Rev. 2/18/08
ERRATA – Thermal-Fluid Sciences: An Integrated Approach
p. 5 -
Caption at bottom: Lower case “k” in “kingfisher”
p. 25 -
Line 7: Replace “terminology” with “term”
p. 31 -
5th line in section 1.7: “International (SI) d’Unités”
p. 40 -
Left column, last line: “I-S” should be “1-s”
p. 42 -
Prob. 1.43: Delete comma in “1000”
p. 50 -
Line above Number of Moles: “Measure” should be “Measures”
p. 77 -
5 lines from bottom (not counting footnote): “Eqn. 3.32” should be “Eqn.
2.32”
p. 127 -
Fig. 2.33 RH axis units: Add “sub m” to “lb”, i.e., “lbm”
p. 132 -
Fig. 2.34: Tweak triple point pointer to point at bold dot
p. 138 -
Footnote 17: Change “temperature” to “pressure”
p. 148 -
Line 20: Change “T/P” to “P/T”
p. 152 -
1st line 2nd column: “Avogadro”
p. 153 -
Next to last line, 2nd column: Italic “P” in “P°”
p. 164 -
Prob. 2.105: Insert “1 kg of” after “contains”
p. 164 -
Problem 2.112: Change mass from “0.136” to “1.36” kg
p. 169 -
Denominator of Eqn. 2A.3: “ ‘ ” should be “ ! ”
p. 176 -
Ex. 3.1: Delete comma in “1250”
p. 191 -
First unnumbered equation: Change bold “V” to unbold “V”
p. 232 -
Prob. 3.22: Change “170°C” to “169°C”
p. 273 -
Problems 3.67 & 3.68: Insert “Assume incompressible flow.”
p. 275 -
Self Test 4.6: Insert period after last sentence of answer: “energy.)”
Rev. 2/18/08
p. 278 -
Caption to Fig. 4.16; Courtesy line should read “Photographs (b, c, d) by
Paul Ruby, (a) by Sibtosh Pal …”
p. 280 -
2nd equation: Add overbar to hconv: hconv
p. 287 -
3rd line from bottom: Insert left parenthesis before [=], i.e. ([=].
p. 362 -
Ex. 5.17: Change T2 to T4 in drawing following problem statement.
p. 364 p. 366 -
Middle of page: Reference to Eq. 5.63a should be Eq. 5.63e.
Self Test 5.13: Answer should be “9.5 m/s”
p. 367 -
Eqn. 5.70: Delete subscript “in” on “m-dot”
p. 399 -
Enthalpies in problem 5.144 should be 2856.5 kJ/kg and 2562.2 kJ/kg,
respectively. Note change in Answers to Selected Problems (p. 1152) for
this problem.
p. 415 -
Fig. 6.6: Wrong font for “d” in “dV”
p. 420 -
2nd line of Comment: “9900” should be “8800”
p. 422 -
2nd equation: RHS is missing “P2 +”, i.e., P2’ = P2 + etc.
p. 455 -
The shear stress terms in Eq. 6.63a should read:
∂xx/∂x + ∂yx/∂y + ∂zx/∂z
Similarly, the shear stress terms in Eq. 6.63b should read:
∂xy/∂x + ∂yy/∂y + ∂zy/∂z
And shear stress terms in Eq. 6.63c should read:
∂xz/∂x + ∂yz/∂y + ∂zx/∂z
p. 475 -
Insert density on RHS of Euler equation within the unnumbered equation:
Location 2

V ( P   g   DV / Dt )ds.
Location 1
p. 480 -
3rd line from bottom: replace “an” with “a”
p. 490 -
Prob. 6.20: 2nd & 3rd sentence combined should read: “The right and left
legs of the manometer have diameters d1 and d2, respectively, with z0 the
elevation at which the levels in the two legs become equal.”
Note also that the interface between Fluid A & Fluid B on the sketch
should be moved down an arbitrary a distance below z0.
Rev. 2/18/08
p. 495 -
Problem 6.51: The dimension “L” should include only the cork and not
the nickel.
p. 505 -
Problem 6.112: Reposition bottom dimension arrow to elevation of hole,
not bottom of tank.
p. 506 -
Problem 6.120: Delete “(P1 = 150 kPa)”. Insert the following before
“Find the suction…”: “The pressure in the large-diameter main water line,
which supplies water to the primary tube of the device, is P0 = 150 kPa.
The velocity in the water main is negligible.”
p. 509 -
2 lines above Eq. 6.59b: Replace “a noninertial;” with “an inertial”
p. 517 -
In 2nd equation & within Self Test 7.1, lower case “m” should be capital
“M”
p. 517 -
Self Test 7.1: Delete “and pressure”
p. 532
Fig. 7.14: “W-dot-1-2” should be “W-dot-4-1”
p. 538 -
Sentence above Eqn. 7.22a should begin “For Case II” (not Case I),
whereas sentence below Eqn. 7.22a should begin “For Case I” (not Case
II).
p. 545 -
Self Test 7.6: Add masses to parenthetical material: “(2 kg copper and 2.5
kg iron)”
p. 553 -
Top box: Lower case “c” in “chapter”
p. 560 -
Answer to Self Test 7.9: Insert solidus before (1/Pº), i.e., “/(1/Pº)”
p. 568 -
Add “M Mass (kg)” to nomenclature list
p. 580 -
Problem 7.111: “mole function” should read “mole fraction”
p. 590 -
Fig. 8.4 vertical axis: “cL” should be “cL”
p. 612 -
Add to Problem 8.4: “What happens if you force Red to appear within
your result?”
p. 613 -
Problem 8.12: Add T & P: “… at 30,000 ft. (T = 229 K, P = 29 kPa).”
p. 642 -
Fig. 9.13: Remove small rectangles in vertical axis legend and legend on
figure.
p. 643 -
2nd line above “Comments”: “0.36” should be “0.036”
Rev. 2/18/08
p. 649 -
1st & 4th equations: “0.322” should be “0.332”
p. 656 -
Fig. 9.17: Remove small rectangle in legend of bottom sketch
p. 657 -
Fig. 9.18: Remove small rectangle in vertical axis legend
p. 664 -
7 lines from bottom including equations: subscript “eonv, L” should be
“conv, L”
p. 668 -
3rd line below “Cylinders & Other 2-D Shapes’: Replace “ ≤ 5x105 ” with
“ > 104 ”
p. 677 -
Assumption ii: Replace “ >” with “>>”
p. 670 -
Fig. 9.25: Remove small rectangle in vertical axis legend
p. 747 -
7th line following list of assumptions: “vx(x only) should be “vx(r only)”
p. 789 -
CFD art at top: Zero in legend is cut off.
p. 807 -
Prob. 10.25: Parts (a) & (b) should read: 0.253 cm3/s and 0.15 cm3/s,
respectively. Correct answers: (a) 1.38x10-6 m2/s (b) 2.38x10-6 m2/s (c)
9.02x10-6 m2/s.
p. 844 -
Line 6: Lower case “k” in “kelvins”
p. 851 -
1st line: Inequalities are reversed. Should read: “P0 > Pb ≥ Pc”
p. 869 -
Eqn. 11.39d: Add “g” in denominator of last term
p. 888 -
Change values for h1 and h2 (2 locations) to “1798.6” and “861.1”,
respectively, to agree with Table C.2 values
p. 896 -
Eqn. 11.56: Add subscript “C” to m-dot on RHS
p. 896 -
Eqn. 11.58a: Add subscript “H” to m-dot on RHS
p. 897 -
Eqn. 11.58b: Add subscript “C” to m-dot on RHS
p. 931 -
Chapter 11 Problem Subject Areas: Change “11.21” to “11.20” & change
“11.22” to “11.21”.
p. 933 -
Prob. 11.17: Change “14 psia” to “16 psia”
p. 935 -
Prob. 11.32: Change “at the nozzle exit Pe” to “in tank B”
Rev. 2/18/08
p. 940 -
Prob. 11.101: Units on the convective heat-transfer coefficient should be
“W/m2·ºC”
p. 974 -
Add arrowhead to “Steam out”
p. 1020 -
Fig. 12.40: Pointer to “Capillary tube” is incorrectly located. It should
point to coil of copper tubing near center of photo. See same figure from
Thermodynamics for correct location.
p. 1027 -
Example 12.15: Change “mm Hg” to “in Hg” in problem statement and in
Analysis section.
p. 1042 -
2nd column, 2nd line from bottom: Add hyphen at end of line.
p. 1047 -
Problem 12.43: Formula for iso-octane should be “C10H18”
p. 1049 -
Problem 12.55: Replace “compression” with “heat addition”
p. 1050 -
Problem 12.59: Add “per unit mass” to the end of the last sentence.
p. 1050 -
Problem 12.60: Add “per unit mass” to the end of the last sentence.
p. 1051 -
Problem 12.70: Add to Part C “The turbine inlet temperature is 1500 K.”
Modify Part D, 2nd & 3rd lines to read “thermal efficiency for no
regeneration. Discuss.”
p. 1054 -
Problem 12.91: Add “Hint: Use saturation temperature for R-22 inlet and
outlet to evaluate Tlm.”
p. 1058 -
Prob. 12.126: Reword: …0.15 MPa. Does any moisture condense? If so,
determine the moisture condensation rate (kg/min). If not, determine the
relative humidity.
p. 1059 -
Problem 12.135: Insert “(dry basis)” after “4-lbm mass of air” and after “1lbm mass of air”
p. 1059 -
Problem 12.139: Add “at 1 atm” to the end of the last sentence.
p. 1059 -
Problem 12.143: Add word “flow” after word “mass” in Parts B & C.
p. 1062 -
Problem 12.170: Change “is maintained” to “contains air”.
p. 1063 -
Prob. 12.173: Remove “dry-bulb”.
p. 1107 -
Table D.3V heading: Replace “24.0” with “26.0”
Rev. 2/18/08
p. 1149 -
Round answers to Problem 2.17c and 2.17d to five significant digits:
51,386 kJ/kmol, 56,364 kJ/kmol
p. 1150 -
Prob. 2.96 answer should be: 0.0023 kg
p. 1150 -
Prob. 2.112 answer should be: 454 K
p. 1150 -
Problem 3.8: A. 0.04852, B. 0.02536 kg, 0.05997 m3,
C. 0.002316 kg, 2.40 x 10-5 m3
p. 1151 -
Problem 5.65 answer should be 2333 W (Solution Manual is OK)
p. 1152 -
Answer to Problem 5.144 with revised enthalpies (2856.5 kJ/kg and
2562.2 kJ/kg) is 769.4 m/s.