n-Butane is converted to isobutane in a continuous isomerization reactor that operates isothermally at 175 °C. The feed to the reactor contains 83 mole% n-butane vapor, 15% isobutane vapor, and 2% HCl vapor at 175 °C, and a 50% conversion of n-butane is achieved. Assuming a basis of 1 mol of feed gas, calculate the amount of heat transfer to/from the reactor (kJ). The heat capacity for n-butane is 148.66 J/mol K and that for isobutane is 149.24 J/mol K. Use a reference state of 25 °C and 1 atm.
n-Butane is converted to isobutane in a continuous isomerization reactor that operates isothermally at 175 °C. The feed to the reactor contains 83 mole% n-butane vapor, 15% isobutane vapor, and 2% HCl vapor at 175 °C, and a 50% conversion of n-butane is achieved. Assuming a basis of 1 mol of feed gas, calculate the amount of heat transfer to/from the reactor (kJ). The heat capacity for n-butane is 148.66 J/mol K and that for isobutane is 149.24 J/mol K. Use a reference state of 25 °C and 1 atm.
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Transcribed Image Text:TABLE B.1 Selected Physical Property Data
SG
Mol. Wt. (20%/4°)
Compound
Acetaldehyde
Acetic acid
Acetone
Acetylene
Ammonia
Formula
CH CHO
CH₂COOH
carbonate
Calcium
chloride
C₂H₂O
C₂H₂
NH;
Ammonium NH₂OH
hydroxide
Ammonium
nitrate
Ammonium
sulfate
Aniline
Benzaldehyde
Benzene
C₂H6
Benzoic acid
C₂H₂O₂
Benzyl alcohol C₂H₂O
Bromine
Br₂
1,2-Butadiene C₂H6
1,3-Butadiene C₂H₂
n-Butane
C₂H₂0
Isobutane
C₂H₂0
1-Butene
C₂H₂
CaC₂
Calcium
carbide
Calcium
CaCO3
44.05 0.78318
60.05 1.049
58.08 0.791
26.04
17.03
CaCl₂
NHNO,
(NH,)SO. 132.14
CH₂N
C₂HSCHO
35.03
80.05 1.7252⁹
=
1.769
93.12 1.022
106.12 1.046
78.11 0.879
100.09
122.12
1.2661
108.13 1.045
159.83 3.119
54.09
54.09
58.12
58.12
56.10
64.10 2.22
2.93
110.99 2.15215
T₁ (°C)
-123.7
16.6
-95.0
-77.8
169.6
513
-6.3
-26.0
5.53
122.2
-154
-74
-136.5
-109.1
-138.3
-159,6
-185.3
2300
782
AĤ(Tm)
kJ/mol
12.09
5.69
5.653
5.4
I
||
9.837
10.8
4.661
4.540
3.8480
28.37
Tb (°C)
20.2
118.2
56.0
-81.5
-33.43
184.2
179.0
80.10
249.8
205.2
58.6
10.1
-4.6
-0.6
AR, (T₂)
kJ/mol T.(K) P.(atm)/
25.1
24.39
30.2
17.6
309.5
61.6
23.351 405.5 111.3
38.40
Decomposes at 210°C
Decomposes at 513°C
after melting
699
30.765
31.0
22.305
-11.73
-6.25 21.916
461.0
594.8 57.1
47.0
21.292
Decomposes at 825°C
>1600
508.0
562.6
52.4
48.6
584
446
425
42.7
425.17
37.47
408.1 36.0
419.6 39.7
102
(AH)
(kJ)
-166.2(g) -1192.4(g)
-486.18(1)
-871.69(1)
-438.15(g) -919.73(g)
-248.2(1)
-1785.7(1)
-216.7(g) -1821.4(g)
+226.75(g) -1299.6(g)
-67.20(1)
-46.19(g) -382.58(g)
-366.48(aq)
-365.14(c)
-399.36(aq)
-1179.3(c)
-1173.1(aq)
(AH₂)
(kJ)
-88.83(1) -3520.0(1)
-40.04(g)
+48.66(1) -3267.6(1)
+82.93(g) -3301.5(g)
3226.7(g)
-3741.8(1)
0(1)
-147.0(1)
-124.7(g)
-794.96(c)
-2855.6(1)
2878.5(g)
-2849.0(1)
-158.4(1)
-134.5(g) -2868.8(g)
+1.17(g)
-62.76(c)
-2718.6(g)
-1206.9(c)
25 °C and 1 atm.
J/mol
mol of feed gas, calculate the amount of heat transfer to/from the reactor (kJ). The heat capacity
2% HCl vapor at 175 °C, and a 50% conversion of n-butane is achieved. Assuming a basis of 1
at 175 °C. The feed to the reactor contains 83 mole% n-butane vapor, 15% isobutane vapor, and
for n-butane is 148.66 K and that for isobutane is 149.24 J/mol K. Use a reference state of
n-Butane is converted to isobutane in a continuous isomerization reactor that operates isothermally
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