Fundamentals of Chemical Engineering Thermodynamics

Fundamentals of Chemical Engineering Thermodynamics
Kevin D. Dahm and Donald P. Visco, Jr.
9781111580704
First Edition
Errata for First Printing
Page
Number
12
Correction Description
36
70
70
In paragraph starting with “‘One Kelvin’ is defined,” change “plus” to “minus” where marked.
“…rather than specific molar enthalpy, gives…
79
81
89
Add circled part to the equation.
In problem 2-15 parts B and C, change “exists” to “exits”
In the table in the upper left corner, there is an H that has both underline and a ^ over it. The ^ is
correct. It should NOT be underlined.
In equation 3.9, add circled numbers,
91
92
93
105
Change “lb” to “lbm” , so that denominator is 162 lbm/lb-mol
Change “Step 6” to “Step 7”, and “Step 7” to “Step 8”
4th line “…time-dependent Equation 3.31:” should be “Equation 3.1”
The sentence, "...since that it is what we are trying to determine,"
Page
Number
116
Correction Description
Replace “36,560” with “38,560.”
Replace “kJ/mol” with “J/mol”
117
Change "36,560" to "38,560"
Change "44,400" to "46,400"
128
162
187
188
192
211
212
232
233
234 & 235
235
274
285
285
286
317
In problem 3-27, change “1 bar” to “1 atm”
In Step 5, change “ 669.0” to “946.0”
Problem 4-12. “A 10 ounce glass that is half full of water (half full)…”
Problem 4-27. “…at T=100 degrees F and expels it as a saturated liquid at T=100 degrees F.
Immediately above Figure 5-2, change “on the operation of the reactor” to “on the safety of, or the
operation of, the reactor”
In margin note at the bottom of the page, change step “7” to step “6”
Every mention of the following on this page should be changed:
- step “7” to step “6”
- step “8” to step “7”
- step “9” to step “8”
- step “10” to step “9”
- step “11” to step “10”
- step “6” to step “5”
In problem 5-7, parts B and C, change each mention of “HFC-134a” to “R-422A”
In problem 5-10, change “HFC-134a” to R-422A”
In problem 5-16, change all mentions of “R-134a” to “R-422A”
In problem 5-19, change “HFC-134a” to “R-422A”
The “HR” in equation 6.141 should be “HR”
In the last line above problem 6-14, change “CP* = 40 J/mol” to “CP* = 40 J/mol·K”
In problem 6-16 part C, change “1.5 kJ/min” to “1.5 kJ/min·K”
In problem 6-20 part A, change “0.100 mol/L” to “0.100 L/mol”
In Figure 7-10, there are two lines that are labelled “T=400 (l)
The darker line (for which the label is on the right hand side) should be labelled “T=450 (l)
Page
Number
326
Correction Description
399
Paragraph 3, change sentence to read “Next, you have another system that has one black molecule than
can be in either of the two available locations (different than the blue system).
One of the chemical structures in the margin is for “1-hexanol”. This figure should be removed and
replaced with “1-hexene”. The structure of 1-hexene is:
403
H
C
H2C
403
408
419
420
423
478
H2
C
C
H2
CH3
C
H2
In the paragraph that follows the end of the example, there are two references to “Andrzej et. al.,
2010”. Please change both to “Treszczanowicz et al., 2010”
In 2nd paragraph, delete “component.” and replace with “the components.”
In the sentence following Equation 9.65, delete “is” and replace with “it”
In equation 9.68, the superscript “IG” should be “ig”
In problem 9-3, change “ethanol” to “2-propanol”
Equations 11.34 and 11.39 at the bottom of the page- there is a hat missing on the middle term.
11.34 should be: = = Page
Number
Correction Description
11.39 should be: = = 482
486
504
530
540
547
553
570
580
607
607
609
609
609
609
609
609
609
610
In the problem statement for Example 11-2, between “…0.1 mol% benzene.” and “You know the
infinite…” add a new sentence that reads “The absorber operates at 20 °C.”
Equation 9.48, in the middle of the page, should be numbered 9.42. The text also contains two
references to “Equation 9.48”, one above the equation and one below it, that should be changed to
“Equation 9.42”
Unnumbered equations in the middle of the page- please change “0.3354” to “0.3646” and change
“0.2846” to “0.2852”
In the caption of Table P11-27, change “70 °C” to “40 °C”
"Recall the virial equation as provided in Equation 7.78 7.91:"
The equation number right below it should be listed as 7.91 and not 7.78
Table 12-5 caption. Add a "(2)" after "dimethyl carbonate" in the caption.
“…dimethyl carbonate (2) system at ….
The equation that is currently numbered “(8.88)” should be “(8.67)”
In problem 12-23, change “… at 413.15 Kusing the” to “…at 413.15 K using the …”
In the bottom paragraph, there are two references to “Figure 12-1”, both of which should be changed to
“Figure 13-1”.
In the problem statement for Example 13-11, part b, change “At what temperature and composition
does the eutectic occur?” to “At what temperature and composition does the eutectic occur, according
to the model?”
In the problem statement for Example 13-11, part c, change the end from “…as the temperature is
lowered.” to “…as the temperature is lowered, according to the model.”
Change the heading for Step 5 from “The eutectic temperature and composition” to “The eutectic
temperature and composition according to the model”
At the end of the first paragraph under the “Step 5” heading, change “T = 305 K and x1 = 0.71.” to “T =
305 K and x1 = 0.67.”
At the end of the second paragraph under the “Step 5” heading, change “T = 305.02 K and x1 = 0.715.” to
“T = 303.66 K and x1 = 0.672.”
Change the heading for Step 6 from “Cooling a system of x1 = 0.6 from 330 K to 300 K” to “Cooling a
system of x1 = 0.6 from 330 K to 300 K according to the model”
In the third line below the Step 6 heading, change “about 315 K” to “about 312 K”.
In the fourth line from the bottom of the page, change “305.02 K” to “303.66 K”
In the second line from the bottom of the page, change “x1 = 0.715” to “x1 = 0.672”
Replace Figure 13-18 with this figure. (The caption should not change.)
Page
Number
Correction Description
360
350
Temperature (K)
340
330
320
310
300
290
280
0
0.2
0.4
0.6
0.8
1
mole fraction hexane-1,6 diamine
615
616
643
646
655
693
743
746
749
In the problem statement for problem 13-29, delete the following section of text: “If you were to
improve the modeling result through the use of an excess molar Gibbs free energy model, would the
activity coefficients for the system need to be greater than or less than 1 to bring the model closer to
the experimental data? Please demonstrate how you arrived at your answer.” The text before and after
this section should remain as is, and the two margin figures should remain intact.
In the problem statement for problem 13-30, part C, change “76%” to “60%”
First line under equation 14.78, “analogous to step 4” should be “analogous to step 3”
In Table 14-8, bottom row leftmost column, change the “y” to an “x”
In equation 14.112, delete “=7.47x1018” from the end of the line.
Add a margin note immediately below the “Example 15-6” heading that says “Oxygen is treated as an
“inert” in this problem because it does not participate in the chemical reaction examined here. But it is
certainly not an “inert” compound in general. The presence of oxygen in a system that also contains
flammable/explosive compounds is a severe hazard.”
Change “HFC-134a (also known as R-134a or 1,1,1,2-tetrafluoroethane) to “R-422A (also known as R422a or ISCEON® 79”
At the top of the page, change “HFC-134a” to “R-422A” and “R-134a or 1,1,1,2-Tetrafluoroethane” to
“ISCEON® 79”
The second to last entry under “Non-ring increments” currently reads “=CH”. It should be “≡CH”