Massachusetts
Institute of Technology
Department
of Mechanical Engineering
2.55: Advanced Heat and Mass Transfer
Course
Information
Fall Term 2003
I. Credit and Content
2.55 is a 12-unit H-level subject serving as the
Mechanical Engineering department's core graduate course in heat and mass
transfer. This course is open to
students from all areas of engineering, although an undergraduate background in
heat transfer will be assumed. This
class is an appropriate preparation for the doctoral qualifying exam.
Topics to be covered include: diffusion kinetics,
conservation laws, some heat conduction, laminar and turbulent convection, mass
transfer including phase change or heterogeneous reactions, and basic thermal
radiation. Problems and examples will
include theory and applications drawn from a spectrum of engineering design and
manufacturing problems.
II. CLASSES
Lectures: Monday and Wednesday from 11.00 AM to 12:30 PM in Room 1-246
Tutorial: Wednesday from 3:00 PM to 4:00 PM in Room 1-371
Lecturer: Professor B. Mikic mikic@mit.edu 3-166 253-2242
T.A.: Fiona McClure fmcclu@mit.edu 31-159 253-5329
Office Hours: Monday
from 2:00 PM to 4:00 PM in Room 31-156
Email: Please
add yourself to the class e-mail list for various important announcements (NO
JUNK MAIL). The list is called
"2.55" and you can add yourself using mailmaint or by visiting the
website https://ca.mit.edu/moira/index.jhtml
and following the instructions there.
Textbook: Heat Transfer (2nd
Edition) by A. F. Mills (Prentice Hall, 1998). Available at The Coop.
III. EXAMS
AND GRADING
The course grade will be based on two midterm exams (25%
each) and a final exam (50%). The tests
will be open book unless otherwise announced.
The exam dates are as follows:
Quiz
1: Wednesday, October 8
Quiz
2: Wednesday, November 17
Final
Exam: December 15-19 final exam period,
time and place TBA.
Homework Problems:
A set of ten
homework problems will be assigned during the course. In addition, three
sets of review questions will be handed out before the exams. You should work all
these problems carefully as they are an essential aid to learning the
material. Some of these problems will
be worked in the tutorials and attempting the problems before the tutorial is
strongly recommended.
IV. PREREQUISITES
Students entering this course should have had
undergraduate classes in heat transfer, thermodynamics, and fluid mechanics
corresponding to 2.51, 2.40, and 2.20.
A graduate level background in mathematics will be assumed. Some specific areas you should have seen
previously include:
Mathematics: Vector calculus, first and second-order ODEs, linear PDEs solved
via separation of variables and Fourier series.
Heat Transfer: One-dimensional steady and unsteady heat conduction, fins,
elementary laminar and turbulent convection, natural convection and
condensation, heat exchangers, simple blackbody and gray body radiation.
Fluid
Mechanics: Elementary viscous flow including Couette
flow, boundary layers and tube flows; transition Reynolds number and concepts
of turbulence; skin friction and pressure drop calculations.
Thermodynamics: Concept of an equation of
state; first law; phase transitions.
If you have gaps in a few of these areas, it
shouldn't prevent you from doing well in this class; if a large fraction of
this is new to you, consider taking 2.51.
V. Lecture Schedule
Lect.# Date Topics
Readings
1 Wed. Sep. 3 Introduction
and Mills: 5.7
Conservation
Equations Lienhard: 2.1, 7.3
White: 1.3-1.4, Ch. 2
2 Mon. Sep. 8 Conservation
Equations
3 Wed. Sep. 10 Conservation
Equations
and Gas Kinetics Vincenti &
Kruger: Ch. 1, 2
4 Mon. Sep. 15 Gas
Kinetics
5 Wed. Sep. 17 Conduction Mills: 2.4.4, 3.1-3.5
Lienhard: Chapter 5
6 Wed. Sep. 24 Conduction
(cont.)
7 Mon. Sep. 29 Laminar
Boundary Layers Mills: 4.2, 4.3.2, 5.4, 5.8.1
Lienhard: 7.1-7.5
White: 3.5, 3.8, 4.1-4.3,
4.10-4.10.1,
4.12,
7.1-7.3
K
& C: Ch. 8, 10
8 Wed. Oct. 1 Laminar
Boundary Layers (cont.)
9 Mon. Oct. 6 Laminar
Boundary Layers (cont.)
Wed. Oct. 8 Quiz
1
Mon. Oct. 13 Columbus
Day – Holiday
10 Wed. Oct. 15 Laminar
Internal Flows Mills: 4.3.1, 5.3
Lienhard: 8.1-8.2
White: 3.1-3.4, 4.9
K
& C: Ch. 7, 9
11 Mon. Oct. 20 Natural
Convection Mills: 4.4, 5.4.5, 5.8.1
Lienhard: 9.1-9.4
Bejan: Ch. 4
12 Wed. Oct. 22 Natural
Convection (cont.)
13 Mon. Oct. 27 Turbulence Mills: 5.5
White: 6.1-6.7, 6.10
K
& C: Ch. 5, 11-14
14 Wed. Oct. 29 Turbulence
(cont.)
15 Mon. Nov. 3 Turbulence
(cont.)
16 Wed. Nov. 5 Condensation Mills: 7.2
Lienhard: 9.5
Mon. Nov. 10 Veterans
Day – Vacation
Lienhard: 10.1-10.4
Mon. Nov. 17 Quiz
2
18 Wed. Nov. 19 Boiling
(cont.)
19 Mon. Nov. 24 Radiation Mills: Ch. 6
Lienhard: Ch. 11
Edwards: Ch. 1-3
20 Wed. Nov. 26 Radiation
(cont.)
21 Mon. Dec.
1 Radiation (cont.)
22 Wed. Dec.
3 Mass Transfer
23 Mon. Dec.
8 Mass Transfer (cont.)
24 Wed. Dec. 10 Mass
Transfer (cont.)
Dec. 15 – Dec. 19 Final Exam (time and place to be announced)
IV. REFERENCE MATERIALS
Heat Transfer, A. F. Mills, 1998
(Prentice Hall). TJ260.M52 1998
Heat and Mass Transfer, A.F.Mills, 1995 (Irwin).
TJ260M518 1995
A Heat
Transfer Textbook, J. H. Lienhard, 2nd edition, 1987 (Prentice Hall, Englewood
Cliffs). TJ260.L445
Introduction to
Physical Gas Dynamics, Vincenti & Kruger, (Kiley & Sons). QC168.V775
Viscous Fluid
Flow, F. M.
White, 2nd edition, 1991 (McGraw Hill, NYC).
QA929.W48
Convective
Heat and Mass Transfer, W. M. Kays and M. E. Crawford, 3rd edition, 1993 (McGraw Hill, NYC). QC327.K37
Convective
Heat Transfer,
A. Bejan, 1984 (John Wiley & Sons).
QC327.B48
Radiation Heat
Transfer Notes,
D. K. Edwards, 1981 (Hemisphere: Washington).
TJ260.E318
Conduction
Heat Transfer,
V. S. Arpaci, Abridged Edition, 1991 (Ginn Press, Nedham Heights, MA). (TJ260.A772).
V. PHYSICAL
PROPERTIES AND UNITS
Table
1: Physical Constants for 2.55
Stefan-Bolzmann constant, s 5.6697 ´ 10-8 W/m2K4
Ideal gas constant, R0 8314.3
J/kgmol·K
Bolzmann's constant, kB 1.3805
´ 10-23 J/K
Avogadro's
number, NA 6.022045 ´ 1026 molecules/kgmole
Table 2: Selected Conversion Factors
Dimension SI = multiplier ´ Other Unit
Density kg/m3 = 16.018 ´ lbm/ft3
kg/m3 = 103 ´ g/cm3
Diffusivity m2/s = 0.092903 ´ ft2/s
m2/s = 10-6 ´ centistokes
Energy J = 1055.04 ´ Btu
J = 4.1868 ´ cal
Flow Rate m3/s = 1.6667 ´ 10-5 ´ lpm
m3/s = 6.3090 ´ 10-5 ´ gal/min (gpm)
m3/s = 4.7195 ´ 10-4 ´ ft3/min (cfm)
Heat Flux W/m2 = 3.154 ´ Btu/hr·ft2
Heat transfer coefficient W/m2K = 5.6786 ´ Btu/hr·ft2°F
Length m = 0.0254 ´ inches
m = 0.3048 ´ feet
Power W = 0.022597 ´ ft·lbf/min
W = 0.29307 ´ Btu/hr
W = 745.700 ´ hp
Pressure Pa = 248.8 ´ in.
H2O (@60°F)
Pa = 6894.8 ´ psi
Pa = 101325 ´ atm
Specific Heat Capacity J/kg·K = 4186.9 ´ Btu/lbm·°F
J/kg·K = 4186.8 ´ cal/g·°C
Temperature K = 5/9 ´ °R
K = °C + 273.15
K = (°F + 459.67)/1.8
Thermal Conductivity W/m·K = 1.7397 ´ Btu/hr·ft°F
W/m·K = 418.68 ´ cal/s·cm°C
Viscosity (absolute) Pa·s = 10-3 ´ centipoise
Pa·s = 1.4881 ´ lbm/fts
Pa·s = 47.8803 ´ lbf·s/ft2