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Similaire à 02 - Group 3 - P&ID - Piping and Instrumentation Diagrams
Similaire à 02 - Group 3 - P&ID - Piping and Instrumentation Diagrams (20)
02 - Group 3 - P&ID - Piping and Instrumentation Diagrams
- 10. moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW
[g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol]
1 CO2 44.00 0.3604 0.10% 15.9 0.27% 0.0 - - - - - 0.3604 0.10% 15.86 0.00 0.0
2 N2 28.00 0.1194 0.03% 3.3 0.06% 0.0 - - - - - 0.1194 0.03% 3.34 0.00 0.0
3 H2S 36.00 0.00009 0.00% 0.003 0.00% 0.0 - - - - - 0.0780 0.02% 2.81 0.00 0.0
4 CH4S 48.00 0.0803 0.02% 3.9 0.06% 0.0 - - - - - 0.0024 0.00% 0.12 0.00 0.0
5 CH4 16.04 328.2563 93.60% 5265.6 88.55% 15.0 - - - - - 328.3342 93.60% 5266.81 0.89 15.0
6 C2H6 30.07 21.8838 6.24% 658.0 11.07% 1.9 - - - - - 21.8838 6.24% 658.04 0.11 1.9
7 H2 2.02 - - - 0.08 100.00% 0.2 100.00% 2.0 - - - - -
350.70 100.00% 5946.66 100.00% 16.96 0.08 100.00% 0.16 100.00% 2.02 350.78 100.00% 5946.98 1.00 16.95
moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW
[g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol]
1 CO2 44 0.36 0.10% 15.9 0.27% 0.05 0.36 0.10% 15.9 0.27% 0.05 - - - - -
2 N2 28 0.12 0.03% 3.3 0.06% 0.01 0.12 0.03% 3.3 0.06% 0.01 - - - - -
3 H2S 36 0.08 0.02% 2.8 0.05% 0.01 0.01 0.00% 0.3 0.005% 0.00 - - - - -
4 CH4S 48 0.00 0.00% 0.1 0.002% 0.00 0.00 0.00% 0.1 0.002% 0.00 - - - - -
5 CH4 16.041 328.33 93.60% 5266.8 88.56% 15.01 328.33 93.62% 5266.8 88.60% 15.02 - - - - -
6 C2H6 30.07 21.88 6.24% 658.0 11.07% 1.88 21.88 6.24% 658.0 11.07% 1.88 - - - - -
7 H2Sout 36 - - - - - - - - - - 0.07 100.00% 2.5 100.00% 36.00
350.78 100.00% 5946.98 1.00 16.95 350.71 100.00% 5944.45 100.00% 16.95 0.07 1.00 2.53 1.00 36.00
SG-03
0.251Pipe Diameter (in) 1.75
Pipe Diameter (in) 1 1 -
1.00
0.05246.79234.18
228.28
-
MASS BALANCE
3SG-08 SG-04
- -
2.00
0.10 448.81
ΔP (bar)
ΔP (bar)
Volume rate (m3/h)
Volume rate (m3/h)
Total
Density gas (kg/m3
) 26.05 1.62 13.25
Pressure (bar) 40.00 40.00 39.00
Temperature (°K) 313.15 600.15 600.15
Temperature (°K) 313.15 313.15 313.15
Density gas (kg/m3
) 25.39 24.09 51.16
Molecular
Weight
Pressure (bar) 39.00 37.00 37.00
Total
HYDROGENOLYSIS REACTOR - HR-01
No. Component
MASS BALANCE
OUTLETMolecular
Weight
INLET
H-01 SG-06
INLET OUTLET
DESULFURISATION UNITS - DF-01 to DF-06
No. Component
- 11. moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW
[g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol]
1 CO2 44 0.36 0.10% 15.9 0.27% 0.05 - - - - - 0.36 0.04% 15.86 0.14% 0.02
2 N2 28 0.12 0.03% 3.3 0.06% 0.01 - - - - - 0.12 0.01% 3.34 0.03% 0.00
3 H2S 36 0.00009 0.00% 0.0 0.00% 0.00 - - - - - 0.00 0.000009% 0.003 0.00003% 0.00
4 CH4S 48 0.08 0.02% 3.9 0.06% 0.01 - - - - - 0.08 0.008% 3.86 0.04% 0.00
5 CH4 16.041 328.26 93.60% 5265.6 88.55% 15.01 - - - - - 49.24 5.01% 789.83 7.18% 0.80
6 C2H6 30.07 21.88 6.24% 658.0 11.07% 1.88 - - - - - 3.28 0.33% 98.71 0.90% 0.10
7 O2 32 - - - - 158.1 100.00% 5059.5 100.00% 32.00 - - - - -
8 CO 28.01 - - - - - - - - - 316.22 32.16% 8857.33 80.47% 9.01
9 H2 2.016 - - - - - - - - - 613.84 62.44% 1237.50 11.24% 1.26
350.70 100.00% 5946.66 100% 16.96 158.11 100.00% 5059.52 100.00% 32.00 983.14 100.00% 11006.43 100.00% 11.20
moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW
[g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol]
1 N2 28 0.12 0.01% 3.3 0.02% 0.0 - - - - - 0.12 0.01% 3.34 0.02% 0.0
2 H2S 36 0.00 0.00% 0.0 0.00% 0.0 - - - - - 0.00 0.00% 0.00 0.00% 0.0
3 CH4S 48 0.08 0.01% 3.9 0.02% 0.0 - - - - - 0.08 0.01% 3.86 0.02% 0.0
4 CH4 16.041 49.24 3.69% 789.8 4.55% 0.6 - - - - - 49.24 3.69% 789.83 4.55% 0.6
5 C2H6 30.07 3.28 0.25% 98.7 0.57% 0.1 - - - - - 3.28 0.25% 98.71 0.57% 0.1
6 CO 28.01 316.22 23.67% 8857.3 51.01% 6.6 - - - - - 9.30 0.70% 260.51 1.50% 0.2
7 H2O 18.016 352.96 26.42% 6358.9 36.62% 4.8 - - - - - 46.04 3.45% 829.42 4.78% 0.6
8 CO2 44 0.36 0.03% 15.9 0.09% 0.0 - - - - - 307.28 23.00% 13520.32 77.87% 10.1
9 H2 2.016 613.84 45.94% 1237.5 7.13% 0.9 - - - - - 920.76 68.91% 1856.25 10.69% 1.4
1336.10 100.00% 17365.31 100.00% 13.00 - - - - - 1336.10 100.00% 17362.24 100.00% 12.99
Pipe Diameter (in) 7 - 7
Pipe Diameter (in) 2 1 5
7.89
Pressure (bar)
Temperature (°K)
246.54591.17 1395.55
1896.57 - 1922.91
- 0.50
OUTLET
MASS BALANCE
POX - PARTIAL OXIDATION REACTOR - GR-01
-
-- 0.50ΔP (bar)
ΔP (bar)
Volume rate (m3/h)
Volume rate (m3/h)
Pressure (bar) 36.50 - 36.00
Molecular
Weight
Molecular
Weight
Temperature (°K) 623.15 - 623.15
Density gas (kg/m3
) 9.16 - 9.03
OUTLET
WGS - WATER GAS SHIFT - FIRST REACTOR - SR-01
MASS BALANCE
Total
SG-05
37.00
750.15
STH-01
Density gas (kg/m3
)
Total
No. Component OX-01
INLET
40.00
750.15
20.5210.06
623.15
36.50
STH-01 -
INLET
STH-02No. Component
- 12. moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW
[g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol]
1 N2 28 0.12 0.01% 3.34 0.02% 0.00 - - - - - 0.12 0.01% 3.34 0.00 0.0
2 H2S 36 0.00 0.00% 0.00 0.00% 0.00 - - - - - 0.00 0.00% 0.00 0.00 0.0
3 CH4S 48 0.08 0.01% 3.86 0.02% 0.00 - - - - - 0.08 0.01% 3.86 0.00 0.0
4 CH4 16.041 49.24 3.66% 789.83 4.50% 0.59 - - - - - 49.24 3.66% 789.83 0.04 0.6
5 C2H6 30.07 3.28 0.24% 98.71 0.56% 0.07 - - - - - 3.28 0.24% 98.71 0.01 0.1
6 CO 28.01 9.49 0.70% 265.83 1.51% 0.20 - - - - - 0.19 0.01% 5.32 0.00 0.0
7 H2O 18.016 56.73 4.21% 1022.11 5.82% 0.76 - - - - - 47.43 3.52% 854.55 0.05 0.6
8 CO2 44 307.28 22.81% 13520.32 76.99% 10.04 - - - - - 316.58 23.50% 13929.55 0.79 10.3
9 H2 2.016 920.76 68.36% 1856.25 10.57% 1.38 - - - - - 930.06 69.05% 1875.00 0.11 1.4
1346.98 100.00% 17560.25 100.00% 13.04 - - - - - 1346.98 100.00% 17560.16 1.00 13.04
moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW
[g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol]
1 N2 28 0.12 0.01% 3.3 0.02% 0.0 0.12 0.01% 3.3 0.02% 0.0 - - - -
2 H2S 36 0.00 0.00% 0.0 0.00% 0.0 0.00 0.00% 0.0 0.00% 0.0 - - - -
3 CH4S 48 0.08 0.01% 3.9 0.02% 0.0 0.08 0.01% 3.9 0.02% 0.0 - - - -
4 CH4 16.041 49.24 3.66% 789.8 4.50% 0.6 49.24 3.79% 789.8 4.73% 0.6 - - - -
5 C2H6 30.07 3.28 0.24% 98.7 0.56% 0.1 3.28 0.25% 98.7 0.59% 0.1 - - - -
6 CO 28.01 0.19 0.01% 5.3 0.03% 0.0 0.19 0.01% 5.3 0.03% 0.0 - - - -
7 H2O 18.016 47.43 3.52% 854.6 4.87% 0.6 - - - - 47.43 100.00% 854.55 100.00% 18.0
8 CO2 44 316.58 23.50% 13929.5 79.32% 10.3 316.58 24.36% 13929.5 83.38% 10.7 - - - -
9 H2 2.016 930.06 69.05% 1875.0 10.68% 1.4 930.06 71.57% 1875.0 11.22% 1.4 - - - -
1346.98 100.00% 17560.16 100.00% 13.04 1299.55 100.00% 16705.61 100.00% 12.85 47.43 100.00% 854.55 100.00% 18.02
0.50
Pipe Diameter (in) - -
Volume rate (m3/h)
1492.67-1471.94
997.611019.46 36.41
0.50
H-05
ΔP (bar)
ΔP (bar) -
Total
- -
Pipe Diameter (in) 3.50 3.75 1.00
17.23 16.75 23.47
Volume rate (m3/h)
35.00
Temperature (°K) 323.15 323.15 323.15
5
Molecular
Weight
INLET OUTLET
473.15
11.76
W-13
Density gas (kg/m3
) 11.93 -
Pressure (bar) 35.50 35.00
INLETMolecular
Weight
SEPARATOR - FD-01
No. Component
MASS BALANCE
H-06
OUTLET
Density gas (kg/m3
)
- 35.50
H-03
WGS - WATER GAS SHIFT - SECOND REACTOR - SR-02
No. Component
MASS BALANCE
STH-02 + H20 -
Temperature (°K) 473.15 -
Pressure (bar) 36.00
Total
- 13. moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW moles/time %Mole mass/time %W MW
[g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol] [kgmol/h] % [kg/h] % [g/gmol]
1 N2 28 0.12 0.01% 3.3 0.0 0.0 0.0001 0.00% 0.00 0.0002% 0.00 0.12 0.03% 3.3 0.02% 0.0
2 H2S 36 0.00 0.00% 0.0 0.0 0.0 0.0000001 0.00% 0.00 0.0000002% 0.00 0.00 0.00002% 0.0 0.00% 0.0
3 CH4S 48 0.08 0.01% 3.9 0.0 0.0 0.0001 0.00% 0.00 0.0003% 0.00 0.08 0.02% 3.9 0.03% 0.0
4 CH4 16.041 49.24 3.79% 789.8 0.0 0.6 0.06 0.01% 0.99 0.05% 0.00 49.18 13.00% 788.8 5.32% 2.1
5 C2H6 30.07 3.28 0.25% 98.7 0.0 0.1 0.004 0.00% 0.12 0.01% 0.00 3.28 0.87% 98.6 0.66% 0.3
6 CO 28.01 0.19 0.01% 5.3 0.0 0.0 0.0002 0.00% 0.01 0.0004% 0.00 0.19 0.05% 5.3 0.04% 0.0
7 CO2 44 316.58 24.36% 13929.5 0.8 10.7 0.40 0.04% 17.43 0.93% 0.02 316.18 83.57% 13912.1 93.81% 36.8
8 H2 2.016 930.06 71.57% 1875.0 0.1 1.4 920.76 99.95% 1856.3 99.01% 2.01 9.30 2.46% 18.8 0.13% 0.0
1299.55 100.00% 16705.61 1.00 12.85 921.22 100.00% 1874.81 100.00% 2.04 378.33 100.00% 14830.80 100.00% 39.20
Pipe Diameter (in) 3.75 3.25 -
2.00
Total
Volume rate (m3/h)
Temperature (°K)
Density gas (kg/m3
)
997.61 750.04 308.03
323.15 323.15 323.15
16.75
ΔP (bar) -
2.50 48.15
Pressure (bar) 35.00 33.00 33.00
PSA - PRESSURE SWING ADSORPTION UNITS - PSA-01 TO PSA-06
No. Component
MASS BALANCE
3
Molecular
Weight
INLET OUTLET
H-28 H-27
