Table 5.
Open in new tab

Input conditions for simulating hydrogen production process.

StreamValues or assumptions
11 (Water-1)(Mass flow of 3 kg/s–T = 20°C–P = 1 atm)
14 (Natural gas)(Mass flow of 1 kg/s–T = 25°C–P = 1 atm)
StreamValues or assumptions
11 (Water-1)(Mass flow of 3 kg/s–T = 20°C–P = 1 atm)
14 (Natural gas)(Mass flow of 1 kg/s–T = 25°C–P = 1 atm)
BlockAssumptions
HE-1T18 = 270°C
HE-2T13 = 270°C
HE-3T20 = 75°C
ReformerR-Gibbs reactor , T = 520°C
WGSR-Gibbs reactor
BlockAssumptions
HE-1T18 = 270°C
HE-2T13 = 270°C
HE-3T20 = 75°C
ReformerR-Gibbs reactor , T = 520°C
WGSR-Gibbs reactor
Table 5.
Open in new tab

Input conditions for simulating hydrogen production process.

StreamValues or assumptions
11 (Water-1)(Mass flow of 3 kg/s–T = 20°C–P = 1 atm)
14 (Natural gas)(Mass flow of 1 kg/s–T = 25°C–P = 1 atm)
StreamValues or assumptions
11 (Water-1)(Mass flow of 3 kg/s–T = 20°C–P = 1 atm)
14 (Natural gas)(Mass flow of 1 kg/s–T = 25°C–P = 1 atm)
BlockAssumptions
HE-1T18 = 270°C
HE-2T13 = 270°C
HE-3T20 = 75°C
ReformerR-Gibbs reactor , T = 520°C
WGSR-Gibbs reactor
BlockAssumptions
HE-1T18 = 270°C
HE-2T13 = 270°C
HE-3T20 = 75°C
ReformerR-Gibbs reactor , T = 520°C
WGSR-Gibbs reactor
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