Hydrogen Membrane Reformer Technology
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INTERNAL
Hydrogen Membrane
Reformer Technology
6.11.2003
L
Hydrogen Mixed Conducting Membranes
PH2(I) PH2(II)
e-
½ H2 ½ H2
H+
(Syngas) (Hydrogen)
½ H2 H+ + e- H+ + e- ½ H2
PH2(I) > PH2 (II)
•Driving force for H2: H2 flux ≈ log PH2(I) / PH2(II)
•Membrane material 100% dense
EPI
Porsgrunn KÅ - Date: 2003-11-04 - Page: 2
L
Hydrogen Membrane Reformer
• extract product gas (H2) from reactor
• drive equilibrium limited reactions towards
completion
• expand allowed range of temperatures and
pressures
ΔH = + 165 KJ/mol
CO2
CH4 + H2O
CH4 + 2H2O = 4 H2 + CO2
H2 transport H2
membrane
EPI
Porsgrunn KÅ - Date: 2003-11-04 - Page: 3
L
H2 Generator System step 1 & 2
Air
H2 membrane H2 membrane
1 N2+H2O 3
Air (Sweep) N2+H2O+H2
Q Q CC
CH4 / Residual
H2O Gas H2 H2 Syngas
H2 H2
4 Air/H2O
2
1 ½ O2+H2 = H2O 3 Sweep
2 CH4+H2O = CO+3H2 4
CH4+H2O = CO+3H2
CO +H2O = CO2+H2 CO +H2O = CO2+H2
EPI
Porsgrunn KÅ - Date: 2003-11-04 - Page: 4
L
H2 Membrane Reformer - Power Plant
EPI
Porsgrunn KÅ - Date: 2003-11-04 - Page: 5
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