| Lect. | Date | Description | Pertinent are... | ||
|---|---|---|---|---|---|
| Text | Notes | Hmwk | |||
| L01 | 8/25 Tue |
Introduction to course. Introduction to textbook. Introduction to gas absorption.
Rigorous calculation allowing for evaporation of liquid.
Simplified calculation neglecting evaporation of liquid ("the usual approximations"). |
MSH pp. 521-525 |
■ Lecture 01 (pdf) ■ Single-stage absorption (pdf) |
#01 (pdf) |
| L02 | 8/27 Thur |
Improving a gas absorption operating by adding stages; why countercurrent contact is best. Operating line, equilibrium curve,
McCabe-Thiele diagram, counting of stages. |
MSH pp. 643-653 |
■ Lecture 02 (pdf) |
#01 (pdf) |
| L03 | 9/01 Tue |
Absorption factor method (Kremser equation).
Absorption operations, including minimum liquid flow rate. Stripping operations, including minimum gas flow rate. |
MSH pp. 653-660 |
■ Lecture 03 (pdf) | #02 (pdf) |
| L04 | 9/03 Thur |
Saturated vapor pressure and relative volatility. Binary vapor-liquid equilibria and phase diagrams. | MSH pp. 663-666, 737-742 |
■ Lecture 04 (pdf) |
#02 (pdf) |
| L05 | 9/08 Tue |
Graphical method for binary flash distillation. Analytical method for binary and multicomponent
flash distillation. Why a column improves product purities relative to flash distillation. Column mass balances.
Percent recovery. |
MSH pp. 666-681 |
■ Lecture 05 (pdf) |
#03 (pdf) |
| L06 | 9/10 Thur |
McCabe-Thiele diagram: rectifying section operating line, feed line, stripping section operating line, counting of stages, feed stage location. |
MSH pp. 681-694 |
■ Lecture 06 (pdf) ■ Binary distillation McCabe Thiele 1925 ■ Binary distillation Murphree 1925 |
#03 (pdf) |
| L07 | 9/15 Tue |
Partial versus total condensers. Minimum number of stages, Fenske equation. Minimum and optimum reflux ratio. Use of overall and Murphree tray efficiency. ■ Effective Equilibrium Excel Calculation |
MSH pp. 674-675, 687-691,712-722 |
■ Lecture 07 (pdf) |
#04 (pdf) |
| L08 | 9/17 Thur |
Nearly pure products: use of the Kremser equation for distillation. Enthalpy balance calculations:
liquid and vapor mixture enthalpies. |
MSH pp. 694-701 |
■ Lecture 08 (pdf) |
#04 (pdf) |
| L09 | 9/22 Tue |
Enthalpy balance calculations: Condenser and reboiler duties.
Design of columns: vapor pressure drop, downcomer level and tray spacing; flooding velocity and column diameter.
|
MSH pp. 701-712, 718-724 |
■ Lecture 09 (pdf) |
#05 (pdf) |
| L10 | 9/24 Thur |
UNIFAC Calculating non-ideal VLE |
MSH pp. 724-727 |
■ Lecture 10 (pdf) ■ UNIFAC |
#05 (pdf) |
| L11 | 09/29 Tue |
Introduction to multicomponent distillation: light and heavy keys, splits, non-distributed and distributed
components, column sequencing. Short-cut methods: Fenske equation for minimum number of stages,
Underwood's method for minimum reflux ratio, Gilliland correlation for number of ideal stages
at operating reflux ratio. |
MSH pp. 742-752, 757-759 DM pp. 144-145, 290-291 |
■ Lecture 11 (pdf) ■ L11 Example Problems (pdf) |
#06 (pdf) |
| L12 | 10/01 Thur |
Degrees of Freedom in a distillation process.
Tray-to-tray calculations. Design versus performance models. Batch Distillation |
MSH pp. 752-756 DM pp. 115-124, 144-145, 147 |
■ Lecture 12 (pdf) |
#06 (pdf) |
| L13 | 10/06 Tue |
Definition of leaching, everyday example (making tea), theory for countercurrent contact. Problem-solving procedure, solved example problem. |
MSH pp. 764-772 |
■ Lecture 13 (pdf) ■ Leaching example |
#07 (pdf) |
| Exam 1 | 10/08 Thur |
Covers Lectures 1-10, Homework 1-5 |
|||
| 10/13 Tue |
FALL BREAK | ||||
| L14 | 10/15 Thur |
Introduction to liquid extraction: basic process and uses,
liquid-liquid equilibria, ternary phase diagrams, mass balances for a mixing step.
Single-stage liquid extraction. |
MSH pp. 772-783 T pp. 433-446 |
■ Lecture 14 (pdf) |
#08 (pdf) |
| L15 | 10/20 Tue |
Multistage crosscurrent extraction.
Multistage countercurrent extraction: overall mass balances. |
MSH pp. 772-783 T pp. 446-448, 450-451 |
■ Lecture 15 (pdf) ■ Lecture 15b (pdf) |
#08 (pdf) |
| L16 | 10/22 Thur |
Multistage countercurrent extraction: Hunter-Nash and
McCabe-Thiele methods for counting stages. |
MSH pp. 772-783 T pp. 450-453 |
■ Lecture 16 (pdf) ■ Lecture 16b (pdf) | #09 (pdf) |
| L17 | 10/27 Tue |
Multistage countercurrent extraction: minimum entering solvent flow rate.
Liquid extraction equipment. |
MSH pp. 783-789 T pp. 450-453 |
■ Lecture 17 (pdf) ■ Lecture 17b (pdf) |
#09 (pdf) |
| L18 | 10/29 Thur |
Introduction to mass transfer: where mass transfer is "hidden" in tray towers.
Estimation of liquid- and gas-phase diffusion coefficients. Solute flux: definition |
MSH pp. 527-540, 542-543 |
■ Lecture 18 (pdf) ■ Appendix 19 | #10 (pdf) |
| L19 | 11/03 Tue |
Solute flux through 1D slab for cases of equimolar counterdiffusion and one-component mass transfer (A diffusing through
non-diffusing B).
Film theory and mass transfer coefficients. Two Film theory introduction |
MSH pp. 547-548, 555-556 |
■ Lecture 19 (pdf) |
#10 (pdf) |
| L20 | 11/05 Thur |
Two-film theory: interfacial mole fractions yi and xi,
overall mass transfer coefficients Ky and Kx.
Correlations for mass transfer coefficients: dimensionless groups (Sherwood number Sh, Stanton number St,
Colburn j factor for mass transfer jM), correlation equations for various flow situations. Theory of Murphree tray efficiency. |
MSH pp. 576-585 |
■ Lecture 20 (pdf) |
#11 (pdf) |
| L21 | 11/10 Tue |
Introduction to gas absorption with packed towers. Four alternate expressions for per-volume rate of mass transfer,
integration of differential mass balance, height of transfer unit, number of transfer units.
Mass transfer correlations for heights of a transfer unit (HTU's) Hy and Hx (equations and example). |
MSH pp. 576-585 |
■ Lecture 21 (pdf) ■ Table 18.1 |
#11 (pdf) |
| L22 | 11/12 Thur |
Types of packing. Hydraulics of packed towers: loading and flooding, correlations for
pressure drop and flooding velocity. Determination of tower diameter based on operation
at a fraction (typically 50-60%) of the flooding velocity, or at an appropriate specified
pressure drop. |
MSH pp. 565-575 |
■ Lecture 22 (pdf) |
#12 (pdf) | L23 | 11/17 Tue |
Introduction to adsorption. Adsorption isotherms.
Fixed beds: concentration profiles, mass transfer zone, break point and break-point time,
breakthrough curve, length of unused bed. |
MSH pp. 836-851 |
■ Lecture 23 (pdf) |
That's enough... |
| Exam 2 | 11/19 Thur |
Covers Lectures 11-19, Homework 6-10 |
|||
| L24 | 11/24 Tue |
More detailed look at adsorption: fundamental mass transfer equations.
Adsorbent regeneration. Distillation Column Control |
MSH pp. 836-851 |
■ Lecture 24 (pdf) ■ Lecture 24b (pdf) |
That's enough... |
| 11/26 Thur |
THANKSGIVING BREAK | ||||
| L25 | 12/01 Tue |
Azeotropic Separations Air Separation Partial Condensers Revisited |
■ Lecture 25 (pdf) |
That's enough... | |
| L26 | 12/03 Thur |
No Class Today - Extra Office Hours in 309A Furnas Hall | That's enough... | ||
| Homework | 20% |
| 2 Midterm Exams, 20% each | 40% |
| Final Exam | 40% |
Final grades for all students will be determined by a curve.
Students must earn at least 30% of total possible weighted points to pass the course
Grades
% of Students receiving grade
A, A-
20%
B+, B, B-
30%
C+, C, C-
40%
D+, D
10%
An effort will be made to position grade lines at gaps in
the distribution of course totals.
Professionalism:
Students are expected to turn in homework that is neat,
clear and well organized. Significant point penalties will be imposed for messy, disorganized,
confusing or otherwise unclear work. Although allowances will be made for the effects of time
pressure on exams, points will also be deducted for messy, disorganized, confusing or otherwise
unclear solutions of exam problems.
Grateful thanks to Johannes M. Nitsche for use of website and other course materials