1963
has been an assistant professor at the Instituto Quimico de Sarria.
He is also head of the Library and Documentation Services at IQS,
which is a pioneer centre of automized chemical information in Spain.
L. Murray Rose has a B.Sc. and a Ph.D. in chemical engineering

of the production of SDI (Selective Dissemination
of Information) tapes. To rationalize the pro-
duction of the printed abstracts, the total ab-
stracts were coded onto magnetic tape. It was then
a small step to the distribution of these tapes to
institutions wishing to perform their own
searches electronically rather than waiting for
the printed versions to be posted and going
through them manually!
It is interesting for most chemical engineers
to know the principles on which the computer
searching is done. The availability of the ab-
stracts on tape, the need to have a thesaurus and
to invert the SDI tapes to be able to recover
which abstracts refer to each particular keyword
are important points to explain in the course.
There is a growing feeling among informa-
tion scientists that the engineer himself should
understand how computer searches are done. The
need to choose the individual keywords carefully
and to define a suitable search strategy, to know
the pitfalls of not including enough alternative
descriptions, and to know how to improve the
relevance by including further keywords. It is
particularly important that the chemical engi-
neer know which data bases are likely to be of
most use to him. Surveys in Europe have shown
Chemical Abstracts to be the most useful (al-
though it is far from ideal for most chemical engi-
neering problems). Chemical Abstracts needs
backing up with COMPENDEX or INSPEC,
where appropriate. Besides these three there are
many other data bases covering particular areas
of use to chemical engineers-part of the NIH-
EPA Chemical Information System for safety

from Birmingham University. Before joining the Systems Engineer-
ing Group of the Technical Chemistry Laboratory of the Swiss Federal
Institute of Technology (ETH) in 1971, he spent twelve years in in-
dustry. His efforts are toward instigating the sensible use of com-
puters in all branches of chemical engineering. (R)


and chemical properties, DERWENT for patents,
PREDICAST for commercial information, DE-
CHEMA for equipment design and corrosion
problems, etc. The undergraduates should be
made aware of the scope and limitations of the
various fields.
It is also good for the undergraduates to be
informed on the component parts of the computer
literature searching system-the abstractors, the
files and inverted files, the hosts, the communica-
tions networks-that all need paying for every
character retrieved. And then, the multitude of
Numerical Data Banks: Parallel to computer
retrieval of bibliographic data, banks of physical
properties for use by chemical engineers have

The subject would be
given more status if it were a
short course in its own right, and not
simply squeezed into odd hours.

been developing and are now generally accessible
by any terminal connected to the telephone net-
work. Most normal chemicals in commerce
(-800) are now available on these banks which
store numerical physical property data, or use
predictive methods to give estimated values for
those not available. PPDS, EPIC and DECHEMA
systems are available in Europe, and PPDS in the
For teaching purposes, a number of small
demonstration banks exist. CHEMCO is probably
the most widespread. There is no better way of
making a student realize that these modern tools
are available to him than to let him use them
during a design project.
Such data banks could be handled in an in-
formation and documentation course or in a
thermodynamics course, since they are excellent
for demonstrating enthalpies, chemical equilib-
rium, vapour-liquid equilibria (VLE), and equa-
tions of state. For them to be handled in both
courses would have the advantage of helping inte-
grate the whole curriculum.

There are two fundamental types of litera-
ture searching
Retrospective searching, where a comprehensive
list of relevant literature published on a special
topic is sought

*Current awareness searching (SDI = Selective
Dissemination of Information), where the interest
concerns the current publications on the topic under

The selection of information sources and the
mode of information retrieval will depend on the
type of search. For starting a systematic litera-
ture search, the problem and its limitations should
be clearly defined. In manual as well as in on-line
searches, the effectiveness of the study depends
on how well-prepared the search strategy is. To
get some experience in strategy preparation and
optimization, the library users should practice
manual searching techniques before starting on-
line searches.
A very useful start for undergraduate students
in chemical literature are small search exercises
in Chemical Abstracts using the printed indexes.
The user should become familiar with the Index
Guide and the Chemical Substance Index using
the Chemical Abstracts nomenclature. He should
also learn the concept and the limitations of the
Registry Numbers. These numbers, characteriz-
ing a single, well-defined chemical compound,
build a link between different bibliographic and
numerical data banks. The user should also prac-
tice how to select relevant keywords with all their
synonyms and truncations. He should also be
familiar with the linking concepts (and, or, not)
creating combinations of sets selected by the key-
words. For narrowing the search strategy the
user should also be aware of other possible limi-
tations such as language, document type, country,
or publication year.
Even with all these preparations, electronic
information retrieval continues to be a difficult
task for the average user without the assistance
of information specialists. For example, the
Chemical Abstracts (CA) SEARCH files are ac-
cessible from many host systems such as Lock-
heed, SDC, or Data Star. However, every host
system has its own software and its specific ad-
vantages and disadvantages, making different set
combinations and search strategies possible. The
fine structure of the programs are developing. An
average end-user making only a limited number
of on-line searches cannot be aware of all the pro-
gress made to reduce the search costs. Although
development in the direction of "user-friendly
systems" is progressing, at the moment the op-
timal combination seems to be co-operation be-
tween the information specialist who knows the
information systems and the end-user who knows


the extent of his information requirements, so
that the on-line systems can be used efficiently as
an interactive system adapting the search strategy
to the given information. This need for teamwork
between the information specialist and the engi-
neer is ground enough for the undergraduate
engineer to be made aware of the principles of
information retrieval.

Experience in the Swiss Federal Institute of
Technology (E.T.H.)
In common with many other universities, the
time-table structure at E.T.H. makes it virtually
impossible to introduce new courses, so modern
methods of information and documentation have
to be squeezed into two hours borrowed from an-
other course, with practical exercises carried out
as part of a semester project. The introduction to
the semester project enables an additional two-
lecture-hours on manual searching to be given.
Because the particular semester project is con-
cerned with literature retrieval (four days), the
students get ample practical experience on manual
searching. The total of four lecture hours (which
includes a computer search demonstration) is not
really adequate to properly cover the material-
six to eight hours would be better. The four-day
manual search project is more than necessary for
the normal chemical engineering student. How-
ever, in the Technical Chemistry Department at
E.T.H. there is a strong emphasis on chemistry,
which is consistent with extended information re-
trieval exercises.
The subject would be given more status if it
were a short course in its own right, and not
simply squeezed into odd hours. This could con-
veniently be taught together with odd hours given
on communication (report writing, specification
writing, drawing standards, speaking and lectur-
ing) to provide sufficient material for an inde-
pendent course on communication.
Undergraduates do not carry out computer
searches, but postgraduates are allowed to carry
out some of the searches by computer in collabora-
tion with an information specialist.

Experience at the Instituto Quimico de Sarria
Since 1979 the Higher Technical Education
Centre for the formation of engineers has pro-
vided a course on Scientific and Technical Docu-
mentation for the fifth-year students (the last


The ChE Department at Virginia Tech wishes to invite ChE edu-
cators to attend the Frank Vilbrandt Memorial Conference on Chemical
Process and Plant Design. The Conference is scheduled in celebration
of the 50th anniversary of the founding of the ChE Department at
Virginia Tech and will be held on October 10 and 11, 1985. Further
information can be obtained from Y. A. Liu, ChE Dept., Virginia
Tech, Blacksburg, VA 24061.

year of the chemical engineering curriculum). It
is compulsory for those students who opt for the
research course, at the end of which a Trabajo de
Fin de Carrera (final report on conclusion of
studies) has to be submitted before the degree
(in chemical engineering) can be awarded. It is,
however, optional for those students who do not
go for this research course and who will conse-
quently not complete their studies with this de-
The course is run for one week with two hours
every day, giving a total of ten hours for the
presentation of the various topics. The exercises
are done on an individual basis outside the regu-
lar course time, which means an average extra
time requirement of three hours for the practical
exercises. In the presentation of the material,
emphasis is put on practical application, the im-
portance of one-line systems demonstrated, and
extensive use of visual material like slides and
transparencies is made. The course contents are
remarkably similar to Table 1, which is the pro-
posed curriculum we are recommending.
The experience with this course during the
last five years has been highly positive. The
students have learned or improved their ability
to handle basic documentary sources (like Chemi-
cal Abstracts, Beilstein, Science Citation Index).
They know the possible ways of using information
media in their search for information, how to ac-
cess them, and finally, and this is very important,
they realize the complexity of the process for
searching for information and are aware of the
assistance available from the specialist in in-
formation and documentation.

The European Federation of Chemical Engi-
neering has had a Working Party on Information
Continued on page 142.





Cornell University
Ithaca, NY 14853

T HE USE OF COMPUTER graphics to aid and im-
prove the teaching of chemical engineering
principles is an area of growing interest. Many
topics have the potential to be greatly improved
by utilizing the special capabilities of computer
graphics, with rewards such as greater instructor
efficiency and additional aid for educationally
weaker students. One such topic is the teaching
of staged operations, usually conducted within a
separations course. For studies involving distilla-
tion-the single most important separation tech-
nique-the graphical method of McCabe and
Thiele [1] is typically employed due to its con-
ceptually simple formulation. However, the
manual calculation of a single McCabe-Thiele
plot for one case study is a lengthy and laborious
procedure, as any junior will attest! In order to

investigate the effect of different design param-
eters on the resulting column, this time-consuming
procedure must be repeated for each new case.
The repetition involved is of limited educational
value, yet it is most important that the student
have a firm grasp of the interrelationship be-
tween the various operating parameters, e.g., the
reflux ratio and the condition of the feed. The
usual result is that a severely restricted number
of cases can be studied, with additional limita-
tions on the complexity of the system. The results
of other interesting designs must be presented to
the student already complete, dulling the sense of
discovery that their investigation might have pro-
duced. Computer graphics offers solutions to
these problems, removing the burden of compu-
tational effort while preserving the simple graphi-
cal representation which allows a ready compre-
hension of the situation. These advantages were
recognized by Calo and Andres [2]. However, their
McCabe-Thiele package was devised around the
older technology of direct view storage tube
graphics, which is unsuitable for interactive use.

Maryam Golnaraghi is cur-
rently a Ph.D. candidate in the
Theoretical and Applied Me-
chanics Department of Cornell
University studying non-equi-
librium properties of granular
materials using statistical me-
chanics. She received her B.S.
degree in Chemical Engineer-
ing at Cornell in 1984. (L)
Paulette Clancy is current-
ly an assistant professor in
chemical engineering and as-
sociate director of the Manu-
facturing Program at Cornell
University. She received her BS degree at the University of London
and a D.Phil. degree at the University of Oxford. She held fellowships
at Cornell University and at London University before joining the
faculty at Cornell in 1984. (C)
Keith E. Gubbins is currently the Thomas R. Briggs Professor of
Engineering and director of chemical engineering at Cornell Uni-
versity. He received his BS and PhD degrees at the University of

London, and was on the staff at the University of Florida from 1962-
76, when he moved to Cornell. He has held visiting appointments at
Imperial College, London, at Oxford University, and at the University
of California at Berkeley. He has co-authored two books, Applied
Statistical Mechanics (Reed and Gubbins) and Theory of Molecular
Liquids (Gray and Gubbins). (R)
Copyright ChE Division, ASEE, 1985


Computer graphics offers solutions to these problems, removing the
burden of computational effort while preserving the simple graphical representation which
allows a ready comprehension of the situation.

In the graphics package developed at Cornell,
the software was written for a sophisticated
vector refresh graphics workstation offering su-
perior interactive capabilities with virtually im-
mediate response to user-interaction. This pack-
age was implemented in the fall semester of 1984,
and will be used in our separations course.

The Computer Aided Design Instructional
Facility at Cornell's Engineering School has been
described in an earlier publication [3]. Of the
graphics workstations available, a vector refresh
Evans and Sutherland Multipicture System was
chosen for this application since software ex-
pertise for this type of system was available with-
in the department. However, the nature of the
application is such that it could equally well have
been set up on a raster graphics system; indeed,
the programs have been structured for such a
change if necessary. User interaction with the
package was made possible largely through the
use of an electronic tablet and stylus (or pen),
with a VT100 terminal for alphanumeric input.
An electrostatic plotter was available for 'hard
copy' output of the contents of the screen, a use-
ful feature for the preparation of homework as-
As with the graphics package to represent
phase diagrams developed at Cornell [3], the ap-
pearance of this software package was carefully
conceived so that the design criteria given below
would be fulfilled in the most effective and invit-
ing fashion-in other words, in what computer
scientists like to call a "top-down" approach. The
objectives of the software package were
For a complete set of user-supplied variables de-
scribing the system, a McCabe-Thiele plot should
appear on the monitor's screen, together with a
scaled diagram of the resulting distillation column.
Interaction with the software package to change
any of the design parameters should be easily
effected and should produce an almost instantaneous
response in recomputing the McCabe-Thiele plot
and the design of the column, redisplaying them
on the monitor. This interaction should be designed
so that qualitative trends in column design result-

ing from parameter changes could be viewed almost
continuously if desired, or that specific values for
these parameters could be entered if a quantitative
calculation is required.
Extensive help must be available to aid the con-
fused, while the ability to restore the original screen
display is essential for the computationally en-
tangled. Instructive messages should appear on the
screen to inform the user of the program's status--
for example, if some unavoidable delay in process-
ing the input is about to occur.
The program must be structured in such a way
that its extension to more complex problems can be
incorporated into the existing software in a straight-
forward manner. Thus, some long-range planning
of the possible modifications to the package had to
be considered.
As far as possible the software produced should
be portable, so thought had to be given to pro-
ducing a machine-independent code. The decision
to write the software in FORTRAN, still the most
widely used high-level language in engineering,
stemmed from this desire.
Last, but still important, the programs should be
"bomb-proof," even for the most inventive student
user! The most likely input errors, or miskeying,
must be anticipated wherever possible.
Should these objectives not be met, resulting
in a final product that was difficult or frustrating
to use, much of its educational impact would be
lost. Such attention to detail in designing the ap-
plication graphics package is extremely time-con-
suming in terms of software development, but the
effort is amply recompensed once its use is es-
tablished as a regular component of the course.

We believe that the final product does indeed
meet the criteria given above, satisfying both the
instructor's and the student's differing needs. It
is a routine matter to produce numerical sub-
routines performing the calculations for the Mc-
Cabe-Thiele plots, but more time-consuming to
incorporate the graphics software to display an
aesthetically pleasing picture on the screen and
an ergonomically attractive interaction with the
displayed image.
The layout for the display is as shown in Fig.
1. The master object displayed consists of a Mc-
Cabe-Thiele plot with appropriate equilibrium
and operating lines and the "ladder" of stages.


This is supplemented by a scale diagram of the
corresponding design for the distillation column
(relative to a six-foot tall 'stick figure' standing
beside it). Above these diagrams information
about the current values of the various operating
parameters is displayed, while the space below is
reserved for the "menu." The menu provides a
selection of options to enable the user to interact
with the viewed image. The user may select a par-
ticular option by moving the pen across and slight-
ly above the tablet until the cursor (in the form
of crosshairs on the screen) lies within the re-
quired area (or window) designated for this
option. Pressing the tip of the pen down in con-
tact with the tablet activates the window to per-
form a specific task.
The menu options for interacting with the
package are listed below (the window names are
in bold face type)
1. Six windows allow input of both the com-
position and the flowrate of the feed, distillate, and
waste product. The program will prompt the user
for values of any four independent variables from
these six in order to completely define the prob-
lem. Values are entered by placing the pen down
at some point within the window. Each window
contains a potentiometer which allows the value
of the appropriate variable to decrease or increase
as the pen is moved left or right across the
window. The value given by the current position
of the pen may be read in the area above the
2. When the calculate window is selected, the
program checks to see if the mass balance was
satisfied by the user-supplied variables. If the
mass balance was not satisfied the user is in-
formed and will be prompted to re-enter all four
values. In this way the programs assure that the
student is capable of performing the mass balance
correctly. Assuming all is well, a McCabe-Thiele
plot is produced for "start-up" values of the
operating parameters, e.g. the reflux ratio.
3. The user may now alter these operating
parameters by selecting appropriate windows for
the reflux ratio, operating pressure and heat per
mole of feed. Again, moving the pen along the
length of the window alters their respective
values with immediate response from the pro-
grams, producing altered images for the McCabe-
Thiele plot and column design.
4. If the user desires to set an exact value
for any variable this can be done using the key in
option. This offers an alternative to using the po-


tentiometers within the windows, which are
more suited to observing qualitative trends in the
behavior of the McCabe-Thiele plot. The 'key in'
feature prompts for numerical input at the VT100
5. The reset window sets all the flowrates and
compositions to zero and the operating paramet-
ers (p, R and q) back to their initial preset values.
6. The window marked economical analysis
allows the user to determine the optimum value
of the reflux ratio in cost effectiveness. This will
be explained in more detail in the following
7. Snap triggers the production of a paper
copy of the current screen contents on a nearby
8. Help invokes the display of information
pertinent to the operation of each of the windows
in turn.
9. Exit halts execution of the program.

The McCabe-Thiele method is widely used as
an educational tool in teaching distillation column
design at the undergraduate level, and details of
the method need not be repeated here. In the
existing version of the program, a single column
involving only one feed of a binary mixture of
components is considered. Extension of the pro-
grams to multiple feeds and sidestreams is under-
way. The feed may be introduced into the column



0 e Rt

in any fluid condition (i.e., saturated liquid, sub-
cooled liquid, etc). Antoine's equation is used to
obtain the saturated temperatures and pressures
of both components, and the x-y equilibrium
curve is obtained assuming ideal behavior. Op-
tional consideration of a variety of non-ideal de-
scriptions of the equilibrium curve is also
Routines are included which calculate the di-
ameter and height of the distillation column for
each case study in order to produce the scaled
diagram described earlier, including the correct
number of bubble-cap trays, a total condenser,
reboiler, and the location of the feed tray. This
is achieved by following the recipe outlined in
Treybal [4].
Some interesting aspects of column design
with regard to the economics involved are also in-
corporated by allowing the preparation of a graph
showing the relationship between a given reflux
ratio and the total cost involved, considering both
capital costs and estimated running costs over the
expected lifetime of the column. The minimum
of this parabolic curve allows the estimation of
an optimum reflux ratio for the most cost-effec-
tive operation of the column.

The implementation of the computer graphics
package described has proved to be of consider-
able assistance in the teaching of staged opera-
tions. Instructors benefit from the increased
quantity and complexity of problems which can
be investigated in the allowed time, and students
welcome this novel and easy-to-use tool which
makes completing their assignments so much less
onerous. D

M. G. would like to thank C. D. Naik and G.
Charos for many helpful discussions. It is a plea-
sure to thank the Gas Research Institute for
practical support of this work.

1. McCabe and Thiele, Ind. Eng. Chem., 17, 605 (1925).
2. J. M. Calo and R. P. Andres, Comp. in Chem. Eng., 5,
197 (1981).
3. C. D. Naik, P. Clancy and K. E. Gubbins, Chem.
Eng. Ed., 19, 78, (1985).
4. R. E. Treybal, Mass Transfer Operations, 2nd edition
(1968), McGraw-Hill, NY, p. 131-135, 142-144.

I letters

More on Tubular Flow Reactors
Dear Editor:
Professor Asfour's two improvements (CEE
XIX, 2, 84, 1985) to the original design of a tubu-
lar flow reactor using crystal violet dye and
sodium hydroxide reactants (Hudgins and Cayrol,
CEE XV, 1, 26, 1981) are timely ones. This ex-
periment, to judge from a recent survey (E. 0.
Eisen, "Teaching of Undergraduate Reactor De-
sign," AIChE Meeting, San Francisco, Nov.
1984), is now incorporated into several reaction
engineering laboratory courses in North America.
I welcome the occasion of the Asfour article
to suggest several additional improvements that
arise out of our experience since 1981.
First, I concur with the footnote in the Asfour
paper. Tygon tubing is an unhappy choice for
the tubular reactor. In our experience, clear Tygon
tubing darkens within a few hours' use to a per-
manent deep violet. This obscures the pleasing
axial color change that is one of the main at-
tractions of the experiment. Polyethylene tubing,
though translucent rather than transparent, re-
sists the crystal violet dye for a much longer
Calculating the reactor volume can be a prob-
lem. Certainly, the nominal value of the inside
diameter of the tubing is not sufficiently accurate.
Some students have improved on this value by
trying to fit the tubing using indexed drill bits.
Because of the flexibility of the tubing, however,
it is not certain that the cross-sectional area re-
mains undistorted when the tubing is wound on
the large spool. Weighing the spool with the re-
actor tubing empty and then filled with water ap-
pears to be the most rigorous way to obtain the
In both of the above CEE articles, the spool
is shown mounted on its side. This has proven to
be an unfortunate method of mounting since
bubbles often enter the reactor tubing (perhaps
from the mixer pump), become trapped in the
coils of the tubing, and grow. An effective remedy
is to remount the spool with axis perpendicular
to the lab bench and flow spiralling upward. Of
course, this does not eliminate bubbles but does
prevent their retention and growth sometimes to
several percent of the total reactor volume.
Continued on page 161.


SP laboratory


A Laboratory Experiment

Loughborough University of Technology
Loughborough, Leicestershire, England

SOME OF THE BASIC methods of chemical engi-
neering (heat and mass balances, for example)
have analogies (such as money) in everyday life,
and freshman students rarely have any con-
ceptual difficulty when such basic ideas are intro-
duced. However, when heat and mass balances
are combined with recycle, students often have
difficulty in analysing the process. They have diffi-
culty not so much with the heat and mass balances
themselves as with the whole concept of the re-
cycle process. This is mainly because there is no
immediate everyday counterpart, although an-

Tony Foord received his BSc and PhD degrees in chemical engi-
neering at the University of Birmingham (England) and was sub-
sequently employed in research and development by the U.K. Atomic
Anergy Authority and by the Distillers Company in London in process
development and project evaluation. In 1966 he joined the faculty at
the Loughborough University of Technology. His teaching interests
have been process economics and chemical engineering calculations,
and his principal responsibility has been the overall management
and development of the undergraduate courses. (L)
Geoff Mason graduated in chemistry at the University of Bristol
in 1962. He then worked for his PhD in the physics department at the
University of Bath before returning to Bristol as a research fellow. In
1970 he joined the faculty at Loughborough where, apart from a year
spent at the Petroleum Recovery Research Center (New Mexico), he has
been ever since. His research interests are mainly concerned with the
capillary properties of porous materials, particularly pore blocking
and network effects. (R)

In order to aid the
understanding of recycle we have
devised a simple apparatus in which water is
heated in a recycle loop

alogies can be attempted with taxis and people.
In order to aid the understanding of recycle
we have devised a simple apparatus in which
water is heated in a recycle loop. When operated
in the steady state, the apparatus permits both a
visual and an experimental appreciation of the
operation of a simple recycle loop. Moreover, in
the unsteady state the apparatus has a response
time of ten minutes or so, and thus, transient be-
haviour can be followed easily. The apparatus is
relatively simple, and since it is built from do-
mestic plumbing pipes and fittings it has a
familiar and easily grasped appearance. It is
mounted on a wallboard so that the flow path can
be seen at once. It uses only water and electricity
as consumables.

Fig. 1 is a schematic diagram of the appara-
tus. The recycle is driven by a domestic central
heating pump of the type used to circulate water
around radiators. Ours is an SMC Commodore
and it consumes about 150 watts. The heater is a
modified instantaneous shower heater, in essence
a copper can containing a 3kW heating element.
The shower heater originally had two in-built
safety devices, one a water pressure switch and
the other an anti-scald thermal cut-out. The heater
could only be activated when there was pressure
(and hence water) in the can and the tempera-
ture was below 500C. We modified our heater to
increase the cut-out temperature to 80C and re-
moved a flow constriction in the pressure-sensing
The pump drives the recycle at up to 8 litres/

Copyright ChE Division, ASEE, 1985



FIGURE 1. Schematic diagram of the apparatus. The inlet flow, Q
(maximum 3 litres/min), is ordinary mains water. A recycle loop,
flow q (maximum 8 litres/min) is driven by a pump through a do-
mestic shower heater (3kW). The temperature of the inlet water, the
outlet water and just after the heater in the recycle loop, are all

min, the highest reading of the recycle rotameter.
There is a rotameter (3 litres/min maximum) on
the inlet side measuring the inlet flow of tap
water and an identical one on the outlet side.
Mercury-in-glass thermometers (although digital
devices would be better) are used to measure the
water inlet temperature, the temperature after
the heater in the recycle loop and the outlet
temperature. The water flow rate of the feed
and also of the recycle loop may be adjusted and
set by means of valves. The complete rig is il-
lustrated in Fig. 2.
The tube sizes, although apparently arbitrary,
make a difference to the performance of the ap-
paratus. Air comes out of solution in the heater
and tends to accumulate in the pump which is
working here at less than its design flow. By using
28 mm tubing at a slightly rising angle for the
top tube of the recycle loop and 22 mm tube for
the descending tube to the pump, the air tends to
enter the outlet pipe rather than be carried down-
wards. In the 15 mm sections air bubbles are
easily carried along, either upwards or down-

Mass balances: The first experiment is trivial
but is a graphic illustration of the mass balance
principle: at various valve settings it is easy to
show that whatever the recycle rate the inlet flow
rate always equals the outlet flow rate.
Heat balances: a) With the heater switched

T, = To + (H/QC)

where H is the combined heat input of the pump
and heater and C is the specific heat capacity of
Similarly one obtains

T. = To + (H/QC) + (H/qC)

from a heat balance across the shower heater,
after eliminating T1 by means of Eq. (1).
So, by measuring the outlet water tempera-
ture, T,, as a function of the through flow rate,
Q, it is possible to determine the combined heat
input of the heater and pump by the use of Eq.
(1). The experiment takes some time to perform
because it takes about fifteen minutes for the
steady-state to be reached after a change in flow
rate. By plotting (Ti To) against 1/Q, the gra-
dient (H/C) gives the power input (H) as shown
on Fig. 3. Alternatively, Eq. (2) can be used. In

FIGURE 2. A photograph of the apparatus. It is mounted on a wall
board so that the flow directions are obvious. The top pipe is slightly
angled to assist in purging the air which comes out of solution as
the water is heated.


on and at a fixed input water flow rate, the ap-
paratus shows that the outlet water temperature
is independent of the recycle rate. Students often
find this observation disconcerting. They observe
a change in the temperature of the recycle water
when its flow rate is altered, but find that the out-
let temperature of the loop remains the same.
Only when they consider the overall heat balance
do they find it obvious that the outlet temperature
is unaffected.
b) Using the variables marked on Fig. 1 for
flows and temperatures for the steady-state, a
heat balance over the whole system shows that



r 30-


- 10-


Gradient = 45.9 degree.litres/min

Heater power = x 4.2
= 3,21 kW *

./ *


0 0.2 0.4 0.6
I/Q min/I

1.0 1.1

FIGURE 3. Results from the steady-state operation of the apparatus.
The temperature rise of the through stream is plotted against the
reciprocal of the through flow rate. The graph is a straight line through
the origin with a gradient determined by the combined energy input
of the heater and circulating pump.

this case T2 is plotted against 1/q, where q is the
recycle rate, and H is obtained from the same
gradient. This latter method has the advantage
of actually making use of the recycle flow.


In unsteady-state experiments both the inlet
flow and recycle flow are fixed, the system is al-
lowed to approach, but not necessarily reach, equi-
librium, and the heater is switched either on or
off as appropriate. The apparatus takes several
minutes to respond and the dynamic changes can
be monitored by hand. Typical examples of
temperature-time graphs are shown in Fig. 4 for
both rising and falling temperature. The recycle
rate was 5 litres/min and the inlet flow rates 1.0,
1.5, 2.0, 2.5, and 3.0 litres/min.
A heat balance on the system for a small time
interval, dt, in which the outlet temperature, T,
changes by dT gives

QCTo + H = QCT + VC (dT/dt) (3)

where V is the volume of the recycle circuit which,
as an approximation, is assumed to be perfectly
mixed. Using Eq (1) to eliminate H, and then
integrating from To at time 0, gives

In [(T1 T) / (T To)] = -Qt/V (4)
T thus rises exponentially to the steady-state
temperature T, when the heater is switched on

time sees

Heater switched off ot time = 0

3 I/min -2.51 /min

200 300
time, t scs

400 500 600

Figure 4. Results from the unsteady-state operation of the apparatus.
The recycle rate was fixed at 5 litres/min and the response is only
slightly dependent upon it. Fig. 4(a) shows the effect of switching the
heater on at different through flow rates. Fig. 4(b) shows the effect
of switching the heater off at different flow rates. The temperature
rises in Fig. 4(a) and falls in Fig. 4(b) exponentially to the limiting
temperature. The different limiting temperatures in Fig. 4(b) are
caused by the heat input from the recirculating pump and also by
small changes in the feed water temperature. Note that the re-
sponse time is a function of the inlet flow rate.

and falls exponentially to the temperature To
when the heater is switched off. The time constant
is independent of the heater power and also of
the recycle rate but depends on Q, the inlet flow
rate, and the volume of the system. By plotting
the log arithmetic term of Eq. (4) against time,
the gradient (-Q/V) can be determined. If this
is repeated for several flows then a graph of these
gradients against Q gives a straight line of slope
1/V through the origin.
The volume of the recycle circuit so deter-
mined is only an effective volume rather than a


FIGURE 5. Logarithmic plots of the results of Fig. 4(a).

f T,-


0, litres/min
I 2 3

Heating *

Gradient= I/V = 0240

V = 4.17 litres equivalent

FIGURE 6. The effective volume of the recycle system determined
from the gradients of the lines in Fig. 5 by plotting the gradient
against the through flow rate. Values from the curves of Fig. 4(b) are
also shown although the straight line logarithmic plots have not been

true internal volume because the metalwork of
the system behaves as a heat sink. Its effect is
quite large because the pump weighs several
pounds but conduction is fast enough for the
metal and fluid in the recycle loop to have the
same temperature. The temperature profiles of
Fig. 4 demonstrate that, as predicted by Eq. (4),
the system reaches equilibrium faster for higher
inlet flow rates than it does for lower inlet flow
Figure 5 shows the straight lines given by Eq.
(4) for rising temperature using the typical data
given in Fig. 4. Note that there is a delay of be-
tween 10 and twenty seconds before the ther-
mometer responds to the heater being switched
on, due to the transit time of the water in the
pipes. Fig. 6 shows the gradients of the lines of
Fig. 5 plotted against Q, the inlet flow rate, and
it is from the gradient of Fig. 6 that the effective
volume, V, of the recycle loop can be determined.




Gradient = 3.00 degree-litres/min
Heat input 3 x 4.2 0.21 kW

0/ ._0

I I/Q min/litre

FIGURE 7. The temperature rise of water passing through the system
obtained from the limiting temperatures of the cooling curves. (Fig.
4(b)) and the feed temperature plotted against the reciprocal of the
through flow rate. This graph is equivalent to the steady state results
of Fig. 3 but with the only heat input coming from the energy of
the pump. The slight offset of the line from the origin is most likely
caused by a systematic error between the two separate thermometers
which were used to measure the temperature rise.


The analysis of the behaviour of this appara-
tus is straightforward. The accurate interpreta-
tion of actual experimental results is not so simple
because of drift in the temperature of the water
feed and other small effects. Rough and ready
results and analysis may be adequate for routine
teaching, but to get the best from the apparatus
a more refined approach is necessary. For example
it is better to extrapolate the dynamic experi-
mental data to obtain the steady-state tempera-
tures. This gives students useful practice in analys-
ing an exponential rise to a limit as well as giving
the steady-state temperatures more accurately.
The falling temperature curves give limiting
temperatures which, because of the heat input
from the recycle pump, are not equal to the inlet
water temperature To. Indeed the temperature
rise between the inlet water temperature and the
extrapolated outlet water temperature with the
heater switched off can be used in a heat balance
to determine the energy input by the pump. Fig.
7 shows AT, the temperature rise of water through
Continued on page 143.


class and home problems

The object of this column is to enhance our readers' collection of interesting and novel problems in
Chemical Engineering. Problems of the type that can be used to motivate the student by presenting a
particular principle in class or in a new light or that can be assigned as a novel home problem are re-
quested as well as those that are more traditional in nature that elucidate difficult concepts. Please sub-
mit them to Professor H. Scott Fogler, ChE Department, University of Michigan, Ann Arbor, MI 48109.


An Exercise in Modelling

Indian Institute of Technology
Kanpur-208016, India

IN APPLIED MATHEMATICS courses the emphasis
is usually on solving equations. There is very
limited discussion about problem-definition and
expressing it in terms of mathematically under-
stood phenomena. A mathematically understood
phenomenon is one which, at least in its simplest
form, can be expressed mathematically [1]. Once
the problem is interpreted, it requires only the
substitution of symbols for words before a rele-
vant equation is obtained. Teaching this missing
part of the story is difficult because it is a crea-
tive process. There are no set procedures avail-
able for such an exercise. The students can, at

V. Ravichandran is an assistant professor at the Indian Institute
of Technology, Kanpur, India. Prior to coming to Kanpur he was a
visiting assistant professor at the University of Notre Dame where
he obtained his PhD (1981). He received his BTech in ChE from the
University of Madras (1977) and MS from Oklahoma State University
(1978). His research interests include a variety of topics including
chemistry of catalysis, biochemical engineering, mathematical
modelling, and application of microprocessor to chemical engineering.

best, be helped to learn by themselves. With this
in view, in a course entitled "Applied Mathematics
in Chemical Engineering," the students are
given a 'one month problem.' The problem is a
real life situation which has to be defined in such
a way that it can be expressed and analyzed
The students are encouraged not to get into
complicated mathematical formulations. This
strategy helps the students to concentrate and to
appreciate the subtle nuances involved in prob-
lem definition and modelling strategies. Thus the
scope of the 'one month problem' is limited and
should not be confused with the regular modelling
exercises. Wherever possible, the simple model
obtained is evaluated against the existing data.
Near the end of the semester the problems are
assigned to the students (one each) as a project,
to solve as regular modelling problems. One such
problem is discussed below.

You are going to spend the winter in the
middle of nowhere, say in the Himalayas or in
Alaska, where the temperature gets very cold.
You are going to stay in a cabin where there is
no heating. How will you decide whether the
sleeping bag you have will keep you warm enough
or comfortable?

The best way to find out is to ask somebody
who has experienced the same climate. In the ab-
sence of an experienced person, however, we have
Copyright ChE Division, ASEE, 1985


to resort to mathematical modelling to determine
how much insulation is necessary to keep the
body warm and comfortable. Before we proceed
with the solution, the term "comfort" has to be
defined in the context of the problem.
"Comfort" depends largely on the skin
temperature. When the skin temperature is high,
sweating begins and the latent heat of evaporation
cools the body down. It is very uncomfortable
when one starts sweating inside the sleeping bag.
Hence the temperature at which sweating begins
marks the upper limit of the "comfortable" skin
temperature, which is 34.5C [2].
The skin temperature begins to fall when the
skin is exposed to cold temperature. The self-de-
fense mechanisms of the human body try to main-
tain the skin temperature; however the com-
pensatory measures fail below 32 C, which is
known as the shivering temperature [2].
As long as the skin temperature is between
the sweating temperature and the shivering
temperature the person feels comfortable, i.e.,

Tw > Ts > Tsh

where T,, = the sweating temperature
T. = the skin temperature
Tsh = the shivering temperature.

From the above discussion the problem can
be redefined as follows: At a given outside
temperature, calculate the insulation necessary to
maintain the body temperature between shivering
and sweating temperatures.
The following assumptions are necessary to
make the problem mathematically tractable

The heat production rate is at q kcal/ and the
skin temperature is uniform throughout.
The loss of heat by convection, radiation, and
evaporation is negligible, and the heat is lost only
by conduction.
The air pocket between the sleeping bag and the
body is neglected.

Let us assume the body is rectangular in cross




section, and a sleeping bag of thickness t is cover-
ing it uniformly as shown in Fig. 1 (a). Since the
skin temperature is uniform throughout, a simple
one-dimensional model is sufficient to describe the
system, as shown in Fig. l(b). Under steady
state conditions the rate at which heat is pro-



0 2

-30 -20 -10 0 10 20
Surrounding temperature To, C

duced should equal the rate of
through the sleeping bag. Thus

heat conducted

q = KA dx

and the integrated form is

t Kp(T,-T) K Ta + (KT) (1)
q q q

where A

= 1
= surrounding temperature
= thickness of the sleeping bag
= thermal conductivity of the
packing material

For a given outside temperature and the
thermal conductivity of the insulator, the re-
quired thickness of the sleeping bag can be com-
puted using Eq. (1).
Fig. 2 shows the relationship between the sur-
rounding temperature and the bag thickness for
a man whose average basal metabolic rate is 40
kcal/m2 hr [2]. In the absence of any other in-
formation, the thermal conductivity of the bag
is assumed to be the same as that of animal wool,
i.e. 0.0315 kcal/m-hr-C [3]. It is very obvious
that this model fails closer to the ambient tempera-


Average basal metabolic rate for males and females
of various ages [2]




ture because of 'no air pocket' assumption.
It can be easily shown that the required thick-
ness does not change with various age groups as
the heat production rate is not significantly differ-
ent (Table 1). In cases where the ground tempera-
ture is cooler than the atmospheric temperature,
we can make a conservative estimate of the bag
thickness by taking both the ground temperature
itself as the surrounding temperature and the
thermal conductivity of the compressed packing
It was found that the assumption of cylindri-
cal shape for the body does not alter the result
significantly. O

Contributions of Umesh K. Jayaswal, Atul
Bansal, and V. L. N. Murthy are gratefully

1. Ravichandran, V., "Chemically Processed Mathe-
matics," to be published.
2. Bell, George H., J. N. Davidson and D. E. Smith,
Textbook of Physiology and Biochemistry, 8th Ed.,
3. Foust, A., L. A. Wenzel, C. W. Clump, L. Maus, and
L. B. Anderson, Principles of Unit Operations, 2nd
Ed., 1980.

Continued from page 131.
and Documentation in existence for a number of
years, with the objective of assisting the intro-
duction of new methods into the chemical engi-
neering profession. As part of this work they have
developed a suggested curriculum for a course in
information and documentation for chemical
engineers. This is given as Table 1. This table
could be taken as the basis for any new course de-
veloped for chemical engineers.
The aim of this paper has not been to give a

quick course on information and documentation,
but simply to mention the trends in this quickly
moving area and to indicate that there is sufficient
material relevant to a chemical engineer to form
a short course on the subject. If the reader is left
confused, but impressed, then we have achieved
our aim and suggest he get together with his own
information scientist (librarian) to develop a
course for his undergraduates.
We believe a course of about nine to twelve
hours would be ideal. This would enable about
three hours of exercises in the library to be made
and a computer retrieval demonstration to be at-
tended. If this amount of time is not available,
then two hours of lectures could survey the
material and practical experience could be gained

Proposed Curriculum for Basic Information
Science Training
a) Primary Sources: Journals and reports, con-
ference reprints, patents, dissertations.
b) Secondary Sources: Chemical, Chemical Engi-
neering and Engineering Abstracts; SCI.
c) Tertiary Sources: Handbooks, encyclopedia,
books. Advances in List important
Computer Data Bases
a) Bibliographic data bases.
b) Numerical data banks.
a) Manual: Indexing, Search Techniques; Biblio-
graphic, Data.
b) Computer Searching:
Bibliographic: files, networks, host computer; data
base selection; searching techniques; costs
Numeric Data Banks: available banks; procedure,
c) The role of libraries and information scientists

in association with laboratory work and project
work. At least, practical experience should be
planned and guided-not simply left as a random
search for the student to undertake when all else
has failed. O

The authors wish to express their thanks to
those members of the E.F.C.E. Working Party
on Information and Documentation who comment-
ed on the draft outlines of this paper. Their com-
ments were gratefully received and incorporated


into the final text.

Baltatu, M. E., "On-Line Information," Chem. Eng. (NY),
p. 69 (1984).
Fidel, R., D. SSrgel, "Factors Affecting On-Line Biblio-
graphic Retrieval: A Conceptual Framework for Re-
search," J. Am. Soc. Inform. Sci. 34 (3), pp. 163-180
Fries, J. R., "Data Base Searching in Chemical Engi-
neering," Chem. Eng. (NY) 88 (26) p. 71 (1981).
Graham, M. H., A. B. Lamy, B. Lawrence, and L. Y.
Stroumtsos, "Information Retrieval," in Kirk-Othmer,
3rd. ed., 13, pp. 278-336, (1981).
Hall, J. L., M. J. Brown, "On-Line Bibliographic Data
Bases." An International Directory, 2nd. ed., Aslib,
London (1981).
Henry, W. M., J. A. Leigh, L. A. Tedd, and P. W. Williams,
On-Line Searching: An Introduction, Butterworths,
London (1980).
Kaback, S. M., "On-Line Patent Searching: The Realities,"
Online 7 (4), pp. 22-31 (1983).
Rasmussen, P., "Data Banks for Chemical Engineers,"
Danmarks Tekniske Hojskole, Lyngby, Denmark
Rose, L. M., "Uebersicht iiber die gegenwiirtig ver-
fiigbaren Datenbanken fir physikalische Eigen-
schaften," CHIMIA 33, p. 256 (1979).
Stanley, W. G., "Unique Information Resources for the
Chemical Engineer," Chem. Eng. Prog. 77 (6), pp. 80-
82 (1981).

Continued from page 139.

the apparatus, plotted against 1/Q. The energy in-
put of the pump is found from the gradient to be
about 210 watts. The intercept (about 0.3C)
probably represents the scale reading difference
between the two thermometers.
A further refinement that is possible with the
apparatus is to run the dynamic experiment in the
limiting case of recycle with no through-flow.
With no through-flow the apparatus is analogous
to a well-mixed batch reactor, whereas it is an-
alogous to a CSTR when through-flow is present.
Fig. 8 shows results for this case for three differ-
ent recycle rates. The three lines do not coincide
because different starting temperatures were used.
The results show that after 30 seconds or so
there is, as expected, a linear temperature rise
with time. The temperature rises with no limit
at least until the safety cut-out of the shower
heater operates. The gradients of the lines on Fig.
8 are all the same and by using the combined
heater and pump energy input of 3.21 kW it is
possible to estimate the effective recycle volume.

This is 3.95 litres for the results shown, about 5%
less than the value obtained using the through-
flow method. The most likely cause is the time
taken to heat up parts of the metalwork of the
pump; this experiment lasts only four minutes,
compared to ten for the through-flow method.
Students always say that the apparatus could
be improved by lagging the pipework to reduce
heat losses, but simple measurements on a cool-
ing curve indicate that the heat losses are very
small. Also, for some of the temperature response




1 20-


Recycle Rate
* 3 litres/min
* 5 litres/min
S7 litres/min

Gradients = 0.193 "C/sec

If energy input is 3.21 kW then
the effective volume is 3.21
4.2 x 0.193

= 3.95 litres

0 100 200 300
Time sees

FIGURE 8. With no through flow the recycle loop temperature rises
without limit as can be seen above. Using the combined energy input
of the heater and pump (determined on Fig. 3) the effective volume of
the recycle loop can be determined using the gradient of the lines.
This volume can be compared with the value determined on Fig. 6
(4.17 litres equivalent). The lines are for different recycle rates which,
as expected, have no effect. Different initial temperatures were used.
Up to the first minute it can be seen that the system is not well.mixed.

curves the water temperature is below the am-
bient air temperature and so the system is gain-
ing heat rather than losing it.


Our apparatus has been in service for several
years without giving trouble, perhaps a conse-
quence of using well proven domestic components.
The recycle experiments performed with it can
range from simple mass and heat balances right
through to the dynamics. Its main purpose, how-
ever, is to provide a vivid demonstration of basic
mass and heat balances in a system with re-
cycle. E





Teesside Polytechnic
Middlesbrough, United Kingdom

IN AUGUST 1982 THE Department of Chemical
Engineering, Teesside Polytechnic, UK, took
delivery of a Ferranti Argus 700GL process
control computer system. The system was supplied
in accordance with a detailed enquiry specification
which defined precisely the objectives and scope
of the system (Table 1). The objectives of the
system are
To assist departmental research into varied chemi-
cal engineering topics by providing a compre-
hensive and flexible data logging and plant control
To provide a teaching facility for the department

The availability of packaged software
transforms this situation, enabling the engineer
(student or practitioner) to produce useful
process control software in a matter
of days rather than months.

by live demonstrations of plant monitoring and
control applications, simulation, and implementation
by students of control strategies.

It is now timely to report on the extent to
which these objectives have been realized. At the
time this paper is being written, the system is
capable of controlling two pilot plants and has
also been substantially integrated into our teach-
ing programmes. Computer control is now taught

Enquiry Specification

1. Objectives and scope of the system
2. Extent of supply
3. Exclusions from supply
4. Functional specification
Data acquisition
Data logging
Pilot plant control
Operator interface
Data links
Development facilities
Teaching facilities
5. System hardware configuration
Equipment specification
Control system description
Maintenance facilities
6. Supply of software
Standard systems software
Standard packaged application software
Special to project software for a) plant control
b) data links
High level language
Operator facilities

Management/engineer facilities
Expansion capability
7. General electrical & electronic design requirements
Equipment housing
Power supplies
Cable schedules
Environmental requirements
Safety requirements
Expansion capability
8. Acceptance tests
System hardware/software
Packaged software
Application software
System robustness
System loading
9. Installation and commissioning requirements
10. Documentation
11. Project time schedule
12. Maintenance and training requirements
13. Project management
Project organisation
Project communications and control
14. Commercial requirements

Copyright ChE Division, ASEE, 1985


X C_7
,,., MU.I
ii raRE Lourro arxr
irsrr~ COI~OLE
m rlror PWKISI


\ ?

Brian Buxton is a senior lecturer in the Department of Chemical
Engineering, Teesside Polytechnic, UK. He studied at the University
of Aston in Birmingham, receiving his BSc degree in 1967 and
his PhD in 1971. He spent 10 years in industry with both ICI and
the British Steel Corporation. During this period, he was responsible
for the specification, installation and commissioning of several com-
puter control systems. He joined Teesside Polytechnic in 1981 and
was responsible for the specification and procurement of the Ferranti
Argus computer control system featured in this article. His research
interests include the implementation of adaptive control techniques
on chemical processes.

in all the higher education courses offered by the
Higher Diploma
BEng Honours Degree Courses
Post Graduate Degree Courses (MSc and PhD)

as well as providing a key facility for our post-
graduate research teams.
It is emphasized that all the teaching pro-
grammes involve a substantial proportion of
practical experience on the computer system
coupled with live demonstrations of on-line com-
puter control. It has been found that this new
approach to teaching process control stimulates
considerable interest from the students who are
readily able to relate to these practical situations.
Furthermore, the experience gained on such

FIGURE 1. Computer System Configuration.

systems is much more directly applicable to the
industrial environment than the classical control
theory or the modern control theory commonly
taught in higher education courses.
The configuration of the computer system is
illustrated in Fig. 1 and defined in Table 2.
Sufficient industrial interface equipment has been
purchased to enable the system to control several
pilot plants simultaneously. It also provides con-
nection to simulation equipment.
The simulation equipment facilitates both teach-
ing and testing of research software. The mono-
chrome VDU's may be sited alongside pilot plants
to provide local operator display and control facili-
ties. Software development may also take place
at these locations if required. Further colour
graphics terminals will be added to the configura-
tion in the future.
The pilot plants are accommodated in three
module rooms. These rooms extend from the
ground to the top floor of the building and can ac-

Computer System Configuration


Argus 700 GL processor
Semiconductor stores (256 Kb)
Monitor and control console


Monochrome VDU's (15 inch display
heads and keyboards)
20 inch colour monitor and functional
Matrix printers (180 cps)
Keyboard for printer
Plus drive cards for all peripheral de-
vices and serial input/output cards

for data links
Storage Media
Twin cartridge disc storage system
(10 Mb) (one exchangeable, one fixed)
Twin floppy disc storage system
(1.0 Mb)
Industrial Interface Equipment
Analogue inputs
Analogue outputs
Digital inputs
Digital outputs
Pulsed digital outputs
Plus usual power supplies, fans, pack-
aging, etc.




- --TXoN ..NE


commodate large column type processes. A pair
of reactor bays is also provided on each floor of
the building. Multicore cables have been laid to
link the computer to pilot plants in all of the above

The standard system software P.M.S. (Pro-
cess Management System) encompasses all the
facilities required to implement, operate, and
manage a computer controlled process. Software
packages have been provided by the computer
manufacturer which greatly assist the engineer
in building the application software required to
operate his particular plant. It is this facility
which enables the teaching of the subject within
the time scale and context of a higher education
Prior to the availability of control packages,
the general approach of computer system suppli-
ers was to provide "tailor made" software for a
specific application in the form of a so-called
"turn key" contract. The software was written in

Ferranti computer control system.

a real-time high level language such as CORAL.
This meant that engineers were either required to
learn in depth a high level language and the as-
sociated operating system of the host computer
system, or to define their system requirements to
a programmer, who in turn implemented the re-
quired functions in software. Either of these op-
tions was time consuming, costly, and therefore
inefficient. The time scale required to learn such
programming skills can be measured in months,
rather than weeks, of dedicated work, which makes
it impossible for it to be incorporated as part of a
higher education course.

The task of the engineer is then
to select which operations are needed for
a specific case and to link them
together accordingly.

The availability of packaged software trans-
forms this situation, enabling the engineer
(student or practitioner) to produce useful pro-
cess control software in a matter of days rather
than months.
Specifically, the packages assist the engineer
in implementing the following functions in soft-
Interfacing of plant signals to and from the com-
Continuous control
Sequence control
Operator interface: a means of display and modi-
fication of process and control information.

All are clearly essential for the commission-
ing of any computer control system. The packages
are based on the principle that certain operations
are common to all process control applications,
while the order in which they are applied is spe-
cific to the particular application in question.
The task of the engineer is then to select
which operations are needed for a specific case
and to link them together accordingly. The pack-
age provides considerable assistance with this
linking "construction" by providing a conversa-
tional facility for the engineer in the form of
displayed messages (prompts). The task is then
reduced from one of detailed programming to
one of deciding on a control strategy and then de-
fining a series of operations and associated
parameters to implement the strategy. Thus, vir-
tually no programming skills are required and the
problem of programming errors which normally
arise in the programming of complex software is
largely avoided.

In the context of control packages, the teach-
ing of control system design, from initial strategy
to implementation and testing of software using
hardware and software simulators, is entirely
Every opportunity has been taken to incorpor-
ate our computer control facilities in our teaching
programmes. These include
Laboratory Practicals for the Higher Diploma


students: e.g., interfacing of plant measurements.
This requires that the student generate the software
to condition and convert electrical signals into
engineering units. The operation of the software is
then tested by means of simulation panels.
*Short Course (10h) for the final year of the BEng
course. The course includes several practical sessions
on building software to interface signals, continu-
ous control loops, and operator displays. The pro-
ject used to assess the students in the current
academic year requires that the students work as
a project team to generate the entire software to
monitor, data log, and control a fermenter. The
facilities will include sequence control of the plant
and a colour graphic display of the process pro-
viding a live mimic of the plant operation. This is
no artificial project since the software produced by
the undergraduates will ultimately be used by the
department's biotechnology research team to imple-
ment computer control on a newly acquired fer-
Mention should also be made of the allocation
of a limited number of research projects to second-
year degree students which involve the computer
control of laboratory scale apparatus. Current
projects involve the control of pH and level.
Chemical engineering also offers service teach-
ing to other Polytechnic departments. The op-
portunity has, therefore, been taken to offer com-
puter control of a pilot plant as a case study.
This academic year, students from both the Com-
puter Science Department (Information Tech-
nology MSc Course) and the Department of
Electrical, Instrumentation and Control (BSc2),
have received a concentrated study on computer
control of a specific pilot plant. Like the other
courses offered, the courses include a substantial
proportion of practical experience on the com-
puter system and live computer control demon-

With regard to research, the main thrust has
been directed toward the commissioning of direct
digital control of a gas absorption column. This
work involved the use of adaptive control (the
self tuning regulator) which has been used to
optimise the operation of a cascade loop on the
column. This research is reported in a separate
paper [1] and will not be considered further here.
However, it is worth noting that the speed with
which this research was implemented owes a great
deal to the availability of packaged software on
the system. While the self tuning regulators were
in fact programmed in a high level language, the
interfacing of this software with the control

packages (which are responsible for all other
control facilities) was straightforward and
rapidly achieved. It should be noted that apart
from this one specialized application, all our soft-
ware requirements to date have been easily imple-
mented by the control packages.
Future research effort will be directed to the

Graphics display of gas absorption column pilot plant.

implementation of computer control on a novel
catalytic reactor which has been developed within
the department over a number of years [2]. The
control system will facilitate prolonged operation-
al runs and assist in further research into com-
mercial application and scale up of this unique
reactor. The plan is to apply the adaptive control
techniques (recently proven on the gas absorption
column) to this reactor. This process lends itself
particularly well to these techniques in view of
its time varying nature due to the decaying
catalyst. This is the main target for the research
In conclusion, it is clearly important to recog-
nise the potential of packaged software in the
teaching and research environment. (There are
also considerable implications for the industrial
applications, but that is beyond the scope of this
paper.) Packages are rapidly gaining recognition
as vital tools for the modern chemical engineer.
In an environment of continuously falling com-
puter hardware costs, coupled with the ever-rising
costs of producing "tailor made" software, it is
essential that the engineer makes full use of com-
mercially available packages. The cost of plant de-
sign, implementation and operation of chemical
processes and their associated automation systems
can be considerably reduced by judicious use of
Continued on page 161.


S classroom


Ben-Gurion University of the Negev
Beer-Sheva, Israel

N UMERICAL VALUES OF physical, thermodynamic,
and transport properties of pure compounds
and mixtures are necessary for the development
of chemical processes and the design of chemical
plants. Experimental data available in the litera-
ture are limited but the need for the estimation of
such properties is crucial in calculations carried
out by chemical engineers. The study of correla-
tions for estimating various properties is an inte-
gral part of courses in transport phenomena and
Considering the importance of the subject, a
course designed to cover the theoretical and practi-
cal aspects of properties estimation was intro-
duced into the curriculum. The course is given to
junior and senior students who have a strong back-
ground in thermodynamics and transport phe-
Throughout the course, two fundamental
methods for estimating properties are emphasized
Corresponding states principle (CSP)
Equations of state (EOS)
Another method is the group contribution
method. This approach is used for estimating
thermodynamic properties of ideal gases (no
intermolecular forces) and also for estimating
critical points of pure compounds [1] and activity
coefficients in the liquid phase [7].
The outline of the course is listed in Table 1.
Since this field is very dynamic, the outline is up-
dated every year according to new developments.
All correlations and samples of calculation are
organized in a manual distributed to the students.
During the lectures the theoretical basis of the
correlations is discussed and the advantages and
disadvantages of various correlations are pointed
In the first lecture the students receive a list
of primary, secondary, and tertiary literature
sources which are useful during the course. The

M. Herskowitz completed his PhD in chemical engineering at the
University of California, Davis, in 1978, and since 1979 has been a
faculty member at the Ben-Gurion University of the Negev, Beer-
Sheva, Israel. His principal interests are multiphase reactor design,
synthetic fuels, and estimation of thermodynamic properties. In
1984-85 he is spending a sabbatical with Exxon Research and Engi-
neering Co. and at the University of Delaware as a visiting professor.

book of Reid et al [1] is recommended as an excel-
lent reference to correlations published until 1976.
Other books [2, 3, 4] are used as references to the
theoretical basis in properties estimation. The
proceedings of the International Conference on
Phase Equilibria and Fluid Properties [5, 6] are
also valuable references. The students are en-
couraged to read original papers in order to gain
some insight into the limitations of the various
The material studied during the course is
practiced in homework problems which include ap-
plications of the correlations. For this purpose
computer programs are available in topics such as
Phase equilibria calculations by the UNIFAC
Phase equilibria calculations by EOS
Calculation of critical points of mixtures
Some of the programs were provided by Ras-
mussen [8].
The students are also required to work on a
project. Each student selects a certain property
and prepares a report which includes
A literature search that covers a period of the last
three years, based mainly on Chemical Abstracts


Copyright ChE Division, ASEE, 1985

but also on current journals.
Selection of two papers dealing with general cor-
relations, a summary of the basic approach, and the
Selection of a limited database from the literature
for testing the correlations. Only primary sources
are used with proper estimation of the experimental
accuracy of the data.
A comparison of the correlations and practical con-

Working on this project, the students gain ex-
perience in the literature search, the understand-
ing of correlations, and their proper applications.

Course Outline*

INTRODUCTION: 5 Lectures**
a. Corresponding states principle (CSP): theoretical
background [2, 9]
b. Classification of fluids: simple, normal, polar and
quantum [9]
c. Critical points of pure compounds: Lydersen [1],
Ambrose [10]
d. Equations of state (EOS) [11]: cubic EOS, the
virial EOS, mixing rules
e. Critical and pseudocritical properties of mixtures,
mixing rules

18 Lectures
a. Molar volume of gases and liquids
1) CSP: Lee-Kesler [12], Teja et al [13]; COS-
TALD [14], Gunn-Yamada [1] for liquids
2) EOS: Redlich-Kwong [1], Soave-Redlich-Kwong
[1], Peng-Robinson [15]
3) Virial EOS: Tsonopoulus [1], Hayden-O'Connell
[16], Orbey-Vera [19]
b. Enthalpy, entropy, fugacity, and heat capacity
1) CSP: Lee-Kesler [12], Tyagi [20]
2) EOS: RK [1], SRK [1], PR [15]
3) Construction of diagrams such as the Mollier
c. Vapor pressure and heat of vaporization: Lee-Kesler
[12], Riedel [1], Vetere [17]
d. Thermodynamic properties of ideal gases: Thinh-
Trong [18] for hydrocarbon, Benson [1]
SOLUBILITY: 9 Lectures
a. Theoretical background [2, 3]
b. EOS [3]: SRK [1], PR [15]
c. Group Contribution Methods: UNIFAC method [7]
a. Theoretical background [4]
b. Viscosity: Reichenberg [1], Ely-Hanley [21]
c. Thermal conductivity: Ely-Hanley [22], Euken [1],
Roy-Thodos [1], Robbins-Kingrea [1]
d. Diffusion coefficients: Wilke-Chang [1], Scheibel [1]

*Only part of the references are listed.
**Each lecture lasts 50 minutes.

This is also an opportunity to test the reliability
of experimental data. Some projects have yielded
interesting results which stimulated further re-
The course is a good opportunity to review and
emphasize the practical aspects of fundamental
principles in thermodynamics and transport phe-
nomena. Five classes of students have already com-
pleted this course. They found it useful in practical
courses such as plants design, unit operations lab,
and the senior project. Furthermore, it provides
some of the tools a practicing chemical engineer
needs. O

1. Reid, R. C., J. M. Prausnitz and T. K. Sherwood, The
Properties of Gases and Liquids, McGraw Hill, 3rd
Ed., N.Y. (1977).
2. Prausnitz, J. M., Molecular Thermodynamics of Fluid-
Phase Equilibria, Prentice-Hall, Englewood Cliffs,
N.J. (1969)
3. Van Ness, H. C. and M. M. Abbot, Classical Thermody-
namics of Nonelectrolyte Solutions, McGraw-Hill,
N.Y. (1982).
4. Hirschfelder, J. 0., C. F. Curtiss and R. B. Bird,
Molecular Theory of Gases and Liquids, J. Wiley, N.Y.
5. Sandler, S. I. and T. S. Storvick, eds., "Phase Equilib-
ria and Fluid Properties in the Chemical Industry,"
ACS Symp. Ser. 60, Washington (1977).
6. Renon, H., ed., "Fluid Properties and Phase Equi-
libria for Chemical Process Design", Fluid Phase
Equilibria, 13, 14 (Special ed.) (1983).
7. Fredenslund, A., J. Gmehling and P. Rasmussen,
Vapor-Liquid Equilibria Using UNIFAC, Elsevier,
Amsterdam (1977).
8. Rasmussen, P., Private communication (June 1983).
9. Leland, T. W. and P. S. Chappelear, Ind. Eng. Chem.,
60 (7), 15 (1968).
10. Ambrose, D., NPL Reports 92 and 98, NPL, Tedding-
ton (1979).
11. Abbott, M. M., Adv. Chem. Ser. 182, 47 (1979).
12. Lee, B. I. and M. G. Kessler, AIChE J., 21, 510 (1975).
13. Teja, A. S., S. I. Sandler and N. C. Patel, Chem. Eng.
J. 21, 21 (1981).
14. Hankinson, R. W. and G. H. Thomson, AIChE J., 25,
653 (1979).
15. Peng, D. Y. and D. B. Robinson, Ind. Eng. Chem.
Fund., 15, 59 (1976).
16. Hayden, J. G. and J. P. O'Connell, Ind. Eng. Chem.
Proc. Des. Dev., 14, 209 (1975).
17. Vetere, A., Chem. Eng. J., 17, 157 (1979).
18. Thinh, T. P. and T. K. Trong, Can. J. Chem. Eng.,
54, 344 (1976).
19. Orbey, H. and J. H. Vera, AIChE J., 29, 107 (1983).
20. Tyagi, K. P., Ind. Eng. Chem. Proc. Des. Dev., 14,
484 (1975).
21. Ely, J. F. and H. J. M. Hanley, Ind. Eng. Chem. Fund.,
20, 323 (1981).
22. Ely, J. F. and H. J. M. Hanley, Ind. Eng. Chem.
Fund., 22, 90 (1983).


S laboratory


University of California, San Diego
La Jolla, CA 92093

cently been introduced into the Department of
Applied Mechanics and Engineering Sciences
(AMES) at the University of California, San
Diego (UCSD). The first courses in chemical engi-
neering were offered in the fall of 1979. The
strategy was to integrate the new discipline into
the previously existing engineering curriculum
(fluid mechanics, thermodynamics, engineering
mathematics, etc.) while gradually introducing
traditional chemical engineering courses. A
genuine chemical engineering program was
achieved in the fall of 1982.
Initially targeted as one of the major priori-
ties was the establishment of a chemical engineer-
ing undergraduate unit operations laboratory to
be given at the senior level. We also determined
at an early stage that we should develop the in-
novative skills of the students and not follow the

typical cookbook recipe formats so prevalent in
many chemical engineering departments. During
the past four years, the laboratory has evolved as
a setting in which our seniors refine the classroom
skills they have acquired and attack problems
under circumstances similar to industrial ex-
perience. Under space, faculty, and financial re-
straints typical of many academic programs, we
have developed what we feel is a unique approach.
The Chemical Engineering Process Laboratory is
taught at the senior level over two quarters, and
has proven to be successful for a class size under
forty, with the involvement of two faculty mem-
bers and a teaching assistant.
Our main goal is to provide an environment in
which the students have a large degree of control
over the direction of their work. Students are
skilled at following instructions and obtaining
solutions to well-posed problems, situations which
are not likely to occur in industry. We would like
them to develop the ability to formulate a problem
in process analysis and design, design and perform

Skip Rochefort received his BS from the University of Massachusetts,
his MS from Northwestern University, and is currently working toward
his PhD at the University of California, San Diego. He also worked
at the AT&T Bell Research Labs after receiving his MS. (R)
Stanley Middleman earned his baccalaureate and doctoral degrees
at The Johns Hopkins University and was a professor of chemical engi-
neering at the University of Massachusetts before coming to the

University of California, San Diego. His major research interests are
in the areas of fluid dynamics, especially rheology and polymer pro-
cessing. (C)
Pao Chau is an assistant professor at the University of California,
San Diego. He received his BS from the University of Delaware and
his PhD from Princeton University. (L)

Copyright ChE Division, ASEE, 1985


experiments to elucidate the problem, analyse the
data and present pertinent results in a concise
form, and draw conclusions in support of recom-
mendations of further action.


The structure of each lab group is similar to
that of an industrial process research and develop-
ment group, with a project head (faculty advisor),
group leader and group members, and technical
support staff. A fairly general problem statement
is presented by the project head and the students
are instructed to arrive at the "best solution" to
the problem given constraints in funds, equipment,
and time (ten weeks). An example of a typical
problem statement is shown in Fig. 1. (Blax/
Beech, Inc. is a pun on Black's Beach, a local nude
beach and prime surf spot.)
The students are expected to outline an experi-
mental approach to the problem, design and build
the necessary experimental apparatus, perform
appropriate experiments, and analyze the data.
The design and construction process includes se-
lection of material, pumps, valves, fittings, etc.,
and interaction with the technical support staff
who do most of the machining. The lab group also
has to select appropriate analytical and measuring
devices (e.g., gas chromatograph, viscometer, pH
meter, thermocouples, etc.), as well as proper data
acquisition procedures (e.g., IBM PC with A/D
card, multichannel DVM, strip chart recorder,
etc.). Once they have selected a device, the students
are expected to learn from instruction manuals
provided by the manufacturers, and to perform
all necessary calibrations. No exceptions are made
with the more expensive equipment such as gas
chromatographs, a Brookfield viscometer, or IBM
personal computers. The technical staff is avail-
able for consultation but only intervenes when
procedures undertaken by students may endanger
the equipment or themselves.
During the planning phase, the students are
encouraged to contact local industry for ideas, and
to consult equipment manufacturers and field
representatives when necessary. They are also
urged to examine and keep abreast of the current
research literature in their problem area over
the project duration. During the second quarter
of the laboratory, they are encouraged to apply
what they have learned in computer-aided design
and process design courses to the modeling and
design of their experiments.

During the past four years, the
laboratory has evolved as a setting in which
our seniors refine the classroom skills they have
acquired and attack problems under circumstances
similar to industrial experience.

Blax / Beech Inc.
Design Consultants to the Chemical Process Industries
La Jolla, California

Date: January 10, 1985
To: CVD Reactor Group
From: Stanley Middleman, Director
Re: Mass Transfer in a CVD Reactor
Chemical Vapor Deposition (CVD) is a heterogeneous reaction process by
which various chemical species may be deposited as very thin films on silicon
wafers. In the manufacture of semiconductor materials, CVD reactors provide a
means of contact of a gas mixture with a set of wafers. One problem in design of
such reactors lies in the fact that mass transfer may affect the deposition rate, and
that the rate of mass transfer may not be spatially uniform in a CVD reactor.
You are to design an experimental system with which you can explore factors
that affect the rate and degree of uniformity of mass transfer in a CVD reactor.
Beginning January 17, and each week thereafter, I expect to receive a typed
progress report. We shall also have a weekly meeting at which time your group
will make a twelve minute oral presentation to the class on progress and plans for
future work. A final presentation is to be given during the week of March 13 and
a final report is to be in my hands on March 19.
Please do not hesitate to contact me if you need any technical or administra-
tive help in facilitating your progress.
FIGURE 1. Problem statement to CVD lab group.

Strong emphasis is given to oral and written
communication skills. Each week the group meets
with the project head to discuss the project and
present a written progress report. Project goals
may be modified if justified by preliminary experi-
mental results or other extenuating circumstances.
The group also has to give weekly oral presenta-
tions to the entire class.

Students work in groups of three or four. After
receiving their problem statement, they have two
weeks to research the problem area, check out the
available resources, consult with the project head,
specify the goal and postulate the strategy to solve
the problem. The project head mainly serves to
provide insights as to whether the proposed pro-
ject is feasible, trivial, or too ambitious for a ten-
week period.
The next four weeks are spent either in con-


struction of new equipment or in modification of
an existing apparatus, in performing preliminary
experiments and in making further equipment
modifications as required. Students are required
to submit a mock purchase order for supplies and
a job order requesting the assistance of the techni-
cal staff in building equipment. To avoid time lag,
the lab has to stockpile common items such as
rotameters, glassware, valves and fittings. Pre-
liminary experiments usually entail equipment
calibration, determination of necessary thermo-
dynamic and physical properties data, solution
preparation, and at least several trial runs of the
experiment. The main purpose of these prelimin-
ary experiments is to allow the students to become
familiar and comfortable with the new equipment
and to develop clean and efficient techniques. In
the process they also learn the importance of care-

Chemical Process Laboratory
Oral Presentation Evaluation
Lab Group: Date:
Category Poor Good

1. Presence 1 2 3 4 5
(Posture, Voice,
Eye contact, Delivery)
2. Visual Aids 1 2 3 4 5
(Effectiveness, Clarity)
3. Length of Talk 1 2 3 4 5
4. Audience Contact 1 2 3 4 5
(Audience stimulation,
Response to questions)
5. General Organization 1 2 3 4 5
(Introduction, Body,
Summary, Clarity)
6. Technical Content 1 2 3 4 5
(Was any work done?
Data presentation and
7. Overall Effectiveness 1 2 3 4 5
8. If you were this person's boss,
would you give him/her a raise?
Would you continue funding for the

FIGURE 2. Oral presentation evaluation form.

ful planning of experiments and the validity of
Murphy's Law in experimental research.
The remainder of the ten-week quarter is used
to perform final experiments, analyze data, and
prepare final oral and written reports.
During the course of the quarter, the groups
are required to submit a weekly progress report
(five to eight pages). The grading of the report is
broken down into technical content and style. Ex-
tremely strong emphasis is given to proper writing
style at the beginning of the first quarter. As the
writing improves, the grading emphasis moves
more toward technical content, much like a
refereed journal article might be critiqued. The
group leader, who rotates every week, has to edit
the report and do the rewriting if requested. Be-
cause report revisions are often requested, word
processing of the reports is encouraged, using the
CATT system on VAX or WordStar on the IBM
PC. Over two quarters and including the final re-
ports, each student should have participated in
writing sixteen reports.
For the weekly oral report, students are re-
quired to give a twelve- to fifteen-minute presenta-
tion in which the use of visual aids (either trans-
parencies or slides) is mandatory. The presenta-
tions are critiqued immediately after each session
by the instructor for the benefit of all. Evaluation
forms (Fig. 2) from classmates are passed on to
the speaker after the instructor has reviewed them.
Students sometimes find that the harshest com-
ments come from their peers.
We schedule two separate oral presentation
sections per week, each under the supervision of
one of the instructors assigned to the laboratory.
Lab groups are rotated in a staggered fashion
through these sessions over the quarter. Thus each
student faces a different audience for each talk.
Moreover, the entire class is exposed to all the
different experiments being conducted in the lab.


We have listed in Table 1 the experimental
projects that were carried out during the 1984-85
academic year (2 quarters; 20 weeks). The ob-
jectives listed are a synopsis of the general prob-
lem statement which was presented to each lab
group at the start of the project.
Several of these experiments are interrelated
and provide an opportunity for productive com-
munication between groups. The gas-lift reactor
experiment permits examination of gas-liquid


mass transfer in a reactor uniquely designed for
the algae growth experiment. The effects of sparg-
er design, bubble size, gas flow rate, and solution
electrolyte content on oxygen mass transfer are
examined, with special attention given to their
role in algae growth.
The aerated stirred-tank experiment keys on
mixing and oxygen mass transfer problems in
microbial exopolysaccharide production, which is
of interest to a local company (Kelco). Through
pre-arrangement on the part of the instructors,
specific members of the technical staff of Kelco are
available to meet with students and provide con-
In the gas absorption experiment, in-line static
mixers are used to study carbon dioxide absorp-
tion into a dilute sodium hydroxide solution in a
cocurrent pipe flow configuration, as might be
applied to an industrial "gas sweetening" pre-
treatment process. The system was donated by
Komax, which is interested in obtaining perform-
ance data for its Komax Mixers in this type of ap-
Engineers at Chevron Oil Field Research
(COFR) in nearby LaHabra first stimulated our

interest in the use of dilute polymer solutions in
enhanced oil recovery. Using information they pro-
vided, the students were able to set up an experi-
mental study of the effects of polymer configura-
tion in dilute solution on the removal of oil from
packed beds. Cylindrical and two-dimensional
planar beds with various bead and sand packing
have been used. Typical oil recovery polymers,
supplied by Kelco and Dow Chemical Co., have
been used in both pure water and brine solutions.
A variety of experiments have been conducted
over the past several years, ranging from single
"oil blob" movement in a bed with a monolayer
of uniform glass bead packing, to bulk oil dis-
placement from a cylindrical sand packed bed.
Parameters of interest are polymer concentration
necessary for oil displacement, polymer degrada-
tion and adsorption in the packed beds, and the
effect of salts on these results.
The chemical vapor deposition (CVD) experi-
ment required the design of a model of an in-
dustrial CVD reactor for the purpose of studying
mass transfer effects on the vapor deposition pro-
cess. The development of this experiment was
greatly influenced by contacts with researchers in

Experimental Projects in 1983-84


1. Mass Transfer in CVD:
To study the role of mass transfer in chemical vapor
deposition processes.
2. Enhanced Oil Recovery/Porous Media Flow:
To study efficiency of polymers in enhanced oil re-
covery. To look into effects of theology, polymer
degradation and adsorption. Flow visualization of
oil "blob" movement in porous bed.
3. Mass Transfer in gas-lift Reactor:
The analysis of oxygen mass transfer in fermenta-
tion systems. Effect of electrolytes and fluid proper-
ties on bubble dynamics. Reactor and sparger design.
4. Aerated Stirred Tank Mixing:
The study of mixing and gas-liquid mass transfer
in an aerated stirred tank with non-Newtonian
fluids. The application of novel impeller geometries.
5. Gas Absorption:
To obtain design data for a cocurrent pipe flow gas
absorber using in-line static mixers.
6. Heterogeneous Catalytic Reactor:
Kinetics of heterogenous catalytic reactions. To
assess mass and heat transfer effects in catalytic
CO oxidation and methanation reactors.
7. High Fructose Syrup Production:
The study of immobilized enzyme kinetics, enzymatic
reactor design, and ion-exchange column operation
in the production of high fructose corn syrup,

8. Mixing in Chemical Reactors:
To study the effect of non-ideal mixing in the per-
formance of tubular and stirred-tank reactors.
9. Ethanol Fermentation:
Ethanol production in batch and continuous fer-
mentation. Fermentation kinetics and bioreactor de-
10. Algae Growth:
The use of algae in biomass production. Effect of
mass transport and bubble dynamics on the kinetics
of algae growth.
11. Hollow Fiber Membrane Separation:
To study the design problems of hollow fiber separa-
tion of biomass in application to microbial systems.
12. Distillation:
Batch and continuous azeotropic distillation prob-
lems with an isopropanol/water mixture.
13. Liquid-Liquid Extraction:
The mass transport phenomena and design of a
liquid-liquid extraction column with soybean oil as
the organic phase.
14. Plate Heat Exchanger:
To design, construct and operate a plate heat ex-
changer system for use with viscous gelatin solu-
15. Wetted Wall Column:
Study of gas-liquid mass transfer in falling films
of viscous fluids and in the presence of surface-
active agents.


the local semiconductor industry who were drawn
to UCSD, in part, through the spring quarter
Chemical Engineering Seminar Series, which was
developed with the theme "Applications of Chemi-
cal Engineering in Semiconductor Technology."
An experimental system was built in which
naphthalene in a nitrogen carrier gas was de-
posited on the surface of an acrylic disc. The
elimination of chemical reaction from the process
served to isolate the mass transfer phenomena.
In the catalytic reactor set-up we have pro-
visions for either CO oxidation or methanation re-
actions in either packed-bed, recycle, or single-
pellet reactor configurations. All recording equip-
ment, including thermocouples and the gas chroma-
tograph, are interfaced to an IBM PC. A BET ap-
paratus is also available for surface area and
chemisorption experiments. The combination of
all these options allows for a variety of interesting
experiments for the students to plan and design.
A biochemical application of the principles of
kinetics and reactor design is investigated in the
high fructose corn syrup production experiment.
This experiment was implemented with the help
of information supplied by Staley Co., using im-
mobilized enzymes and ion-exchange resins donat-
ed by Novo and Dow Chemical Co., respectively.
The goal of the project is to look at more rational
reactor and process design procedures. Computer
modeling of the reaction/deactivation kinetics is
also included.
Classical chemical engineering kinetics and re-
actor design experiments are conducted by study-
ing mixing in stirred-tanks and tubular reactors.
Mixing, as well as mixing with chemical reaction,
has been studied in any number of reactor
geometries-batch, stirred-tanks in series, tubu-
lar flow with static mixers or packed-beds, and
any combination of these. Residence time distribu-
tions are studied with colored dye tracer and a
spectrophotometer with a flow-through cell.
Along with some of the previously mentioned
experiments which have a biochemical twist to
them, we have a series of experiments which are
more directly oriented towards biochemical engi-
neering. Ethanol production is carried out by fer-
mentation using both single and multiple substrate
growth media. The extensive cell growth, substrate
utilization, and ethanol production data are com-
pared to data generated using classical biochemi-
cal kinetic rate models in computer simulations.
The algae growth experiment was initiated
due to the interest of a group of scientists at

We also have a lab which allows our
students to get acquainted with new industrial
developments, such as microelectronic fabrication and
biotechnology, and with the integration of new
technology... into laboratory experiments.

Scripps Institute of Oceanography. They have
studied the optimum biological growth conditions
(i.e., pH, light, growth medium, and temperature),
while our engineering students concentrated their
efforts on the role of mass transport in algae
growth. As mentioned previously, we have de-
signed a two-dimensional, gas-lift reactor in which
both algae growth and mass transfer experiments
are conducted. The two-dimensional geometry is
useful for flow visualization experiments to deter-
mine bubble dynamics and mixing in the reactor.
The goal is the optimization of algae growth with
respect to mass transfer limitations, while keep-
ing biological parameters constant.
We have used hollow fiber modules donated by
Asahi Medical Co. to conduct simple membrane
separation experiments. The goal is to examine a
process technology for concentrating cell mass in
either cell recycle or biomass production processes.
We do have some conventional chemical engi-
neering unit operations experiments in the lab.
In the distillation experiment, the students have
had to design their own plumbing and control
schemes to convert a three inch diameter, six stage
batch bubble cap column to continuous operation.
The column feed is a cleaning solution provided by
the university glassblower (a 35/65% isopropanol/
water mixture with some minor impurities). Ex-
tractive distillation techniques (e.g. the addition
of a salt into the column) has been applied to pro-
duce an isopropanol/water distillate of 85-90%
purity. The students must also generate their own
thermodynamic data. A gas chromatograph is used
for data analysis and computer simulations of the
distillation column are also conducted.
The liquid-liquid extraction experiment uses
soybean oil as the organic phase, mainly due to
cost and safety reasons, but also because of the
novelty of the process. The operation of the column
for such a viscous continuous phase is quite differ-
ent from conventional extraction processes. The
students must design experiments to examine
transport phenomena in the column (e.g. droplet
coalescence and break-up) and they must deter-
mine solubility data before they can design and
conduct the extraction experiment.


The plate heat exchanger experiment was initi-
ated and financed through a contract received from
Eastman Kodak Co. The interest of Kodak is in
the use of a plate heat exchanger to heat and cool
photographic gelatin solutions. The students must
design and construct the experimental apparatus
and then obtain the heat transfer and design data
required by Kodak. The experimental and logisti-
cal novelty of this project is that the process fluid
is a gelatin solution and the students act as if in
a consulting capacity to a contracting employer.
This program will continue over several quarters
and will require that students study the reports
of preceding groups, building upon their progress.
The wetted-wall column is a standard counter-
current gas/liquid contacting device. The students
are able to change tube dimensions and gas and
liquid Reynolds numbers to examine mass transfer
coefficients in different flow regimes. Water/air
mass transfer data are compared to classical cor-
relations. The use of the column with surface ac-
tive agents and to concentrate viscous aqueous
solutions has also been investigated.

Since our students only work on one project
each quarter (compared with the more standard
rotation of four to six experiments), it appears
that we are sacrificing breadth of exposure to
different processes for in-depth studies of two
topics. However, a single project quite often in-
volves learning how to use several equipment items
or performing experiments (such as generation
of fluid property data) which are frequently used
as separate experiments in rotation-type lab
courses. In addition, students can learn from the
oral presentations and laboratory interactions
with classmates. It has been our experience that
the present system stimulates inter-group inter-
action. Feedback from our graduates reinforces
our opinion that the uniqueness of the present ex-
perience far outweighs it drawbacks.
The two major constraints on the lab are
those that are common to many industrial and
academic projects: time and money. Experimental
set-ups are taken apart every year and, not infre-
quently, even after each quarter. New experi-
ments are frequently introduced and old experi-
ments are rotated in and out depending on student
interest. In the second quarter the students are
allowed to select new experiments of particular
interest to them from among those we have the
facilities to implement. As for old experiments,

objectives often are changed for a new lab group
in the second quarter, and may be different enough
that modifications of the apparatus are required.
To this end, we strike a cautious compromise be-
tween our available resources and our creative
Over the years we have also noticed a certain
latency period in the first quarter of the lab. It
usually takes the students several weeks to adjust
from the cookbook-trained mentality to the point
where they gain the confidence to rely on them-
selves. In several isolated cases we also have to deal
with individuals who are over-enthusiastic and put
unreasonable demands on the technical staff.
Gradually, they all learn to deal with independence,
bureaucracy, lab techs, and fellow group members
who may not have the same motivation or philoso-
Group dynamics are more obvious in the pres-
ent environment, since the lab group has to go
through so many oral and written reports in ad-
dition to interactions with the project head.
Students with leadership qualities, characters with
nonchalent attitudes, goferss," and any possible
strains within a group are quite observable.

We feel that we are successful in developing
the oral and written communication skills of our
students, while providing a forum for innovative
thought. We also have a lab which allows our
students to get acquainted with new industrial
developments, such as microelectronic fabrication
and biotechnology, and with the integration of new
technology, such as microcomputer applications,
into laboratory experiments.
The progress in oral communication skills is
particularly significant and rewarding. We feel it
is a direct result of the fact that each student has
to give a minimum of six talks. (There are ad-
ditional opportunities for oral presentations in the
computer-aided design and process design
courses.) The emphasis is on the student making
a very professional presentation. We have received
quite a number of comments from industrial em-
ployers commending us on the speaking abilities
of our graduates.
The improvement of the writing skills is a
little harder to gauge, even though the students
show obvious progress through the two quarters.
As anyone who has taught a writing class knows,
students have a notoriously high rate of reversion
Continued on page 161.


o M classroom


Worcester Polytechnic Institute
Worcester, MA 10609

THIS COURSE TEACHES the fundamental scientific
principles controlling most chemical, petro-
chemical, and refining processes. The student popu-
lation consists mainly of junior and senior chemi-
cal engineers, but the information is of equal value
to advanced chemistry majors. A few mechanical
engineers interested in plant construction also take
the course. The objective of the course is to pro-
vide the student with a fundamental understand-
ing of the chemical, catalytic and engineering
sciences relating to the chemical reactions taking
place in a variety of reactors of different configura-
tions. Although many major commercial processes
are discussed in the course, the emphasis is not on
an enumeration of all of the major processes, but
the direction is placed on understanding how and
why the chemical transformations occur. This
science is then merged with the technology of the
two dozen or so reactors of radically different de-
signs and configurations currently used com-
mercially. Thus, the student gains an understand-
ing not only of the process fundamentals but also
of the devices used to successfully perform the
processes. The course is kept current each year by
introducing new processes which are in commercial
development. Synthesis gas generation and utiliza-
tion are discussed to address a long range techno-
logical need of engineering and science students.
For the chemical engineering students the course
serves the specific function of allowing them to be-
come more conversant with chemical phenomenon.
This is purposely done in response to the criticism
from both industrial and academic scientists who
feel that the current U.S. training of chemical
engineers is deficient in chemistry. This course has
a chemical orientation but it is placed in the con-
text of learning all of the fundamental sciences
which govern the major commercial processes
which they will deal with in the future. The student
should gain enough fundamental understanding of
the chemical phenomena occurring inside of re-
actors of different designs so that in their future

William R. Moser has been a professor in the chemical engineering
department at Worcester Polytechnic Institute since 1981. Since earn-
ing his graduate degree in 1964 at MIT he has been active in the area
of chemical processing at CIBA, Exxon, and Badger. His research
interests are in mechanistic studies of heterogeneous and homo-
geneous catalyzed reactions using kinetic and in situ spectroscopic
techniques. He has several publications and patents and holds mem-
bership in a number of professional societies.

work they will be able to execute superior process
designs and controls for these or other new pro-

The prior requirements for the course are a
fundamental organic chemistry course, an intro-
ductory inorganic chemistry course (usually in-
cluded in the freshman chemistry series), and a
keen interest in chemical engineering and chemical
processes. Since the course is descriptive and
qualitative, prior chemical engineering courses in-
volving quantitative engineering calculations are
not required.
A successful presentation of the technology de-
scribed by this course requires the application of
several principles of chemical engineering, organic,
inorganic and physical chemistry, thermo-
dynamics, kinetics and mechanical engineering.
Thus, the instructor must make a careful choice
as to the degree of review of these subjects which
is adequate for the understanding of the chemical
process technology. The approach currently used
at WPI is to provide a concise review of just those
principles which are required to master the chemi-
Copyright ChE Division. ASEE, 1985


cal process concepts presented in the lecture of
the day.


The technology presented in the course is ac-
complished in 24 lectures of 50 minute duration.
In addition to outside reading from a list of 89
references taken from the original technical litera-
ture, three term papers are required on topics
which are not discussed in the classroom lectures.
Three one-hour, closed note and closed book exams
are usually given during the duration of the
course. The textbook currently used for the course
is Chemistry of Catalytic Processes by Gates,

Katzer and Schuit (McGraw Hill, 1979).
The course is divided into the following eight
major topics:

1. Survey of Major Chemical and Refining Processes
2. Homogeneous Catalytic Process Fundamentals
3. Heterogeneous Catalytic Process Fundamentals
4. Survey of Modern Commercial Reactor Configura-
5. Synthesis Gas Generation
6. Synthesis Gas Processes for Fuels and Chemicals
7. Technology of Major Advanced Chemical Processes
8. Major Refining Processes

The division of lecture time committed to each
topic may be seen in Table 1. The timing of exams
and due dates for term papers is also shown. A


Chemical Technology: Course Schedule

13 Reactor Configurations for Major Processes


Survey Major Chemical Processes
Homogeneous Metal Catalysis
(A) Major Processes

3 Homogeneous Metal Catalysis
(B) Co-ordination Chemistry
(C) Bonding
(D) Reactivity
4 Homogeneous Metal Catalysis
(E) Metals
(F) Stereochemistry
(G) Key Intermediates
5 Homogeneous Metal Catalysis
(H) Key Transformations
6 Homogeneous Metal Catalysis
(I) Ligand Effects on Reactivity
(J) Classification of Reactions
7 Heterogeneous Catalysis
(A) Major Processes
8 Heterogeneous Catalysis
(B) Surface Adsorption
(C) Surface Kinetics
9 Heterogeneous Catalysis
(D) Surface Chemistry
Problem Set #1 Due-Ziegler-Natta Catalysis

10 Heterogeneous Catalysis
(E) Types of Catalysts

11 Heterogeneous Catalysis
(F) Zeolites and Their Structures

12 Heterogeneous Catalysis
(G) Zeolites and Their Catalysis

14 Synthesis Gas Catalysis and Synthetic Fuels
15 Synthesis Gas Production Processes
(A) Reforming
16 Synthesis Gas Production Processes
(B) Gasification
(C) Downstream Processing
17 Synthesis Gas for Chemicals and Fuels
(A) Methanol Synthesis
Problem Set #2 Due-Catalytic Cracking
18 Synthesis Gas for Chemicals and Fuels
(B) Methanol to Aromatic Gasoline
(C) ZSM-5 Catalysis
19 Synthesis Gas for Chemicals and Fuels
(D) Fischer-Tropsch Catalysis
20 Synthesis Gas for Chemicals and Fuels
(E) New Syngas Processes for Ethanol, Vinyl
acetate, and acetic anhydride
Problem Set #3 Due-Heterogeneous Partial
21 Synthesis Gas for Chemicals and Fuels
(F) New Syngas Processes for Ethylene Glycol,
Styrene, Xylenes
22 Advanced Technology for Chemical Intermediates
(A) Acetic Acid
23 Mature Technology for Chemicals
(A) Wacker Process
(B) Butane Oxidation
(C) Hydroformylation
24 Refining Processes
(A) Hydrodesulfurization
(B) Reforming


brief description of the topics treated in the lec-
tures for the eight major areas listed above

1. Survey of Major Chemical and Refining Processes
The topic is introduced with a definition of the
four principal types of reactions utilized in com-
mercial reactors, e.g. heterogeneous catalyzed,
homogeneous catalyzed, gas phase catalytic and
non-catalytic, stoichiometric reactions in solution
with their individual variations. Examples are
given for each class. Also terms like conversion,
selectivity, yield, etc., are defined.

2. Homogeneous Catalytic Process Fundamentals
Examples are given of the top fifteen com-
mercial processes using homogeneous catalysts.
The student would be expected to know the re-
actants, products, catalysts, and approximate re-

The objective of the course is to
provide the student with a fundamental
understanding of the chemical, catalytic and
engineering sciences relating to the chemical
reactions taking place in a variety of reactors
of different configurations.

action conditions for each process. Several new
processes which are currently being considered for
commercialization are also listed.
This section includes the important funda-
mental information on homogeneous catalysis.
Thus, the key coordination chemistry principles
required to understand the homogeneous catalyzed
process (to be described later on) are tightly re-
viewed and discussed. A few of the concepts dis-
cussed are: elements of crystal field-molecular
orbital theory; metal d-orbitals; d-electron activa-
tion of coordinated ligands; coordination stereo-
chemistries of transition metal complexes; count-
ing d-electrons; eighteen electron rule; key inter-
mediates in homogeneous catalysis like metal car-
bonyls, hydrides, alkyls, etc.; key transformations
in homogeneous catalysis like oxidative addition,
insertion, electron transfer, etc.; ligand electronic
and steric effects such as pi-acceptors, sigma-
donors, cone angles, etc. Then the basic sub-classi-
fication of homogeneous metal catalyzed reactions
like main group and transition metal catalysis, bio-
catalysis, phase transfer catalysis, polymer sup-
ported catalysis, etc., are briefly described. The
typical kinetic treatments and methods for spectro-
scopic analysis are also illustrated.

3. Heterogeneous Catalytic Process Fundamentals
Fifteen examples are given of major com-
mercial processes in terms of reactants, products,
catalysts, and conditions, along with a brief dis-
cussion of a dozen other processes.
The fundamental aspects of heterogeneous
catalyzed processes are discussed by reviewing
principles of the chemistry and physics of surfaces
and surface adsorption, e.g. macro- and micro-
pores, Knudsen diffusion, chemisorption and physi-
cal adsorption; Langmuir-Hinshelwood and Ri-
deal-Eley surfaces kinetic models, competitive
chemisorption and catalyst poisoning; surface
intermediates and surface chemistry.
This section also discusses the major sub-
categories of heterogeneous catalysts like support-
ed and unsupported reduced metals, solid state in-
organic catalysts, carbon catalysts, clays and zeo-
lite catalysts. Several examples are given for each
A detailed discussion is devoted to the struc-
ture, physical and chemical properties, and cataly-
tic properties of zeolites. Some of the topics dis-
cussed are X- and Y-type zeolites and ZSM-5 struc-
tures, modifications and molecular build up; pore
openings and crystal structure; super acidity and
super basicity; and a four component model for
rationalizing the unusual activity of zeolite cata-
lysts. The student is also introduced at this point
to the relationship of shape selectivity and con-
straint index to the crystal and catalytic proper-
ties of zeolites. An assortment of several classes
of zeolite structures is illustrated with 35 mm
slides and three dimensional molecular models.
Support materials used in heterogeneous catalyzed
processes and their criteria for selection are briefly

4. Survey of Modern Commercial Reactor Configurations
Drawings of fourteen of the reactor configura-
tions used commercially in both heterogeneous and
homogeneous catalyzed processes are supplied to
the student, and an example is given of a com-
mercial product produced using each configura-
tion. Within the discussion of these reactor con-
figurations, the various thermodynamic, heat
transfer, kinetic, reactor stability, mixing and
other factors giving rise to the selection of a spe-
cific configuration, are examined. Specific
examples of reactor configurations (process ap-
plications) are as follows: tube and shell (Lurgi
methanol and ethylene oxide process) ; tray re-


actor with interstate cooling (ICI methanol syn-
thesis) ; riser tube (catalytic cracking) ; fluidized
bed (SOHIO acrylonitrile); slurry tank (poly-
propylene) ; radial bed (styrene synthesis) ; and

5. Synthesis Gas Generation

The major processes used in the production
of synthesis gas are discussed along with their
feedstocks and gaseous product compositions. The
thermochemistry of each process is related to
thermal and pressure effects on the syngas pro-
duct ratios and to its consequence on the reactor
design. Drawings for several process reactors such
as methane reforming, partial oxidation, Lurgi
non-slagging gasifier, Koppers-Totzek gasifiers
and the Bi-Gas slagging gasifier are provided to
the student along with a discussion of each. A
survey of next generation gasifiers is given.
Post gasifier processing of raw syngas through

water gas shift, bulk and trace sulfur removal pro-
cesses, CO, removal and CO separation from H2
is discussed. The chemistry of a Claus plant and
Stretford plant is summarized.

6. Synthesis Gas Processes for Fuels and Chemicals

A survey of all commercial and potential fuels
and chemicals processes using a syngas feedstock
is given with reactants, products, catalysts, and
reaction conditions. Details of the thermochemis-
try of methanol synthesis and its consequence on
the evolution of the ICI, Lurgi and Chem Systems
reactor and process configurations are discussed.
The student is introduced to conventions used in
process stream notations. The low pressure
catalyst structure and syngas to methanol surface
reaction mechanism are presented.
A detailed discussion is given to the conversion
of methanol by the Mobil M process to aromatic
fuels. The details of the ZSM-5 catalyst structure,

Exam: Heterogeneous Catalysis Fundamentals and Commercial Reactor Configurations

Part 1. Describe the following commercial processes using
structural formulae of starting materials, major
products and heterogeneous catalysts required in
the process
(A) Sohio Ammoxidation
(B) Styrene Process (Two Steps)
(C) Maleic Anhydride Process
(D) Catalytic Hydrodesulfurization Process
(C) Fischer-Tropsch Process
(D) Mobil M Process
Part 2. A. Describe the following adsorption processes
for gaseous molecules on catalytic solid surfaces.
Give examples of each.
1. Physical Adsorption
2. Chemisorption
3. Competitive Chemisorption
B. Briefly describe how a Langmuir-Hinshelwood
surface kinetic mechanism differs from a Rideal-
Eley mechanism. Give an example of each.
Part 3. Draw the structural formulae of the following
heterogeneous catalytic surface intermediates
(A) Surface alkyl
(B) Selective surface oxidant
(C) Non-selective surface oxidant
(D) Surface hydroxy Carbene
(E) Bronsted acid surface site
Part 4. Discuss the following properties of zeolites
(A) Compare the 3A, 4A and 5A molecular
sieves in terms of
(1) ions used to modify these zeolites
(2) size of pore opening for each

(3) example of molecules absorbed by each
(B) Briefly compare the structures and differ-
ences in composition of the X- and Y-type zeo-
(C) Describe the "Supercage" in a com-
mercial catalytic cracking catalyst in terms of
(1) its geometric form and number of sides
(2) size of its largest pore opening and (3)
internal cage size.
(D) Why are zeolite catalysts as much as
10,000 times more reactive than amorphous
aluminosilicates in catalytic cracking?
Part 5. (A) Sketch the reactor section for a commercial
radial bed reactor showing the inlet reactant and
product effluent locations and catalyst bed con-

(B) Why would one use such a complex reactor
configuration in a commercial process?

(C) Sketch the reactor configuration for a typi-
cal trickle bed reactor used in catalytic hydro-
sulfurization in a refinery.

(D) What essential task does the trickle bed re-
actor perform which other designs do not ac-
(E) What is a typical contact time in a riser
tube reactor and which of the following catalysts
would a refiner use in this reactor for catalytic
cracking: (a) ZSM-5, (b) X-type zeolite, (c) Ca-
Y-type or (d) rare earth-Y-type?


acidity, and shape selectivity are merged with a
detailed evaluation of an intercrystalline surface
mechanism to understand the product distribution
and catalyst stability.
A thorough discussion is devoted to the ARGE
fixed bed and fluidized bed SASOL processes for
the direct conversion of syngas to fuels. Catalysts,
reactor configurations, slides of the Sasol II Plant,
surface reaction mechanistic models, Schulz-Flory
kinetics and thermochemistry of syngas conver-
sion to various products are parts of these lec-
The lectures on the conversion of synthesis gas
to chemicals is less oriented toward reactors and
total processes; rather, they concentrate more on
the detailed reaction mechanisms, using the per-
tinent coordination chemistry intermediates, to
rationalize the conversion of syngas to various
products. This is the first opportunity that the
student has in the course to apply the funda-
mentals learned earlier to homogeneous and
heterogeneous catalyzed processes. Some of the
processes discussed are: acetic anhydride, acetic
acid, ethylene glycol, vinyl acetate, and ethanol.

7. Technology of Major Advanced Chemical Processes
This section also concentrates on reaction
mechanisms for both homogeneous and hetero-
geneous catalyzed processes. Aromatic side chain
oxidation and butane oxidation to acetic acid are
described by listing each of the proposed indi-
vidual, elementary reactions required to form pro-
ducts. The coordination chemistry of the Wacker
process, Carbide and Shell oxo-processes, Halcon
propylene oxide process and others are illustrated.
Likewise, the proposed surface mechanisms for the
super basic zeolite catalyzed conversion of toluene
and methanol to styrene and ZSM-5 zeolite
catalysts for p-xylene production are explored
along with several other.

8. Major Refining Processes
The principal processes utilized in a modern
refinery are surveyed. A few of the processes like
hydrodesulfurization are described in detail by
way of an examination of the crystal chemistry of
the catalyst, processing of various feedstocks, and
reactor configuration. Most of the students' under-
standing of catalytic reforming, and catalytic
cracking comes from assigned textbook reading.
Several of the processes are viewed by 35 mm
slides of various refinery units.


Three term papers are assigned for the purpose
of examining the details of several important
areas of chemical and petroleum processing tech-
nology which are not covered in class. The empha-
sis in the papers is to provide a concise descrip-
tion of the major scientific and engineering aspects
of the technology. In the past, Ziegler-Natta
catalysis, catalytic cracking, and technology of
heterogeneous, hydrocarbon partial oxidation
were assigned.

Three one-hour exams are usually given which
cover all material discussed in class. These exams
are closed notes and books and are given soon
after the subject matter is discussed in class.
No comprehensive final has been given until now.
Table 2 shows a typical exam, given in March of
1982. The high grade was 99, the low was 41, and
the class average of 53 students was 70. O

Continued from page 127.

thanks go to Colin Pritchard, Norman Macleod,
Mike Davidson, Jack Ponton, Don Glass, Leong
Yeow and Jeff Lewis.

1. Macleod, N., and R. B. Todd, Int. J. Heat Mass
Transfer, 16, 485, 1973.
2. Kapur, D. N., and N. Macleod, Ibid, 17, 1151, 1974.
3. Paterson, W. R., R. A. College, J. I. Macnab, J. A.
Joy, to be submitted to ibid, 1985.
4. Paterson, W. R., A. K. Banerjee, N. P. Clark, D. C.
Knott, N. P. Wooley, to be submitted 1985.
5. Scholtz, M. T. and O. Trass, AIChE J, 9, 548, 1963.
6. Bennett, C. 0. and J. E. Myers, Momentum, Heat
and Mass Transfer, 3rd ed., McGraw-Hill, Japan,
p 516-7, 1982.
7. Gover, T. A., J. Chem. Educ., 44, 409, 1967.
8. Crosby, E. J., Experiments in Transport Phenomena,
Wiley, NY, p 139, 1965.
9. Bird, R. B., W. E. Stewart, E. N. Lightfoot, Trans-
port Phenomena, Wiley, NY, p 594, 1960.
10. Williams, R. D., Chem. Eng. Educ., Winter, 28, 1974.
11. Paterson, W. R. and D. L. Creswell, Proc. 4th Int./
6th Europ. Symp. Chem. Rn. Eng., Heidelberg, p
121, 1976.
12. Creswell, D. L. and A. M. Santos, Chem. Eng. Sci.,
35, 283,1980.


Continued from page 135.
Another important refinement is to modify the
impeller in the "mixer" which is a small centri-
fugal pump that blends together the reactant
streams entering the reactor tube. In our particu-
lar reactor geometry, the impeller of the pump
sent rapid pressure pulses back to the dye rota-
meter causing violent fluctuations of the bead in
the dye rotameter. Our solution was to replace the
impeller blade with a flat disc. The rotation of the
disc generates sufficient shear to blend the
R. R. Hudgins
University of Waterloo

Continued from page 147.
these packages. To this end an increased student
awareness and familiarity with these facilities
can only be beneficial. OE

The author wishes to acknowledge assistance
and co-operation from the following members of
staff: A. M. Gerrard, J. Notman (Department of
Chemical Engineering), P. R. Bunn (Department
of Electrical, Instrumentation and Control Engi-
neering), and research students J. C. Cheow, S.
Acey, and C. K. Goh.

1. "Control of a Gas Absorption Column using the
Self Tuning Regulator," C. K. Goh, J. C. Cheow,
P. R. Bunn, and B. Buxton. Paper presented at Insti-
tute of Measurement and Control Symposium "Ap-
plication of Multivariable System Techniques", 31
October to 2 November 1984, Plymouth, UK.
2. Annual Research Meeting, Bath, 4 April 1984. Heat
Transfer, Catalysis and Catalytic Reactors, 247.
Heavy Oil Cracking. S. Acey, J. C. K. Lee, J. R. Walls.

Continued from page 155.
to bad habits as soon as they stop writing regular-
The feedback from the students has been ex-
tremely positive. They fully enjoy the opportuni-
ty to work on what they regard as their own
problems. We have not come across a course which

puts so much demand on the students but receives
so few complaints. (The actual lab work extends
well over the regular six hours per week scheduled
in addition to the time required for report writing
and preparing oral reports.)
The support from industry has also been en-
couraging. We continually receive financial aid and
equipment donations as well as new ideas for ex-
periments. In the next year we expect to receive
an industrial scale CVD reactor, a spin coating ap-
paratus and an experiment to perform membrane
separation of gasses. Our lab course would not
have been so successful without this continued
support. D

We would like to thank our industrial support-
ers-Chevron, Kelco, Eastman Kodak, and Komax
-for their donations of equipment, materials, in-
formation, and money. Finally, we are indebted
to the AMES department technical support staff-
Joe Robison, Paul Engstrom, Ray Hummer, and
Jon Haugdahl-for their continued help and
understanding (both with students and instruc-

REVIEW: Cost Engineering
Continued from page 119.
other new topics added to the first edition such
as an analysis of overtime costs, information on
rework costs, and the handling of back charges.
These topics are illustrated by actual industrial
examples. Additional new information on bulk
material control, monitoring construction field
labor overhead, labor productivity, and forecast-
ing direct labor are illustrated with other in-
dustrial examples. The chapter on contingency
estimating and its application to cost control has
been rewritten to reflect recent developments. The
treatment of estimate types and accuracies like-
wise has been updated. Because of the omnipres-
ent computer, an introduction to computerized
estimating has been added since the first edition.
Advice is provided on how to go about computeriz-
ing routine estimating tasks.
This edition is the first book in a planned
series of about 20 which concern cost engineering
and related topics. Of the twenty, six have al-
ready been published. This series will cover the
whole gamut of cost engineering topics for the
student and for the practicing cost engineer. D


views and opinions


One Way to Keep Up With Technology and Education

University of Colorado
Boulder, CO 80309

A GREAT DILEMMA IN engineering education is
how an individual can become an excellent
teacher and also keep up with the latest technical
developments in his field. This is especially diffi-
cult during this present period of rapid techno-
logical advance in many fields, such as computers,
and the emergence of new fields, such as biotech-
What are some of the problems associated with
an academic professional keeping up in both
technology and education? An instructor normally
has had little or no formal training in educational
skills. Also, at many schools there is a lack of
emphasis and a lack of rewards for good teaching.
This makes it difficult for an individual to develop
the necessary skills to be a good teacher. In
technical research, the emphasis at many universi-
ties is to obtain contract research. This in itself
is a difficult task. Once the funding is obtained,
it may be very difficult to perform good work due
to a lack of graduate students, poor laboratory
and/or computer facilities, or an inadequate li-
There are many possible avenues to solving
this problem. Sabbaticals, leaves of absence, con-
sulting, and graduate research are all possible
means for keeping up with technical advances,
while attending educational meetings and semi-
nars can help to improve teaching skills. This paper
describes an approach that the author has used
to keep up with both technology and education:
combining technical work at a national labora-
tory with an adjunct faculty position at a uni-
At a time when there are still many unfilled
faculty positions, this approach provides one
method to deal with the problem. Some faculty

Copyright ChE Division, ASEE, 1985

Some Benefits of An Adjunct Position
Develop teaching skills
Conduct technical research
Modern facilities
Interaction with students
12 month salary
Employee morale
Public relations
Highly skilled employee
Student labor
Recruitment of students
Inexpensive labor
Additional faculty
Public relations
Added technical skills
Exposure to modern technology
Work with modern facilities

may view an adjunct position as a temporary (one-
to three-year) method to develop research skills
while still "keeping up" educationally.

I currently have a position as a chemical engi-
neer doing research in mass transfer separations
at a national laboratory. My job description also
allows me to teach one course per semester as an
adjunct faculty member. I teach one graduate
course and one undergraduate course in transport
phenomena (the same subject area as my techni-
cal work). The laboratory allows me time to per-
form my teaching duties and to attend education-
al meetings such as the ASEE annual meeting.
The chemical engineering department pays my
travel expenses to these educational meetings in
lieu of salary. An outline of some benefits is shown
in Table 1.


Richard D. Noble received his B.E. degree in 1968 and M.E. de-
gree in 1969 from Stevens Institute of Technology. In 1976, he received
his PhD degree from the University of California, Davis. His current
research in liquid membranes, transient heat transfer, and problem
solving skills.

What are the benefits to me? I can continue to
use and improve my teaching skills by continued
teaching and by attendance at educational meet-
ings. I keep up with the material in the area of
transport phenomena by continued teaching and
technical research, and I keep up with the techni-
cal advances in my field by conducting research
and attending technical meetings. I can use up-
to-date facilities to conduct research. I get to inter-
act with both undergraduate and graduate
students and work with them on research projects.
Continued educational and technical work allows
me to publish in educational and technical
journals. I also have a 12-month salary, so I do
not have to develop additional summer support
for myself.
What are the benefits to my employer? First,
they have a happy employee. If I am enjoying my
job, they benefit. They also get the public relations
benefit of demonstrating their support for higher
education by having an adjunct faculty on their
staff. They have an employee who is technically
"up" in his field through continued teaching in his
subject area, and they enjoy the benefits of
"cross-fertilization" through interaction with uni-
versity colleagues. The employee also develops
communication skills through teaching. Students
work at the laboratory for a small salary or for
credit (no salary), so the labor force is inexpensive
and usually productive. Some of the students may
decide to work for the employer upon graduation
because of their work experience, so there is also
a recruitment aspect for the employer.
What are the benefits to the university? They

get "cheap" labor in a time of fiscal restraints and
they get a faculty member in a time of faculty
shortages. They get the public relations benefit of
having teachers who have up-to-date technical
knowledge, and they also get additional technical
skills in their department.
Last, but not least, what are the benefits to the
student? Students are exposed to modern tech-
nology as it is introduced in the classroom by the
adjunct instructor. They have an instructor who
is "up-to-date" and who can translate the concepts
learned in class to new developments in technology.
For students who work with the adjunct professor,
there are added benefits. They get to use modern
"state-of-the-art" equipment, and through their
work they can gain experience in certain jobs and
determine if they wish to pursue them after
graduation. For graduate students, working with
modern facilities can make their work more pro-
ductive since they spend less time reducing data
and maintaining equipment.
There can also be negative aspects to this type
of arrangement. Adjunct faculty have little or no
time to meet with students outside of class. If the
adjunct has had limited training in teaching, the
communication of information between faculty
and students can be impaired. A job such as I
have described requires the full and continuing
support of both the employer and the university.
If that support is lacking, it would be very difficult
to do a good job.

Combining technical training with an adjunct
faculty position has been shown to be an effective
mechanism for maintaining technical and educa-
tional skills. Benefits to the individual, the employ-
er, the university, and the student are varied and
important. The particulars of an adjunct position
are often flexible and depend on the interests and
objectives of the parties involved. O

This paper was originally presented at the
ASEE Gulf Southwest Regional Conference, Uni-
versity of Houston, March 13, 1982. A revised
version was presented at the ASEE Summer
School for Chemical Engineering Faculty, Uni-
versity of California, Santa Barbara August 1-6,
1982. I am indebted to the many individuals who
have provided comments during these presenta-


Continued from page 123.
The cold gas is warmed in the heat exchanger
to 650F and leaves with an enthalpy of 161 Btu/
lb. Since the mass flow is the same on both sides
of the heat exchanger, the enthalpy decrease of
the liquid CO, is the same as the enthalpy in-
crease of the cold gas, which is (161-148) or 13
Btu/lb. The enthalpy of the liquid going to the
valve (and entering the condenser) is now (65-
13) or 52 Btu/lb. So the refrigeration is
45,300(148 52) = 4,350,000 Btu/hr
The student recognizes that the high-pressure
heat exchanger might be expensive (he suggests
that the high pressure liquid would flow through
tubes and the 200 psia gas through the shell) and
doesn't know if the extra 590,000 Btu/hr of re-
frigeration would warrant the cost of this ad-
ditional piece of equipment (he hopes that he will
soon get a course which will enable him to answer
such questions).

The possible ramifications of this sort of de-
velopment of a thermo problem are enormous.
But this is a course in thermodynamics and must
move along-there is a lot more subject matter to
cover. The problem has been a good workout in
the use of a Mollier diagram and in the applica-
tion of the first law flow equation to heat transfer
equipment and to a Joule-Thomson expansion, as
well as the calculation of isentropic compression
power. The calculations are simple so as not to
divert the student from the ideas introduced. Ele-
mentary concepts of process design are encounter-
ed (possibly for the first time), and the student
has an opportunity to invent and compare alter-
native process schemes. There is a continuous
feedback from analysis to better design.
There are many angles which can be developed
in the discussion. The book and the course lec-
tures have seemed to suggest that reversible pro-
cesses are highly desirable. What are the ir-
reversible features of the fourth student's flow
sheet? Can they be reduced or eliminated? Can
the common work functions ("availability") be
used to calculate the operation of a wholly re-
versible process. Can a completely reversible pro-
cess be described? Could an expansion engine
be employed? Could the heat exchangers be made
reversible, even with a zero temperature differ-
ence at one end? Is counter-current flow in the

exchangers desirable or necessary? What is the
origin of the stipulation of a 5F minimum
temperature difference? The second student
found the high pressure gas to liquefy partially
in passing through the valve. Is this phenomenon
peculiar to C2,? Could the book formulas for the
Joule-Thomson coefficient be useful? What ex-
perimental procedures were employed to get the
data on which the Mollier chart is based? If we
had had no chart, could we have made useful
calculations? Could we make a similar analysis
for the case of a natural gas well (pure methane;
or 90% methane, 10% ethane)? Would it be
better to use a separate ammonia refrigeration
plant, or possibly some combination of ammonia
refrigeration plus Joule-Thomson expansion of
the gas stream? Where would cooling water come
from in New Mexico? What are water cooling
towers and how do they work? Why 200 psia in
the pipeline? Etc., ad infinitum.

The possibility of introducing design thinking
into theoretical subjects depends primarily on the
interest and competence of the instructor. It can
be done, for some M.I.T. instructors have been
doing it for years. My department's most success-
ful teacher, Dr. W. K. Lewis, has done this sort
of thing all his life. Students in engineering
generally like the approach and find that it helps
them greatly to understand the theory.
The instructor who worries continually about
the things he must "cover" hesitates to "take the
time out" for this sort of discussion. Instructors
often lack the practical engineering background
to do it successfully. Such background (and ma-
terial for good problems) often comes from high-
level engineering consulting work. The rise of
engineering science and the increased consult-
ing work by younger staff members may have
resulted in most of the staff's consulting being
devoted to the more scientific "analysis" kind of
activity, rather than to engineering design. It
might even be suspected that only about half of
the M.I.T. engineering staff are true engineers
in the sense of being competent in design, and that
the reactionn is getting smaller. The most im-
portant single thing M.I.T. can do to improve
the instruction in engineering design is to en-
gage more instructors who are enthusiastic about
the subject and who have not yet become so
enamoured of engineering science that they have
lost interest in design. O



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Full Text


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Ciffil educator u/the Colu rmfo Sc / wol of 1"i 1 1 e


In li,rht ot hia !&to; p,of--1 -,,.lill, _,,..._ ... tinf lato f1"WIU'to -Id 1u.,-.-..-.ltaa."Dmdydid ho. ... -N,-. .-aoan-.,.iuato. .,Jd hlo .__.-,. od>ioor, Or.* oephlhlMM."Aol,....11.ho,....a,.nh .. Nn!2 :.::-:.~ndi:r;;-1~':)putin40mii..per .. a1Ci.-Unlv<,,.ltylhatS.,Oo'rolo fJ~!.sl43~1 aanO..MUnloJ,ol,nbdo,...J""--Aol i&~!l!i a.MIO<--mtent of aatural,.. loequiliobriu ..;, 1,y,t.,.c..,_ .-aoa.-..,.ort,p,-,rati-and...-l _,,,.. ,ai,,I K-,.-1. ._,.-. rap:,oolblo ,..,,,_ri.,.andNttinrt1oo.-01ff0>0tent ro; a hip_,.. .. ,.,....,.. .,pe1, .. f,_ ,._,..,i..i.-,-u.llffl(ln""'htiontoDr. yuhlllnthoo,-ofl,y,Jno .... The..,....,,rw, ,-ll1hod.,..,;n, __ m1>dod-- pll&M..,.llibrio,ondtl>erm,,l<>durtiity ,U t ,an,efo,thoprot-iono]opt>Orlonitioo.thoh!rt, ,0111,o,or11donU,ond thohl~hdos',..ofloti to lloro It> f0lioi-ot-to!" !:irt,t-t<>tn-yNr okloon>boli

..,.1opla,,1lol-that1rilll>oWIMi;lo,__, o,t,,,.,.loo....,.f ..... -,!01adutoU... ll o.....,ft-tlmtto"odJ> :::=~~1.,!",'":.":.:,"'!!,"":.'lo,eor>Nt~~=~~:t:.~J1;r~ : =~f:-~ tr1cs..... ,..,f",..;_.;o,r.-i.. 1.,.-...,.1; ... ,.s..,.-.--u.._....,..,_..,..,..,..m .. ._1o, _.i..,EP I Cll ... _f .. 1 .. ,d .. to1ilo .. plooloo,<,flnf.,,.,,.tio,,u,d,... -rc11.~o,t""""tlM""'thomu AqulnulaU..Thlrteo,,t11Ct"r7,lodont& ;::u;:i:i;: .... i::i..:.::::.d~


o -,~ G" 'nc up ornot, .. on <00tont / th,....t,ninr, Hf.,,.,.. ....,t..n to <00tinually l<,,m..,.. motori o lo,"""no"tool3.ondto;~ lta!MJfo,_ ........... look'-lyatho.."""" "'ulboutlMp,..,,,..,.ollff.rninr.'"l'm mindthotilollodtntlea,-..owu,..or ..,hoo[f ..,n,...~,.outhattho,~, ... ,, ,_ ., ,._,.,.r c...,k I;: ..... ~-.. os,o C-., .,.~ "'"""''"k"


@JD department &Hf 141 TH E UNIVERSITY OF UTAH :

oth<> l let'<)willboO\' a ilab le lnal,ooto, .. ~i::~: ~:. .... :,::: :I: ::I:: lnasoialin 1 with t M!Unl,r>lt>acttNiblOn<,.. u Tl'ntdu tl .. :::h::.~:il~h<~:nr;::~~::.:,::: ." modt,.. =t~;: 1 .:.~ ::,:'i.;":i,~~:i~~~.i~~,;,;: Th o lo pra i ,in~ the ,h,roHo::~:~i7i ~:~:.!~: wNow s nledin 1007 Bylhtnto,.wlthheldtheieb l ditabl. two ,,. rau,ing ""Mod<,n ti-. tho "'"'la' !&. ;~~h~:~a:i~~i~;: :h;it%~~~ : 1 ... he oc demiecha,t,,ofthodmpel<,ntly;i ta ladyat&teofO"lo l ution:oOOit, :;:'!:~.i;..:;~f;.,whl

h-..kl .... olpriud,_,.ih..,withlnlh< .. nt1ra,. tho ann:1&for011U t anc1e,..n,c1 ;::g:.~tE?-7~:g &IL&,...iHPo-laMM&ndlnthou_ .,-..1 .. ..,_.inar.~b)'tho1t-AIClr,E ho!>ttt--...,........, ............ ,.... Tha11M .. rn

llmM Moot -,nblo 10, loorna 00W !O I I, onddo!jo,1..U..,.~1<1 ... f,,..lrat_,~o,lllodat&.oalqUMdat&. ondwri!in,u......,.,t ~~~=:.of:".:E~:a =:.. =...~ oooitiOllandi .,..rojt<1>l t -.rl!h1un:=" ..;.:::.;:::.:.. ~~":..!' !""!' ,::; i3:i~J::;.::~1:~ u nn1ual lnr,,n u it;' in vtperitntn t or Mlin ia ..... ,_ ..... ._ ... .-.... pl,aalo.~ll>dlatlacti._ ~:::~=r:-~:: .._....,.1,..1noe11on.1nu,.1a""'...,.,"'""' vtp,;rimtnlo ,,... ...,.,;o....i or _,lro l ltdMlra-pe,lall .. lon or\d :.:.!;'!.':.!".!'~:m~.~;:i:.~== --.11,r......i...--uliria.s--. disilal-1,ol."""-=... ...,. .... ~~.-tl .. -ot,lo

...... boa-..lloottil .... all)oin,i..ontti ,....i,.,_i,,. .... ,_.,.lt., ... -..... ......... _, ___ rdl lndinp.""' ............... -..... ,.;,iw,--.. ,.1_.,,,1 t'O!IT ESGll'EE IU l

c:13.. CHEMIW ENGINURING DIVISION ACTIYmES Ao-rot<-i1 -ra1...... poc1aof..,....,... ;::t ~=l~~


titf?l v1ews anc1 opinions I AR E W E P AR TI C IP AN T S OR V I C TI MS? .IA.Iii&!! WJ,;J ..,_,. ,,,, .. m .... ,r .. h-.r c.,..~,,,.)M0-:139 ---------...... _...._._,__ ... _____ -------.. .... -------------.. ... ,.,.,ir,,.,i-.::~::::~=-~i!"~.;:.~; ... ncilot lT-laiMon!yL-opn,f--.Tllo_,mli._.llon""'" ,al\l OoodtlloadhOo,Of)'f"' prof....,., r...,,, ,,_.,h onivtnitieo. w 1>o1;,,.. ~h::::..~h !~r~::i,r::~ :?: :;;; .:::.-; Jrioo.we".udl.,._l--.,t --oo11u.. ........ -....i1oi-.n1oc1,p. !..-.:.-:.:=:----"" _::!_.c<>IO!ho~ .. il

l!ib?I classroo m THE TEACHING OF PROCESS DESIGN f;VJTOll'S !-."QTE, Th/<>Uo rio WP<,'*"'"' 0 ,., W, T K. Shttk ""' i 1'5' dU, l, "' .,..,.1 ..... i.. ,.11.1 r .. ..... .,., rocu: w 11 amo "'"""g"', .., .. ...-.,u, 1i1cu, b'd""" tw. -.d A=liloti ... co., .. m,..11, er. l.,ll,,.ga,l'riripolDirinoC"""'/l"'iO.PoI' f; viuriuSWf< ,.,,, ,11;, -a, a;,1.,.;,,.1 ,,..,,., ,.-,.,. ;. "" Juul olliliMli .. o//hroo,pld,origi ... 1-.. ,,;,., abo::r

Nll 1,,..,p,of .,'lo/.,HM,0/Thoi,,,,1 c .. bridg,,.\l,102139 f ,.ug1,,,lf0on,teoand ..... 1,.;,.,..._., r in .. dnJocien"ioaph, .... whioes proft< ,t udentm oybede>-. lopedlnoti....tth,,..,.,ys (a) through dNirn ,_ olm""' to,_ :~~ 1a7-1 ,:.:=:,.,:t:::~. 1 :-!~:;~'!tr~u:: sub joo u In hkh dooi,rn problems te Into,.. ... .,,_.ilhlheteach i niolboo!i

ui< thoo,y th techn;q ... of a n alysi1,l

, .. .... i.;.,,,.......... __ ........,...., ., ... ,, .. .. ...... ....... ...... .. .. .... ... p lo nyobo tr .ct i nd ~:::=:~~ :~..:~ireriro-inkin r -~ i:~%~":~. :ti.':~:~ :7.:~ .. ';""~',:; o/at.,.t,rn1<(11J,... inchttnlc ngi-rin~ lhormodynomiramlle,av,ay.Tl>m><>n ,, .. n,ion hrou~h th e Adiabatie,a,oc,,u .... hop>torool.Thi,>ld guiou,odtop"" d<,..fri,t,ra1io,,foranalur.< 1uoi,,.p lant1o< a t.d .. Head Th oon ;:::.: ::..,::;i.,:oe;;~..!, ~:~ :;.~ i, 5 F (l.o .,.rm,d CO, l u ... at in s '::~ !.\' th< lemp,ratu .. of tho CO l u1 71=~.!~2~:: ::.: ::":: 1~;,..,.,..i1,"1, ,,..,,,;otie 11-. Q and II" ..... ,,. ... lpy ... ,in~tho, a l~ i,tho .. me .. ul)$,..m.Thi o i o,...,l f,omthoMollier diagram lob< l46Blu / bCO Al200poi aCO, thi, en\h&lo, t 5 f' which i t he lo AM F nd200,.;aMr;,1M1Bu / ,,.,_,ir,omt ,uotion ., ,pplledtothe>Dd<,..., ,o lh e ,..fripration mootato 12 Blu / bCO, ll<>ini. Th< a pocilil4io. u ;::r:.; ~;;::;;::;,;:,:1~1~:i,.~ha::: : toberooledn ... ope"'"""2Q'F:tho>ld ,...,a nbormodoolylol5'F oo .. tornaintain tll"ntho o ranpd (i,o


drawollo....... )! TI,e-,i .. 11 1 .T."A"" '""rdior o.-.;l&blo .-,,. ""'"' notmlbotllotfH1yaao "C" ....,, _lll ....... \ltlo,._,.i,u1&tiM,IM,\lodoiq .. ..c;,1o,o.,.;q1heval .. la por1iyllq"'1\td.'nlioio-b'roodllol ... lf ollllotCO,-i.tbeliqll hlJh operat,nrp,-u,..,00,...,.,ldbOlo romplottly 1;.,ott.e<1ot70'fwitllan .. 111.&lpfol011lyA l!t>llb.~lo-U.-.i,U..ol-..U..,._ lr\praliM alt.ii Ibo_ lo J.M1 oo11 -111 -s.uo.-Bt Th tuden\-notkno-,, m0UbloclbJ!htf"'1thatthtdu>,t,rl ""'_,. i ....i1arU.. '1h ol 2 Btu ll>iothtt<1111p,-.Hei...1Mmo<1\hatll ~h"fo~ ==~~-::~::, ,. -- .,-G.11(IIGO)Cl tt'MS)-IMl:ho RI ...... ............. u..,,...<,al<,,latloM aa tho -or thlffl ,t.,..... ,. l,o\ "'"" to the-ro t otheploolinta\16F.Cannotlhl, ld pa lo partially rool lh /e,,;lpa...,.,ld011l"""ir .. .. Tllolll!ni 1oolo,thoti.loto-thotli-to<001tlltllqukl ="! :- -Il la


@;j:j laboratory A JUNIOR Y EAR CHE LAB ORA TO RY W R p,1. n ;11SON u,.;.-.,.;1,.,c .,i,,;,,-g, ... lioglo,.,iCB2311,1. s ~~":"~G:::i:of--=-~=-,p~ ='='~ .,:r:=ico-~~ 'flAnd. Thlo writotP<"'It h woUodwolleolumno. lorino tanc< .h unotlittn MppJ,Tholl'l,-oflhloop __ T ... -:A.__,... ___ ,_, ....... ............ -.. ...... Tn_ .. ,., ... ....... C,,.,ol_ .. __ ..... .... _, ............ ., -c-..,, .... ... .__ ..... l.<: ..,l,o"_ .... N .. ,T,...,.,,Ko1o--,n.,: ., ., .... ...,_ .. 1 0.C.... loo.'lltnl. p,Ito _,.;n.l """'< tho po.-t"Od -\ :n":r~: :;,;o; d;i;:~,:."'\:11:~~,j toot-rod ~ll>o .11-ul'N pN:Nur< dart ~~.s,. ,., 11t ..... 1r, .. ferrunoore,,..-. Tho odoot""' ........ ,,...,.,. wor~ pplojt.o

PAGE 19 1 :t~ ~otiloo,..nt,o.g.olhyl .. l ieOdy thiod

........... ............. 1.11,o,t,-UM,-tto =i~.:..-=.::::.:: ~: ~:!::.-::-:.=:; := .____s-,-o, .. r1.11t<111,.I. u,.)_..,,.._ .. _,..,,_,,,,_ ,.;u,r._,.__.._.,....i,... "'..,.,-,...11w1 ...... ,.,,.,oo,.1__,;p, l~~~;:~s~E -1i.,1;: ..-ith 1-0. C.(ZfC."CZ) z-0.1,. ac,a:i:-o ,......,z1au.o .. 1a1 _...; .. ,.., i. 11...i Llolllolobt .... ,rtl,.Tl,,ooolo-1..-t>Oil otiwnodi,,atpo,...UO-efc.,z.o-A. !,A.up ( { ~ ..i ) _,..,,.._"'"'"-"-.. ,.... .. u..i,,111o1__,,,,.,1oac.zJ.111at ::. -:.: ==~ ~-:...'-::"t,"".."':):"'" TulorV .. dil!_of_,,,.,.,.,,,._ ~--= .~-.:.r.:.i .. ,:; :: ,:-.: "": ;;:to::::~:~f~~ ~~ i~$,'":,~ ... l!rlblol ... "-'lthoohorleotti""" .Heo IC.(1'1,.tJ-C,(5 1 6 ) ol--i_:0 ... 1 n .. u.o.....,ot,,.,.o1u..lopritlm-, thot _,..U.d;.,._-,.., lio. ~n..--oudoailot A ,ia....W. ,..1,u .. 1--.!li-ofir.,_;, _, == I~ u.."-.!..'"!, -=:':,:-:: ....,,t1t&1.n..,.,_o111 .... ha .. ,..,.,1a,. ;r:: x~:..': : 11 ::=. ...:e :,,ou;: c 1 .c.s-ti.o,,.i;1,,..u.o,o111>ocLC1au, _,, ....... po,a11 ..... ;, __ toU.._ol __ lot1>o-.,i..,;-::.r:,.-:-..:.7o':!::..~ U..lolhocd __ _..,lhoiole.....,. olti,o ............. b,ot ...... ...._ n...._nr.uptriaMtloC.....,..~ 11 .,,,,.,..,..... ..... _,, __ ~f2;~S:f~:f ~~j~]i~~tG~~ti~ OUN&l,-,,l,M/lni1<11 .. lXldo, o nd..,.U,&niQ,.


i rt ... HJ;iUi~ FH!lflH!:!IHH!J n ~ q,;, 1 i"Iifiitl!il,hl1,l 11,,i,, f" "~~; p l 1. l 5 lf ~ !' ~ ; ;ii .. l i! .sh ntd, i~::. tn;~r ; Iii lt=;,;1<,i:. jll!'i} !l i .f~J; f : }!iHl rlt r!1: 1 ~!. .ilrlHi,! ''"'" h,i 1U,J,, j,,I lf (!!~ rHI[~ i,.r l!hr


[ilDl cuniculum BASIC INFORMATION SC IE NCE TRAINING FO R CHEM I CA L EN GINEERS Q.11.IU.fl". R .QUl: RM .T'. ASOL..11.aOIII:' ~5:~~~-:r::~:=.;~:.~ 1:~EE::'?:~L~; lol0,rlff.. -""-"---llf-tlN ..-1,.,-poroti,..i,-r1-,-illti,, -,11..-poiood.Tl>eOOjo,:tlytoftlll,pooeri,.., lndktolloo~blo-...,i,c,f_..o_,...Ol>d tortlo ........ upori,.,..,l......,plou&IOQ)'I ,_.m,,11....rrith-"h ln r "'iont!il< Jou,,..1o,-u,,.,;-,y,.Wi!i ... 6ln< lpll "',ltloorlon .... ...... .... __ .. _..,_ :=:,;.:-' .. : ~:::; ... -:_....,._.,._ """"""~llo10-lo01loor"""'"h...t,,..for _, ... ........ 1-o .. ........ -"""' ,_...,, ,llffni,t.,-. -"'-<01 ... r, .... nnr .,,.,. .. 11.,. an d olo< h!,.lonJl1>Nrln1 11"',.,1, 0 ,.-lth,arlooo =~~I :";."."for oubJ.,,., pa,1i<,a1,,1, ot \ht P,l-,rliLo,aluror-!..,._itl>oput,ilol,od ;... ..... 1o, ..... ....... ,... .... ...__,nd :.":!.:~=.... ~7...~~ ;......i..n..-1t,-1a..,..;oi-,,-...,.1_ po,1&1,t,-,limioMio-bftl>o ........ -.,""' .. pd,qbt.,-nu_,. ~-=':i,..~lta.:r -:i::~,-,,.:::..:: c1,..;,.,i.,;-.,,u.,..,,. 1POe 1 .._u_.. -..-..,.....,.c-w1i-,._,..,.., =E,!'~:~~=~-:911 ::J~E~E;.;_:::! ,11os,:,,..,c;,., ~ 1 "'" (SC1l,.-h;

-11,1,1...,,..Mia ti OJOj>liOJIOll1 .. bJect ... _M_ ... __ ... __ ... .................... ----~ _____ ., __ ~ -.................. __ _____ ... __ ___ ..... _,_,,_ ..... _,_ _,.,_ ........ ,,_ .. ___ .... __________ ., ____ ,. __


---loo.l)t:llll' F.STf o,p,olOd ... l'~F.VICA!ITl ... -1.ronnatiool,DE-J.;"E!:.~~~~ ltlo olooooodfortlMto_,_,_,..,.1,o ~l!~fj .. .,.,u .. for OM by JU..NJ', ... lo~.::~:-:.s=i~ ~,~ ;r~~~~:;~ 1 =~1?2~1 ~1~:E ::-.:===~: .. ;:= .,.__.,._,..,._r

~ .. ... ---Si-lf'ltU.. H 1ol,orT_iaol_ ""Nf,orU., f .... tloaof_-..l,oo bonanlod ,ltl 1, _,_.,.,..,.. 1 r., u-,t<.i.. nu ho6o""' .,.1 ... u.;,,-r,:1,_ ......... 111 _,,u.-..t_,-..11oe1,.,o,1;.,ri1~,1,1o.._ ,,.._, .... ,...r.,_,.....,,ri11,1...,1,o..,. ,-,rrd>r.1Mn1olol&loftonhooNfo,tl>t p-atllofth<,rioMlo .,.,or.., 1 ;.1"""''" m e, U o inth


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n. ...... ,.,..,,..__lbfo..i-4...,.....oru.. a-f:~E ::=:: .. .. ~ -~~,.: _.,_ .. _, .. _, .. ;,,_ wltl, .......... j n.._,...,.....,. ..... _.,._.,,__..,.,1,e.,....,,_ano1.i1p,. ::~':'i..:~~,";::'..!::1."'"u.!":: ~f.!~~i::~~~=-:~ :: The,..,... Ol)llon. ro, 1 ... ,..,1. 1 .-ith th :~Bg_~;;~;;.:;;~~;:; ....... ..-o,1 ..... n.a,....... .,;q......,,t, .. ::..--:-1:::.:-=~==-= lnL\"ol ____ .,,..,.., ___ .. ___ -p,o1atwui.u.o..-..Eao< ---!lllnthel0Uoin1 =~~~: ~= .... ~~~-7.':: ..:::; 1. 11 ,,.1nvo1t .. thodi,plaJ-oflnr..,...,1o,, r.~~::~toh:::.:::::h = .. .-;.-, 111o~Tloleltl!Mtbo4 .. Widol:r-u ::....-::1::' .=::..=!'!~~uo...:_:-;; ,..,_IMl4-bo-ted1Mn.l,u .. .. 1o11n.1... ... ...... -. ::-...::~ =..!::..'."r:= ~=,.,: ..,,_,omultlplof ..... ,..r.-1_,,.,1,u....,.. .. ,.n..rff

1 ...,.n.1o1.-1oaH ... t<11iou;.!,.,.t,,. = ::~.=.~==~ :.: -and.....-htoll,adlotlllu.iollofo, :!,.':;" ..=m-w:.:.~.::.:: .:!" :i:i':. :,,t'~:"i!".':i.!.n!t,:O =~ !a0l ..... ~'t;!""":,~ .. ,,,....~-... [+lbj l e tt e r s


@bI l aboratory RECYCLE WITH HEATING A .l'OO NO ANDG.MASOS 1-..._ v.;,,..., r ~....,, 1-.... ,.,.,. ...... ,""""""" s ~::.:.-:::..=--.:..-=..-:: ................ ,.. ,._Ji~hfo .,...,_ ...................... ...,. ... ~~~! -1; ;~,::L~:~~= ;:~: ~~ ~r~~~h:::;: :-:;...~~t'!'.! -...1 ._ .. tht -...-holo,_.po,._ oo-rotuoptrmJ,.bolho .. londonol)Orl....,!olooorociationofl,.. ..,.,.ti.,.or,,,.,,p1o,,..,,.1o.,,,,,. Mo ...,,..,. ; n ... ,ttt.opo1n,pdrl-tho....,,.lootup .. llin


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[il!iili classroom ESTI MA TI ON O F FLUID PROPERTIES AN D PHASE EQU ILI BRIA N HE ltSKO\\' I Tl. "-"t _,.....,.._ F o, tllio ,.,_ ,_,,. .,._........,. .. ,lloblololopi

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l'iffiJi laboratory AN INNOVATIVE CHE PROCESS LABOR ATORY SKll'R0CHEFORT,STANU;YMJDIJU:XA1< ANDl'AOC.CIIAU r:;:t1i2~""';._.-; .. Di;,,. T ,,'"tlybffnint::;.;., .:,hen.,."""'"tof AppliI M0s .. ,1noorinf matl1 e, ... tka.Pk&leookbook _i,,.f(lrtn.OUOO ... ,-.i.nt in """YOrtm<'l'ltl.llurlng :h~~~\';.":.~~h:.~:.~1'.::::~!.h,-:.:;:~: t ,,,.,. 0 ha1-.,,>,), Jroop ioado,,nd rroopmombe,.,and tolhon in t~g. 1. S-h ln<.i oa oononBlan>oltation but ooly intctu,..roandfield ]~EiinE*-: ofth e l o bo,ato,y,\l>,yar,e""""~toool> hatthqh"eloamedinoompute,..i"riod Thnoxt'iu, &N1a pn


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@jiU>lcl ass room FUNDAMENTALS OF CHEMICAL PROCESSES WU Uo\.MII .M 08 t:II w .. ~11tt1n,;,, 1 ..,,,,.., u .....,.,,,. ,.M A I __ .., ___ .. .. ------..... __ __ .., ......... .. .. ., ___ ._, _____ ... _____ ., ___ _____ ._ ......... ___ .., _______ --.. -.......,"'"7wlllbo.W.W-.""""' =....t_,,_,_ _.,.....,_....-p,._


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UTTU TO TH E EDITOR ~-A,..11..,.l--lolO-fJIM i,apolloriolM.._,H,,._lo--ri. ,_. ,.. .. p '""' '-""'" '"" ..,..., lll'Nfflllm<~:..:..Ol~':f t ~ing ...__,...ocldot Int odit .... l~Iiiii


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