X1
|
SRC1 |
The feed of ethylene |
kmol/h |
500 |
800 |
X2
|
SRC2 |
The feed of oxygen |
kmol/h |
550 |
850 |
X3
|
SRC3 |
The feed of methane |
kmol/h |
250 |
450 |
X4
|
R1 |
The number of tubes |
- |
500 |
900 |
X5
|
R1 |
Reactor length |
m |
20.0 |
60.0 |
X6
|
R1 |
Reactor temperature |
K |
498 |
523 |
X7
|
SRC4 |
The feed of water |
kmol/h |
1.00×103
|
2.00×103
|
X8
|
T1 |
The number of stages |
- |
13 |
15 |
X9
|
SP1 |
The rate of separation |
- |
0.00100 |
0.0500 |
X10
|
SP2 |
The rate of separation |
- |
0.00100 |
0.500 |
X11
|
T2 |
Pressure |
bar |
0.100 |
0.900 |
X12
|
T2 |
The number of stages |
- |
13 |
15 |
X13
|
T2 |
The number of feed stages |
- |
10 |
13 |
X14
|
T2 |
Bottom reflux ratio |
- |
0.0500 |
1.50 |
X15
|
T3 |
Pressure |
bar |
3.00 |
7.00 |
X16
|
T3 |
The number of stages |
- |
13 |
15 |
X17
|
T3 |
The number of feed stages |
- |
10 |
13 |
X18
|
T3 |
Bottom reflux ratio |
- |
0.500 |
1.50 |
X19
|
T3 |
Vapor fraction |
- |
0.100 |
0.700 |
X20
|
T4 |
Pressure |
bar |
0.100 |
0.900 |
X21
|
T4 |
The number of stages |
- |
13 |
15 |
X22
|
T4 |
The number of feed stages |
- |
10 |
13 |
X23
|
T4 |
Bottom reflux ratio |
- |
0.100 |
1.00 |
X24
|
T4 |
Top reflux ratio |
- |
0.500 |
2.00 |