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CBE 320 Syllabi
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CBE 320 Introductory Transport PhenomenaFall 2007
Instructor Prof. John Yin ([email protected])
Office Hours Mondays, 1:00-2:00pm or by appointment 3633 Engineering Hall
Teaching Assistants Pratik Pranay ([email protected]) 3009 Engr. Hall, tel. (2-3378)
Sunil Sunkara ([email protected]) 4710 Engr. Hall, tel. (5-3786)
Office hours: to be determined
Lectures MWF 8:50-9:40 am 3024 Eng Hall
Discussion Sessions M 2:25-4:20 pm 2239 Eng Hall
Tu 2:25-4:20 pm 2321 Eng Hall
Text Transport Phenomena, 2nd Edition
R.B. Bird, W.E. Stewart & E.N. Lightfoot (“BSL”)
John Wiley & Sons, 2007 (GET THE 2007 VERSION)
Course homepage http://ecow.engr.wisc.edu/cgi-bin/get/che/320/1yin/
Homework Due every Friday in class at 8:50 am. Since solutions will be available at
that time, late homework will receive a grade of zero (0). Use only one-
side of each page. You are encouraged to use the backsides of previously
printed paper.
Homework may be discussed with anyone but it may not be copied. You
may be called on to explain your work. Since homework receives a
substantial amount of credit, your solutions must basically represent your
own work. At the same time the homework provides the single most
effective means by which you can develop an understanding of the course
material. To the extent that this objective is helped by discussions with
your classmates, you should feel free to talk with them, the teaching
assistants or Professor Yin. However, before you do so, you should have
put in a significant effort on you own.
Grading Term exams (3) 45 or 35% *
Final exam 35 or 45% *
Homework (drop lowest) 20%
Class participation 1% (discretion of the instructor)
* Apply the point distribution that gives the higher total score. Term exams will be held during
special evening sessions on the dates below. There will be no late homeworks accepted, and no
exam make-ups except under extraordinary circumstances.
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Exam dates: Oct 2 (Tues, 5-7pm)
Nov 6 (Tues, 7:15-9:15pm)
Dec 4 (Tues, 5-7pm)
Final exam: Monday, Dec 17, 12:25-2:25 pm
If you have any disability that may affect your performance in this course, inform the instructor
during the first week of classes.
Fall Schedule. We will focus on basic sections of chapters (no “•” or “°” sections indicated in
the Table of Contents of BSL). Exceptions will be noted in class, during problem sessions, and
on homework assignments.
Week of TOPIC
MOMENTUM TRANSPORT
SEPT 3 Ch. 0, 1 Introduction,
10 Ch. 1 Viscosity and momentum transport
17 Ch. 2 Laminar flow
24 Ch. 3 Equations of change for isothermal systems
OCT 1 Ch. 5 Turbulent flow
8 Ch. 6 Interphase transport
15 Ch. 7 Macroscopic balances for isothermal systems
ENERGY TRANSPORT
OCT 22 Ch. 9 Thermal conductivity and energy transport
29 Ch. 10 Shell energy balances
NOV 5 Ch. 11 Equations of change for non-isothermal systems
12 Ch. 12 Temperature distributions (space and time)
19 Ch. 14 Interphase energy transport
26 Ch. 15 Macroscopic energy balances
MASS TRANSPORT
DEC 3 Ch. 17 Diffusivity and mass transport
10 Ch. 18 Concentration distributions & transport analogies, review
FINAL EXAMINATION Monday, Dec 17, 12:25-2:25 pm location to be announced
CBE 320 Transport Phenomena
Course Overview
Fall 2007
I. BASICS OF MOLECULAR TRANSPORT
Momentum: Newton’s law, viscosity
Energy as heat: Fourier’s law of conduction, thermal conductivity
Mass: Fick’s law, diffusivity
Q: Similarities? Flux dependence on gradients. Formulations in , , D
Q: Differences? Momentum tensor, density-driven or diffusion-driven convection
Q: Dependence of properties on T, P? (Increase or decrease)
II. CONSERVATION: THE EQUATIONS OF CHANGE
Continuity (mass, species A)
rate of mass accumulation = rate of mass IN rate of mass OUT
rate of A accumul = rate of A IN (diffusion, convection) rate of A OUT + rate of A prodn
Motion (momentum)
rate of mom. accumul = rate of mom. in rate of mom. out + forces on system
Energy
rate of accumul (internal & K.E.) = rate in by convection & conduction rate out by
convection & conduction rate of work done by system
Q: Origin of equations?
Velocity, temperature, or composition dependence on position or time?
Shell balances (geometry, orientation of gradients)
Get derivatives as limit (shell vol) 0
Shell balances become Dif. Eqs. (PDEs or ODEs)
Q: Solution of equations?
Need info at system boundaries (or starting time)
Use solutions to calculate fluxes, average properties
III. INTERPHASE TRANSPORT
Setting the stage: Dimensional analysis of Equations of Change
Q: Scale-up? Dynamic similarity between different scales: match dimless groups
Momentum: friction factor vs Re
Heat: Nusselt number (dimless h.t.c.) vs Re, Colburn analogy (momentum heat)
Mass: Sherwood number (Nusselt for m.t.), Chilton-Colburn analogy (heat mass)
Reynolds analogy (momentum heat mass) for gases
Empirical correlations exist for variety of heat/mass transfer geometries/flow regimes
IV.MACROSCOPIC BALANCES
Macroscopic energy balance: friction losses due to fittings (sizing pumps), designing heat
exchangers, increasing process efficiencies
CBE 320 Transport Phenomena
Fall 2007
Overview of Key Topics
Chapter 1 (BSL, 2nd Ed)
1. Newton's law of viscosity
2. Generalization of Newton's law
3. Viscosity dependence on T, P
4. Convective momentum transport
Ch 2
5. Shell balances for momentum conservation and boundary conditions
6. Examples: falling film, circular tube, annulus, flow around a sphere
Ch 3
7. Derivation of continuity (mass conservation), equation of motion (momentum conservation)
8. Given Navier-Stokes Eq, postulate velocity components for different geometry/flow examples,
simplify NS equations, solve for velocity distributions.
9. Eq. of mech energy
10. Dimensional analysis
Ch4
11. Note that non-steady state problems make velocity dependent on not only position, but also time
Ch5
12. laminar/turbulent flow
13. time-smoothed eq. of change
14. turbulent mom flux
Ch 6
15. Definition of friction factor (f)
16. f for tube flow, definition, and derivation of f = f(Re)
17. f vs Re plot, circular and non-circular tubes
18. f for spheres/particles, f vs Re
Ch7
19. macroscopic momentum balance
20. macroscopic mechanical energy balance, Bernoulli Eq.
21. Derivation and application of friction losses (Ev) for tubes, fittings
Ch 9
22. heat transfer by conduction (Fourier's Law), analogy to momentum transfer
23. thermal conductivity (T, P dependence)
24. convective energy transport (combined energy flux vector)
Ch10
25. Energy Shell Balances (for conduction)
26. Newton's law of cooling
27. Viscous heating, Brinkman number
28. Composite walls
29. Forced convection heat transfer
30. Free convection heat transfer
Ch 11
31. Energy Eq
32. Special forms of energy Eq
33. Boussinesq Eq.
34. Viscous heating in an annulus, transpiration cooling
35. Dim. Analysis for nonisothermal systems
Ch 12
36. Unsteady heat conduction in solids, error function
Ch 13
37. Time-smoothed Eq. of change (Eddy thermal cond., turbulent Pr)
38. Temp distribution for turbulent flow in tubes
Ch 14
39. Heat transfer coeffs, htc (definitions) and Nusselt number
40. Analytical determination of htc.
41. Htc for forced convection in tubes/around submerged objects
42. Colburn analogy
Ch 15
43. Macroscopic energy balance
Ch 17
44. Fick's law; Pr, Sc, Le numbers
45. Combined mass/molar fluxes (molecular diffusion and convection)
Ch 18
46. Shell balances for diffusion, common boundary conditions (mass transfer coeff)
47. Diffusion through a stagnant gas film
48. Diffusion with chemical reaction
Ch 19
49. Eq of Continuity for a binary
Ch 20 (homework)
50. Analogy to Ch 4 and 12
51. Penetration depth for momentum, heat, mass transfer
Ch 22 (class notes)
52. Common dimless groups
53. correlations of mass transfer coeffs
54. Transport analogies (Reynolds, Colburn, Chilton-Colburn)
55. Psychrometry
CBE 320 Transport Phenomena
Fall 2006 D. J. Klingenberg
Syllabus
Note: Letters designate two-hour problem sessions (Monday or Tuesday); numbers designate one-hour lectures(Monday-Wednesday-Friday).
Pd Date Ch Topic Reading Assignment
01 09/06 00 Introduction Ch. 0, Calc. text, App. A, C02 09/08 01 Viscosity 1.1–1.3, 1.7
03 09/11 02 Shell balances: falling film 2.1, 2.2A 09/11-12 02 Shell momentum balances04 09/13 02 Flow in a tube, annulus 2.3, 2.405 09/15 02 Flow around a sphere 2.6
06 09/18 03 Equation of continuity 3.1B 09/18-19 03 Shell momentum balances07 09/20 03 Equation of motion 3.2, 3.508 09/22 03 Solution of flow problems 3.6
09 09/25 03 Dimensional analysis 3.7C 09/25-26 03 Equations of change10 09/27 05 Turbulent momentum transport 5.1, 5.211 09/29 – FIRST EXAMINATION Math. rev., Chs. 1, 2
12 10/02 06 Friction factors (tubes) 6.1, 6.2D 10/02-03 06 Friction factors13 10/04 06 Friction factors (spheres) 6.314 10/06 07 Macroscopic balances 7.1–7.4
15 10/09 07 Friction loss factors 7.5E 10/09-10 07 Macroscopic balances16 10/11 07 Solution of flow problems 7.617 10/12 08 Polymeric Liquids 8.1–8.3
18 10/16 09 Thermal conduction and convection 9.1, 9.2, 9.7, 9.8F 10/16-17 10 Shell energy balances19 10/18 10 Conduction with heat sources 10.1, 10.2, 10.420 10/20 10 Composite walls and fins 10.6, 10.7
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Pd Date Ch Topic Reading Assignment
21 10/23 10 Forced convection heat transfer 10.8G 10/23-24 10 Shell energy balances22 10/25 – SECOND EXAMINATION Chs. 3, 6, 7, 823 10/27 10 Free convection heat transfer 10.9
24 10/30 11 Equations of energy and motion 11.1–11.3H 10/30-31 11 Equations of change25 11/01 11 Solutions of heat flow problems 11.426 11/03 11 Dimensional analysis 11.5
27 11/06 14 Heat transfer coefficients 14.1I 11/06-07 14 Heat transfer coefficients28 11/08 14 Heat transfer in tube flow 14.2, 14.329 11/10 14 Heat transfer around objects 14.4
30 11/13 15 Macroscopic balances 15.1–15.2J 11/13-14 15 Macroscopic balances31 11/15 15 Solution to heat transfer problems 15.332 11/17 15 Solution to heat transfer problems 15.4
33 11/20 16 Energy transport by radiation 16.1–16.3K 11/20-21 – THIRD EXAMINATION Chs. 9, 10, 11, 1434 11/22 17 Mass diffusion and convection 17.1, 17.2, 17.7, 17.835 11/24 18 THANKSGIVING RECESS
36 11/27 18 Diffusion through a gas film 18.1, 18.2L 11/27-28 18 Mass balances37 11/29 18 Diffusion with reactions 18.3–18.6- 12/01 18 Diffusion into a catalyst 18.7
38 12/04 19 Diffusion equations 19.1–19.3M 12/04-05 19 Equations of change39 12/06 19 Solutions to mass X-fer problems 19.4, 19.540 12/08 19 Solutions to mass X-fer problems 19.4, 19.5
41 12/11 22 Mass transfer coefficients 22.1–22.3N 12/11-12 22 Mass transfer coefficients42 12/13 23 Macroscopic balances 23.1–23.443 12/15 Review
FINAL EXAMINATION Tuesday, 12/19/02, 5:05 pm ROOM T.B.A.
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Teaching Assistants
Name Room Phone email Office hoursSean Cullen (301) 1137 ERB 262-6799 [email protected] 11:00 am–12:00 pm M,
1:00-2:00 pm FJoe Bernacki (302) 3713 Engr. Hall 262-1090 [email protected] 12:00–1:00 pm T,
11:00 am–12:00 pm F
TA office hours will be held in the grad student lounge (3036 Engr. Hall).
Instructor
Dan Klingenberg 3006 Engr. Hall 262-8932 [email protected] 4:00-5:00 pm F
Textbook
Transport Phenomena, 2nd edition, by Bird, Stewart, and Lightfoot, Wiley, New York (2002).
Web Page
Some information concerning the course will be posted at
http://homepages.cae.wisc.edu/˜klingen/che320/che320.html.
Examinations, Homework, and Grading
There will be three examinations during the semester and one final comprehensive examination. Each (semester)exam score will be normalized by dividing it by the class average. Your lowest normalized score will be dropped andreplaced by your next highest normalized exam score. For example, if your exam scores are 90, 67, 82, and the classaverages on these exams were 70, 60, 90, your normalized exam scores will be 1.29, 1.12, 0.91. After replacing yourlowest normalized score with the next highest, your normalized scores for the three exams become 1.29, 1.12, 1.12.For final grades, each of these normalized scores will be multiplied by the average score of all three exams. Withthis system,there will be no make-up examinations, except for under extremely extraordinary circumstances.
There will be three lectures per week (MWF) and one “problem session” (M (301) or T (302)). During theproblem session, you will be given an assignment in two parts: Part A is designed to be worked during the problemsession, and Part B (which may be begun during the problem session) is to be completed afterward. Part A willbe handed in at the end of the problem session, and part B will be handed in at the beginning of the next problemsession.
Late homework will not be accepted for credit, except under extraordinary circumstances. Teaching assistantsare under no obligation to grade sloppy or illegible homework. Your homework should be presented in a consistentformat, one side per page, with each problem begun on a new page. You should include the following information onthe top of the first page: Name, date, course, homework number, problem session number and name of your teachingassistant.
Course grades will be determined by the following distributions:
Participation (Disc.) 5%Homework 15%Examinations (20% each) 60%Final Examination 20%
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CBE 326 Syllabi
CBE 326 - Momentum and Heat Transfer Operations
Fall Semester 2006
Description 326 Momentum and Heat Transfer Operations. Analysis of chemical engineering operations involving fluid flow and heat transfer. Flow of fluids through ducts and porous media; motion of particulate matter in fluids; general design and operation of fluid-flow equipment. Conductive, convective and radiative heat exchange with and without phase change; general design and operation of heat-exchange equipment.
Instructor:Nicholas L. Abbott Email: [email protected]
Teaching Assistant Brian Gettelfinger Email: [email protected]
Course Prerequisite(s)
ChE 211ChE 320with grades of C or better
Prerequisite knowledge and/or skills
Chemical Process Thermodynamics Transport Phenomena
Textbook(s) and/or other required material
McCabe, Smith, and Harriott, Unit Operations of Chemical Engineering, Sixth Edition, McGraw-Hill..
Bird, Stewart, and Lightfoot, Transport Phenomena, Wiley.
Course objectives
Ability to apply thermodynamics and transport phenomena to analyze and design chemical process equipment.
Familiarity with the theory and design equations describing common chemical engineering process equipment.
Topics covered
Dimensional Analysis and Scale-Up Mechanical Energy Balances Flow of Incompressible Newtonian and Non-Newtonian Fluids Flow of Compressible Fluids Flow Measurement
Pumps, Compressors, Fans and Blowers Two Phase FlowDrag Coefficients and Settling Packed Beds, Fluidized Beds, and Filtration Cyclones and CentrifugesAgitation and Mixing Conduction in SolidsHeat Transfer Coefficients Forced and Free Convection Boiling and Condensation Heat Exchangers EvaporatorsRadiation
Lecture/Discussion schedule
3 50-minute lectures, 11:00 MWF, EH 3032 50-minute discussion session, 2:25 W in EH3032
Office Hours
Monday, 1.00-2:30pm, EH ????, Brian Gettelfinger Wednesday, 3:30pm-4:30pm, EH 3016, Nicholas Abbott Thursday, 1.00pm-2:30pm, EH ????, Brian Gettelfinger
Assessment
Homework (15%) due at the start of class each Friday. Four quizzes to be held in class (15% for each quiz) Final exam (25%)
Quiz #1: Friday, September 29, in class Quiz #2: Monday, October 23, in class Quiz #3: Monday, November 13, in class Quiz #4 Monday December 4, in class Final Exam, Tuesday, December 19, 12:25pm (check scheduler for location)
Momentum and Heat Transfer Operations
W.L. McCabe, J.C. Smith, and P. Harriott. Unit Operations of Chemical Engineering.7th Ed. McGraw-Hill, New York, 2005.
R.B. Bird, W.E. Stewart and E.N. Lightfoot. Transport Phenomena,2nd Ed. John Wiley& Sons, 2002.R.H. Perry and D. Green (Eds.) Perry's Chemical Engineers' Handbook.
“326” Subject Matter: [ 1-14-07 RES ]
Engineering of macroscopic systems
1. Components as geometries + phenomenologies (“patterns”), not unit operations
2. Integration over macroscopic regions/geometries
– Integration along streamlines
– 2D, 3D field solutions and basic geometries
- Symmetries of governing equations and BCs
- Dimensionless solutions
– Use of simple (high symmetry) solutions to approximately solve real situations
- Streamline bundles
- Approximate geometries
- Property averaging
– Numerical solution - CFD
3. Combinations of components
– Common configurations
– Networks of components
4. Frequently-encountered configurations (equipment) and systems
Phenomenology
1. Physics of fluid flow at higher Reynold’s number
– Qualitative fluid dynamics: boundary layers, flow separation, vortices, etc.
– Rudimentary potential theory: streamline analysis, vortex system analysis andHelmholtz theorems
– Foils and surfaces
– Boundary layer analysis
2. Non-Newtonian flows (simple models, suspensions)
3. Compressible flow
– Sonic velocities, shock waves, Mach number criteria, choking flow
4. Multiphase flows
– Fluid-“particle”
- packed beds, fluidized beds, pneumatic/hydraulic transport
- droplets, sprays, atomization
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- bubbles, aeration
– Fluid-fluid flow
- in conduits
- gravity, surface waves
– Mixing and dispersion
5. Heat transfer with phase change
– Boiling and vaporization
- flux/gradient relations
- natural and forced convection
- choking flow
– Condensation
- transfer coefficients, Colburn-Hougen relation (coupled heat and masstransfer, multicomponent)
- natural and forced convection
6. Radiant heat transfer
– Surfaces: emissivities, absorptivities, gray bodies and temperature dependence
– Exchange with gases
Application topics
1. Flow networks
2. Dynamic compressors, fans, and turbines
– description of geometries and flow patterns, operating behaviors
– polytropic analysis, compressor characteristics, dimensionless groups andrelations
3. Positive displacement machines: losses and heat transfer
4. Separators: filtration, cyclones, electrostatic precipitators, centrifuges, settlers,disengagement
5. Heat exchange configurations
– Analysis: overall balances, pinches, MTD’s, effectiveness and transfer units
– Contacting patterns: countercurrent, cocurrent, crossflow, multipass; periodicflow regenerators
6. Radiant transfer interchange networks
7. Design of equipment. Determining geometry, integrating phenomenologies.
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DEPARTMENT OF CHEMICAL & BIOLOGICAL ENGINEERINGUNIVERSITY OF WISCONSIN
CBE 326: MOMENTUM- AND HEAT-TRANSFER OPERATIONS Fall, 2007
R.E. Swaney, 2008 Engineering (262-3641), [email protected]
Exam Schedule
Exam Date
1 Tues 10–2 (7:15pm)2 Tues 10–30 (7:15pm)3 Tues 11–27 (7:15pm)Final Fri 12–21 (2:45pm)
Grading
Midterm Exams (3 x 20%) 60%Final Exam 20%Design Assignment 10%Weekly Homework 10%
100%
Course Policies
• Exams will be open-book, open-notes.
• Since homework is allocated a portion of the course grade, homework assignments areto be original, individual work. Any use of existing solutions prior to submitting home-work for grading is prohibited and considered unethical. This includes any solutionsprepared by the instructor or previous TAs, or solutions worked out by students whotook the course in a prior semester, regardless of how they might be obtained. Discus-sion among fellow students is acceptable as long as the discussion does not extend togiving answers and/or copying solutions.
The major way you will develop skill at engineering problem solving is by doing thehomework problems. Short-circuiting this process is self-defeating, no matter how busya given week might be. Both the instructor and the TA are eager to provide assistancewhen needed.
• Homework will be due on Friday at the beginning of the discussion period, and solutionswill be posted on Mondays, unless stated otherwise. Homework will not be acceptedlate except by specific agreement of the TA.
• Students with legitimate reasons to reschedule an exam or turn in an assignment lateare asked to inform the instructor in advance so that alternate arrangements can bemade.
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Texts:
1. McCabe, Smith, and Harriott, “Unit Operations of Chemical Engineering”, McGraw-Hill, 7th ed. (2005).
2. Bird, Stewart, and Lightfoot, “Transport Phenomena”, 2nd ed., Wiley (2002).
Recommended References:
1. Perry et al. (Eds.), “Chemical Engineer’s Handbook”, 7th Edition, McGraw-Hill(1997).
2. Levenspiel, O., “Engineering Flow and Heat Exchange”, Rev. ed., Plenum (1998).
3. Holman, J.P., “Heat Transfer”, 9th ed. (or most recent), McGraw-Hill (2002).
4. Johnson, R.W. (Ed.), “The Handbook of Fluid Dynamics”, CRC Press (1998).
5. Schetz, J.A and A.E. Fuhs (Eds.), “Handbook of Fluid Dynamics and Fluid Machin-ery”, Wiley (1996).
6. Hewitt, G.F. “Heat Exchanger Design Handbook”, Hemisphere (1990). (Wendt Li-brary reference section.)
7. Hottel, H.C. and A.F. Sarofim, “Radiative Transfer”, McGraw-Hill (1967).
8. Kuppan, T., “Heat Exchanger Design Handbook”, Marcel Dekker (2000).
9. Kays, W.M. and A.L. London, “Compact Heat Exchangers”, 3rd Edition, McGraw-Hill(1984).
10. Siegel, R. and J.R. Howell, “Thermal Radiation Heat Transfer”, 3rd Edition, Hemi-sphere (1992).
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Course Schedule
Date Topic Reading
W 9-5 Course introduction; review of macroscopic,microscopic mass/momentum/energy balances
MSH-1; BSL-2,3,10,11
F 9-7 Macroscopic mechanical energy balance –Bernoulli equation
MSH-2,4; BSL-7
M 9-10 Qualitative fluid mechanics: turbulence,boundary layers, vortices, “skin” friction and“form” drag
MSH-3; P6–4-5
W 9-12 Flow in conduits; valves and fittings; flowsystems and networks
MSH-5; BSL-5,6,7;P6–9-13,16-22
F 9-14 ” P10–67-102
M 9-17 ”W 9-19 Compressible flow: isothermal, adiabatic, critical
flow, shock wavesMSH-6; BSL-7,11
F 9-21 ”
M 9-24 Metering MSH-8; P10–6-20
W 9-26 ”F 9-28 Pumps and compressors MSH-8; P10–20-37,45-56
M 10-1 ”W 10-3 Compressors
F 10-5 ”
M 10-8 Packed beds/porous media; tube banks MSH-7; BSL-6; P6–36-40
W 10-10 Particles; Filtration MSH-29; P6–50-54;MSH-7; BSL-6;P17–39-51, P18–74-105
F 10-12 Fluidized beds MSH-7; P17–2-19
M 10-15 Cyclones, impingement, electrostaticprecipitators
MSH-29; P17–22-39,51-59
W 10-17 Two-phase flow P6–26-29
F 10-19 Mixing MSH-9; P6–34-35,P18–5-22
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Course Schedule (cont.)
Date Topic Reading
M 10-22 Thermal conduction in solids MSH-10; BSL-9,10
W 10-24 Unsteady-state conduction in solids MSH-10; BSL-12;P5–10-11
F 10-26 ”
M 10-29 Resistances, series and parallel; heat transfercoefficients, individual and overall
MSH-10,11; P5–9-10,12
W 10-31 Extended surfaces MSH-15; BSL-10;P11–22-23,47-51
F 11-2 Macroscopic energy balance MSH-11; BSL-15
M 11-5 Mean temperature difference and transfer units MSH-11
W 11-7 T-Q diagrams, operating lines, effectiveness MSH-11
F 11-9 Exchangers in series, parallel, and networks;nonlinear enthalpy lines
M 11-12 Thermal contacting patterns, cross-current andmultipass; MTD and pinches
MSH-15; P11-4-6
W 11-14 ”F 11-16 Periodic unsteady-state contacting, regenerators MSH-15; P27–52-54
M 11-19 Heat transfer coefficients in forced and naturalconvection; dimensionless groups; the analogy
MSH-12; BSL-14;P5–12-19, P11–25-27
W 11-21 ”F 11-23 (Thanksgiving Recess)
M 11-26 Condensation MSH-13,15; BSL-14;P5–20-22
W 11-28 ”F 11-30 Boiling MSH-13,15; P5–22-23,
P11–13-17
M 12-3 Shell-and-tube exchangers MSH-15; P11–7-10,33-45
W 12-5 Radiation heat transfer MSH-14; BSL-16;P5–23-27, P11–31-32
F 12-7 Assemblies and interchange factors MSH-14; P5–27-32
M 12-10 Radiant transfer with gases P5-32-40
W 12-12 Furnaces P5–40-42F 12-14 Summary topics
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CBE 324 Syllabi
Department of Chemical and Biological Engineering
University of Wisconsin-Madison
Transport Phenomena Laboratory (CBE 324)Calendar - Spring 2007
Week of Topic/Experiment Assignment
1 January 22 Introduction/Logistics ---
2 29 Data Analysis/Statistics/Safety Data analysis
3 February 5 Velocity Profiles for Turbulent Flow (Expt.B.1) Report
4 12 Thermal Conductivity of Solids (Expt. A.2) Memo
5 19 Rewrite week/Report Writing/Lab practice Rewrite
6 26 Rewrite week/Report Writing/Lab practice Rewrite
7 March 5 Temperature Profiles in Solids (Expt. B.2) Report
8 12 Concentration Profiles in a Stagnant Film (Expt. B.3) Memo
9 19 Friction Factors for Flow in Circular Tubes (Expt. C.1) Report
10 26 Efflux Time for a Tank with Exit Pipe (Expt. D.2) Memo
11 April 2 Spring Recess
12 9 Heat-transfer Coefficients in Circular Tubes (Expt. C.2) Group Memo
13 16 Design of Experiments
14 23 Heating Liquids in Tank Storage (Expt. D.3) Group Report
15 30 Oral Presentations
16 May 7 Oral Presentations (if necessary).
Textbooks: Crosby, E. J.,Experiments in Transport Phenomena, Department of ChemicalEngineering, University of Wisconsin, Madison, Wisconsin. Revised by T.W.Chapman and CBE 324 staff, available at Bob’s Copy Shop.
Bird, R.B., W.S Stewart, E.W. Lightfoot,Transport Phenomena, 2nd. Edition, JohnWiley, N.Y. (2002)
Pfeiffer, W.S.,Pocket guide to technical writing, 4th Edition, Pearson Prentice Hall,Upper Saddle River, N.J. (2007)
Instructors/Teaching AssistantsName Section Office Phone Email
Prof. Nick Abbott (T) 3016 EH [email protected]. Rafael Chavez (W) 1006 EHDr. Eric Codner (R) B103FMr Sunil Sunkara (T/W) 4725 EHMr Jinlong Zhang (W/R) 4650 EH
Department of Chemical and Biological Engineering
University of Wisconsin-Madison
Transport Phenomena Laboratory
Textbooks: - Crosby, E. J.,Experiments in Transport Phenomena, Department of ChemicalEngineering, University of Wisconsin, Madison, Wisconsin (1961). Revised byCBE 324 staff, available at Bob’s Copy Shop.
- Bird, R.B., W.S Stewart, E.W. Lightfoot,Transport Phenomena, 2nd. Edition, JohnWiley, N.Y. (2002)
- Pfeiffer, W.S.,Pocket guide to technical writing, 3rd Edition, Pearson PrenticeHall, Upper Saddle River, N.J. (2004)
Instructors and Supervisor
Name Section Office Phone EmailDr. Rafael Chavez 1006 EH 3-1979Dr. Eric Codner Th B103F EH 3-3130I-Hsin Lin T 2112 EH 2-2999 [email protected]
Chem 563 Syllabus
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Daniel J. Klingenberg
From: Mark Ediger [[email protected]]Sent: Thursday, January 10, 2008 4:28 PMTo: Daniel J. KlingenbergCc: Edwin TurnerSubject: Re: 563 syllabus
Hi Dan,I don't think we actually have a syllabus. But I can give you the rough idea. One
credit students do 5 labs:
Viscosity of a polymer solutions. They use an Ubbelohde viscometer and determine intrinsic viscosity.
Conductance of aqueous solutions of strong electrolytes. They determine specific and equilivalent conductances using a capacitance bridge and the absolute mobilities using themoving boundary method.
Thermodynamics of Electrochemical Cells. They measure E vs. T, determine delta G, delta H, and delta S.
Kinetics of the reduction of toluidine blue by sulfite. They measure absorbance vs. time to get reaction kinetics and investigate the kinetic salt effect.
Heat of reaction. They determine delta H and delta H^o for an acid base reaction.
Two credit students do some additional labs but hardly any students take the course for two credits. We can tell you about these labs also if you want.
Ed, do you want to add anything?
Mark
On Jan 10, 2008, at 3:58 PM, Daniel J. Klingenberg wrote:
> Mark:>> Can you send me a syllabus that you have used recently for Chem 563 > (or a URL or whatever would tell us what sorts of lab exercises the > students work on)? We are trying to improve our transport lab > (perhaps going beyond transport), but do not want to overlap too much > with what is being done in Chem 563.>> Thanks,> Dan>
