Pure hydrogen co-production by membrane technology in an IGCC power plant with carbon capture.

Abstract The CO 2 capture in Integrated Gasification Combined Cycle (IGCC) plants causes a significant increase of the cost of electricity (COE) and thus determines high CO 2 mitigation cost (cost per ton of avoided CO 2 emissions). In this work the economic sustainability of the co-production of pure hydrogen in addition to the electricity production was assessed by detailed process simulations and a techno-economic analysis. To produce pure hydrogen a Water Gas Shift reactor and a Selexol® process was combined with H 2 selective palladium membranes. This innovative process section was compared with the more conventional Pressure Swing Adsorption in order to produce amount of pure hydrogen up to 20% of the total hydrogen available in the syngas. Assuming for a base case a hydrogen selling price of 3 €/kg and a palladium membrane cost of 9200 €/m2, a cost of electricity (COE) of 64 €/MWh and a mitigation cost of 20 €/ton CO2 were obtained for 90% captured CO 2 and 10% hydrogen recovery. An increase of the hydrogen recovery up to 20% determines a reduction of the COE and of the mitigation cost to 50 €/MWh and 5 €/ton CO2 , respectively. A sensitivity analysis showed that even a 50% increase of cost of the membrane per unit surface could determine a COE increase of only about 10% and a maximum increase of the mitigation cost of further 5 €/ton CO2. Graphical abstract Image 1 Highlights • H 2 coproduction makes the CO 2 capture economically viable in IGCC plants. • WGS, H 2 selective Pd membranes and CO 2 capture with Selexol® process are combined. • H 2 purification by selective Pd membranes and by PSA are compared. • Recovery of 20% of total H 2 allows 90% CO 2 capture at a cost of 5 EUR/ton CO2. • 50% increase of the membrane cost causes about 10% increase of the Cost of Energy. [ABSTRACT FROM AUTHOR]