Corrigenda for REVISED SECOND EDITION, TRANSPORT PHENOMENA, by Bird, Stewart, and Lightfoot (2007) Most of the corrigenda tabulated here were sent to the authors by Professor 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 above 12b = line 12 from below 12 ll b = 12 lines below fig = 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 = ∂ 2 v x ∂x 2 ∇i∇v [ ] x = ∂ 2 v x ∂x 2 Cover p. 2 3 19b area and, then changing and, by changing 18b 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 dilatational 1.2-7 20 Fig (a) (angle theta missing) (add angle theta) 3 rd 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
This document is posted to help you gain knowledge. Please leave a comment to let me know what you think about it! Share it to your friends and learn new things together.
Transcript
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,
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