Corrigenda for REVISED SECOND EDITION, TRANSPORT PHENOMENA, byBird, Stewart, and Lightfoot (2007)

Most of the corrigenda tabulated here were sent to the authors byProfessor Carlos A. Ramírez of the University of Puerto Rico(Mayagüez), whose attention to details has been most helpful.

12a = line 12 from above 12 ll a = 12 lines above12b = line 12 from below 12 ll b = 12 lines belowfig = figure a 13.1-2 (above Eq. 13.1-2)fig capt = figure caption b 13.1-2 (below Eq. 13.1-2)

Page Location Reads Should Read

Inside Front ∇i∇v[ ]x=

∂2vx

∂x2 ∇i∇v[ ]x =

∂2vx

∂x2

Cover p. 2

3 19b area and, then changing and, by changing18b equations, write equations, immediately

writing

16 fig capt systems directions

17 5 ll a 1.2-2 τ xx ,τ xy ,andτ xz All τ should be lightface,

19 10 ll b dilational dilatational1.2-7

20 Fig (a) (angle theta missing) (add angle theta) 3rd dwg

25 fn 2 edition 1970) edition (1970)6.4. 6.4).

32 fn 2 24 34

39 1D.1(a) Put “[w x” down on next line.

51 fn 1 line 2 is roughly being roughly

58 §2.6 line 4 conveniently understood readily analyzed

61 above terminal velocity viscosity 2.6-17

73 upper fig upper phi should be theta (going in the tangential

direction)

81 3.3-1 irreversible irreversible

84 fn 2 L. M. H. C.-L.-M.-H.

91 fn 3 VanWazer Van Wazer

92 fig 3.6-2 (subscript) trans (subscript) crit

101 6a geometrically geometrically and dynamically

107 3B.7, 2a Fig. 3.B-7 Fig. 3B.7

111 3C.2, 2a example 3.1-1 Example 3.1-1

113 3D.3 Add after Eq. 3D.3-2: Do any additional restrictions have to be placed on this result?

129 a 4.3-21 function functions

139 fig Delete the vertical dashed line and the number 5.64

148 4C.2-11 t = 0 τ = 0Also, add: and dθR dτ = 0

148 4C.2-12 dθR dt = 0 dθR dτ = 04C.2-13 dθaR dt = 0 dθaR dτ = 0

154 fn 1 XXIIV XXIV

162 §5.4, line 2 5.2-11 and 12 5.2-10, 11, and 12

164 5.4-12 The bar should not extend over the “rho”

165 fig 5.5-1 The ordinate should be labeled as cm/sfig 5.5-2 The ordinate should be labeled as cm2/s2

166 fig capt (1950)}. (1950)].

169 a 5.6-2 The subscript xx should be changed to zz

173 last line 5.6-6 5.6-2

180 b 6.2-1 some distances some disturbances

183 b 6.2-16 cross-section cross-sectional area

183 b 6.2-18 mass rate of 1028 mass flow rate of 1028

188 fig 6.3-2 Portion of f versus Re Portion of f versus Re

193 6A.4 line 5 sec2 s2

196 fn 5 447 447-458

196 b 6C.3-2 the torque the magnitude of the torque

201 fig 7.2-1(b) Tube (remove “Tube”)

205 a 7.4-10 The fluid velocity The z-component of the fluid velocity

222 3b compressiblity compressibility

225 7A.5 ans 903 lb f 903 lb f to the right

232 12a the subject polymeric liquids

236 3a direction directions

246 3a higher derivatives higher time derivatives

249 fig capt subscripts on boldface deltas should be changed from 1, 2, 3 to italic x, y, z

250 6a dimensions of time. dimensions of time; also, trτ = τ iii∑

[the first “tau” should be bold face here]

250 fn 5, line 1 374 374 (1983)

262 8C.4, title F C M f c m8C.5 title M R R C m r r c

280 fn 2 Handbook of Handbook of

282 b 9.6-4 Move “That is” to the next line, and adjust accordingly.

285 b 9.8-4 by the unit vector by the normal unit vector

292 a 10.2-5 Eq. 9.1-1 Eq. 10.1-1

308 a 10.7-1 bar (twice) fin (twice)

310 2a tube thickness tube wall thickness3a bar fin

314 b 10.8-25 through the walls through the wall

327 10B.15 (a) temperature profiles temperature profiletemperature gradients temperature gradient

328 2b =12 B(1 ± 1 − 4N B( )

= 1

2 B 1 ± 1 − 4N B( )⎡⎣

⎤⎦

331 10C.3 line 2 T Tz

368 11B.15-2 ρ,β ρ ,β11B.15-3 ρ ρ

371 3a occluded includedb 11C.5-2 occlusions inclusions

371 11C.6-5 Move equation number down to next line (flush right)

382 5a Add at end of paragraph:Here r is the position vector defined in Eq. A.2-24.

384 2a small values. small values of z.

389 12.4-11 1st line Change the upper limit on the integral on the rightside from “infinity” to “1”.

393 12.4-9 hx hx

399 fn 3 110 121

406 12D.7-2 Remove the redundant right parenthesis ) just before the ]

407 Outline §13.6. §13.6•

407 16b If heat is If energy is

408 a 13.1-3 T = T + ′T T + ′T

409 fig 13.2-1 TR TR

412 b 13.4-6 vmax vmax

a 13.4-11 vz ,max vz ,max

413 13.4-18 & 19 T0 T0

13.4-18 & 19 Tb Tb

414 fig T0 T0 (twice)

Tb Tb (twice)

414 13.4-20 T0 T0

Tb Tb

415 a 13.5-9 Eq. 13.5-1 Eq. 13.5-4

419 a 13.6-20 energy equations energy equation

421 13C.1-1 T0 T0

& ans Tb Tb

423 b 14.4-1 J/hr J/s

424 fig Element of surface area Element with heat transfer area

428 14.2-3 hDk

hlocDk

429 1a constant heat flux constant wall heat flux

432 2 lines above b Move the “mu” up to the end of the line above

436 5a Move “RePr” down to the beginning of the line below

438 a 14.4-1 Fig. 14.1-1 Fig. 14.4-1

440 fn 5 (to be published) (unpublished)

440 fig Num0 Num ,0

441 fn 4 (to be published) (unpublished)

445 14.6-14 Num Numlam

14.6-15 Num Numlam

447 fn 3 “Z” should be italic

451 14B.1 Nu Nuloc (twice)

451 right col, 3a C is a constant. B and C are constants.

457 capt, 3a Move the integral sign down to beginning of next line

461 15.3-13 The right bracket “]” should not be under square root sign.

466 fn 1 Applications The Applications

468 fig capt Applications The ApplicationsEngineering Engineering Problems

475 15A.1 (c) amount mass flow rate (twice)

484 15C.3 ans rises increasesand may be obtained may be obtained

506 16.6-1 − ∇ipv( )

− p ∇iv( )

507 16.6-8 mαν maν

509 16B.5, 4a initally initially

527 1a “collisional integral” “collision integral”

530 a 17.4-8 diffusivity for diffusivity in cm2/s for

530 b 17.4-8 methanol; 1.0 methanol; 1.5 for ethanol; 1.0

535 4b DELETE: "plane perpendicular to the"

536 3b total mass mass1b for species for mass of species α

542 17C.3 (a) Use Use

545 18.1 d chemical rate coefficient chemical rate constant

549 a 18.2-20 33.0 mm Hg. 33.0 mm Hg, and its density is 1.629 g/ cm3

549 18.2-2 soln 1.59 1.629154 153.827.26 7.46

550 18.2-21 7.26 7.460.636 0.0634

553 fn 1 Damhöhler Damköhler

572 18B.6 f mass balance molar balance

589 fn b added to added to the right sides of

589 1a ρ ρ

591 fig The horizontal axis should labeled so that it extends from0 at the left to 1 at the right.

593 b 19.4-5 condensing. condensing, after diffusing in the –y direction.

601 14b and Gr. The concentration and Gr. The dimensionless concentration.

603 fig T T (3 times)

603 b 19.5-20 concentration-temperature temperature-concentration5b concentration-temperature temperature-concentration

603 b 19.5-20 On this page, there are 14 parentheses containingan omega and a capital T. In all of these, the order of theomega and capital T should be reversed.

604 5b the concentration profiles the dimensionless concentration profiles

605 17a the concentration profile the dimensionless concentration profile

607 fig Remove δ t( ) just above upper horizontal line.Label the upper horizontal line as z = 0.Label the upper surface of the shaded region as z = δ t( ) .

609 fn 6 Keys Keyes

613 table, col 3 Steady heat conduction solids Steady heat conduction in solids

617 3b the interfacial concentration the liquid-side interfacial concentration

633 3a 20.2-45 and 46 20.2-45 and 47

635 20.3-12 hx hx

20.3-14 hx hx

636 20.3-24 hx hx

20.3-26 hx hx

638 a 20.4-2 (u, v, 0) (u, v)

639 2b basis vectors base vectors

641 1a κ κ D AB( )

653 20C.1-4 ∂ωA

∂r

∂ωA

∂y

658 21.2-5 Cp Cp

664 4b Fig. 21.5(b) Fig. 21.5-1(b)

668 21B.2(a) approach to approach for

678 22.2-9 hx hx

22.2-10 hx hx

22.2-11 hx hx

22.2-12 hx hx

682 7a flow in circular tubes flow around circular cylinders

695 b 22.5-4 here where

696 b 22.5-8 here where

699 22.6-4 z = L (in upper limit) z = l0 (in upper limit)

700 b 22.7-3 forces in the stresses in the

702 1a-2a concentration concentrations

708 a 22.8-20 mass flux from the plate. mass flux at η = 0 .

711 1a factors θx and θT factor θx

712 22.8-38 kx kx ,loc

713 b 22.8-42 a stronger correction a larger correction

719 22.9.14 kx•

kx ,loc• (2 times)

xn−1,0

xN−1,0

[Note: here and elsewhere the "smileys" above the symbolsshould be "klitschkas"]

719 b 22.9-19 kx

. Dα ,φxα( )

kx• Dα ,

φxα( )

[the subscript on D shouldnot be under the D]

721 16b Standart and Krishna12 Krishna and Standart11

722 22A.3 What air temperature What inlet air temperature

722 22B.1(c) 5.6 - 5.6

727 10a emphasis on emphasis in

728 b 23.1-4 becauses moles are produced because the total numberor consumed of moles produced and the total number of moles

consumed are not equal

739 a 23.4-1 include the surface include he mass-transfer bounding surface

751 b 23.5-61 determined from Eq. 23.5-61 determined from Eq. 23.5-60

756 b 23.6-30 defined by: defined by (here r is the position vector defined in Eq. A.2-24):

757 a 23.6-35 according to Eq. 23.6-27 according to Eqs. 23.6-27

762 4a same surface and same surface area and

762 13a of the stream rates of the stream mass flow rates

764 2a Chapter 8 Chapter 9

772 ex title Ultra Centrifuge Ultracentrifuge

773 a 24.2-10 jA = 0 JA * = 0

777 a 24.4-7 we get we get (omitting thedirectional subscript ron NP

782 fn 5 great detail large amount

783 24.4-45 − +

784 b 24.4-51 Eq. 24.4-51 Eq. 24.4-50

786 a 24.5.4 membrane must membrane M musta 24.5-5 membrane is membrane M is

787 ref 6 181-165 131-165

788 3a membrane placed membrane M placed

788 a Solution index, z on the index z on the

788 13a Maxwell-Stefan equation Maxwell-Stefan equation (Eq. 24.5-4)

789 4a and the distribution and the solute distribution

789 b 24.5-12 and m refer and M refer

790 8a from that just described from the previous example

790 b 24.5-19 examining flow behavior examining the flow behavior

792 5a and for the salts and for the salt

792 24.5-31

RTzM+ F

⎛

⎝⎜

⎞

⎠⎟

−

RTzM+ F

⎛

⎝⎜

⎞

⎠⎟

793 9a the absorbent particles the adsorbent particles

793 fn 2 Fixed Bed Operations Fixed Bed Operations

799 24A.2 force of gravity gravitational acceleration

801 24C.3 cm2 /s × 105 ×105cm2 /s

802 24C.4 the electric field gradient (omit)the summation reduces to the summation in Eq.

24C.4-2 reduces to

803 24C.7 ′Dgw Dgw

membrane matrix membrane

803 24C.8 Add just before “Partial answer”:Here the subscripts s, w, and M refer tosolute, water, and membrane, respectively.

803 24C.9 (2) Ni = DimΔci Ni = −Dim∇ci

807 9a Greek symbols Greek letters

809 a A.1-6 magnitude of w magnitude of w

815 A.3-6 ε ijk ε ijl

817 a A.3-11 (add, run on)and its trace is tr τ = Σ iτ ii.

[The first tau is bold face, and the second tau is light face]

820 a A.4-7 operator operation

841 A.8-7 φ (in lower limit) φ1 (in lower limit)

857 5a Add text:In Eqs. C.5-12 and 13 an arbitrary constant ofintegration can be added to the right side.

873 n (A.5-1) (Fig. 1.7-2, A.5-1)

874 r (3.4-1) (3.4-1, A.2-24)

874 β s−1 t−1

874 bold δ 1.2-2 1.2-7

874 δ ij (A.2-1) (1.2-2, A.2-1)

875 sigma constant constant (16.2-11)

875 1b cross operations cross product operations

876 4a tensor tensor (1.2-7, A.3-8)

876 3b 12.2-24 12.2-21

877 Beek (delete 429) add 431

878 Eggink (delet 429) add 430

882 Poling Poling Poling, B. E.

882 Reichardt Move 416 up to the end of the previous line, and delete 165

882 a Riedel Insert: Richardson, S., 74

883 Valstar add 431

883 van Krevelen van Krevelen, D. W.

883 VanWazer VanWazer Van Wazer

891 No-slip add 74

893 Torricelli’s law add 217

900 6a [1999] [1999], Iowa StateUniversity [2007]

901 12b Chemical Engineering teaching Chemical Engineering

902 15b Universidad Nacional Instituto

902 14b Universidad Autónoma Universidad Nacional Autónoma

903 11b extracorporal extracorporeal

904 Awards Bioengineering award Bioengineering Award

905 1979 Elected… [1979]: this should start on the next line as aseparate entry

inside back cover Table 1.2-21 Table 1.2-1