Do material balance on two equipments (one should be reactive and other non-reactive)
Do material balance on two equipments (one should be reactive and other non-reactive)
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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Question
Do material balance on two equipments (one should be reactive and other non-reactive)
Transcribed Image Text:E-201 R-201
Reactor Ethylene Reactor High
Feed
Heater
E-202
V-201
V-202
Low
Effluent Pressure Pressure Compr
C-201
Flash-
Reactor
Cooler Separator Separator
Water
Ethylene
C-202
BFW
E-201 hps
T-201
R-201
E-202 cw
V-201
V-
LIC
LIC
Transcribed Image Text:Table 1: Stream Table for Ethylene Hydration Process - Unit 200
Stream No.
2
3
4
Temp °C
Pres kPa
Vapor mole fraction
Total kg/h
Total kmol/h
Flowrates in kmol/h
Methane
Acetylene
Ethylene
Acetaldehyde
25
202
25
85
229
264
50
5,000
1.00
2,384.54
4,925
4,915
0.35
5,000
5,000
5,000
4,975
1.00
0.39
1.00
1.00
18,266.46
653,86
18,015.00
1,000.00
|36,281.45
1,653.86
36,282.11
1,653.89
36,282.11
36,282.11
1,574.84
85.00
1.574.84
0.0042
0.51
0.51
0.51
0.0001
0.51
0.51
0.0001
0.0001
0.0001
84.9958
644.18
0.00
644.18
0.00
644.20
0.00
565.15
565.15
0.00
0.00
79.80
929.37
79.80
929.37
Ethanol
0,76
0.76
0,76
Water
8.41
1,000.00
1,008.41
1,008.41
Stream No.
8
9
10
11
12
13
14
Temp °C
Pres kPa
Vapor mole fraction
Total kg/h
Total kmol/h
| Flowrates in kmol/h
Methane
|Acetylene
Ethylene
Acetaldehyde
Ethanol
36
36
36
35
35
87
36
500
500
500
250
250
500
500
0.37
1.00
0.00
1.00
1.00
1.00
36,282.11
1,574.84
16,162.52
575.36
20,119.60
999.48
20,119.60
999.48
16,200.26
576.70
37.75
37.75
1.34
1.34
0.51
0.51
0.00
0.00
0.00
0.00
0.51
1.
1.
1.
563.90
0,00
565.15
562.62
2.54
2.54
1.29
1.29
0.00
0,00
0,00
0.00
79.80
929.37
74.45
922.49
5.36
74.45
922.49
5.38
6.90
0.02
0.02
Water
6.87
0.03
0.03
Table 1: Stream Table for Ethylene Hydration Process - Unit 200 (cont'd)
Stream No.
15
16
17
18
19
20
21
Temp °C
30
39
37
39
228
228
37
Pres kPa
500
500
520
500
5,000
5,000
1.00
15,881.92
230
Vapor mole fraction
Total kg/h
1.00
1.00
1.00
0.00
16,010.00
573.45
15,881.92
568,86
1,801.50
1,991.77
103.25
15,881.92
1,991.77
Total kmol/h
100.00
568.86
568.86
103.25
Flowrates in kmol/h
Methane
Acetylene
Ethylene
Acetaldehyde
0.51
0.51
0.51
0.51
563.69
0.21
559.18
559.18
559.18
0.21
0.00
0.00
0.00
0.00
0.76
8.41
0.76
0.76
8.41
Ethanol
4.62
0.76
4.62
Water
100.00
8.48
98.42
8.41
98.42
Stream No.
22
23
24
25
26
27
28
Temp °C
35
123
127
99
50
50
50
Pres kPa
250
235
250
230
220
220
220
Vapor mole fraction
Total kg/h
Total kmol/h
1.00
1.00
0.01
1.00
18,280,14
3,793.48
89.13
20,081.85
20,081.85
998.13
3,793.48
27.23
3,766.25
998,13
1,012.26
89.13
0.90
88.23
Flowrates in kmol/h
Methane
Acetylene
Ethylene
Acetaldehyde
Ethanol
Water
1.25
1.25
1.46
1.46
0.77
0.69
0.00
0.00
0.00
0,00
0.00
1.58
77,46
74.42
922.46
77.35
10.20
74.42
77.46
10.21
0.12
0.01
922.46
1,010.67
10,21
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