An innovative, efficient and large hydrogen liquefier is described. Innovations lie in the fact (i) the feed, 10 kg/s, is refrigerated in heat exchangers catalytically promoting the ortho-para conversion (ii) down to the low temperature of 20.5 K and at the high pressure of 60 bar at which it is available and (iii) lastly expanded to the storage conditions of 1.5 bar and 20 K through a liquid-phase turbomachine; (iv) refrigeration is via four helium recuperative Joule-Brayton cycles arranged so that the refrigerant follows the cooling curve of hydrogen and the volume flow rates in compression and expansion processes are typical of axial-flow high-efficiency turbomachines; (v) compression is accomplished in 15 intercooled 8-stage devices derived from gas turbine technology. Heat exchangers require specific surfaces comparable to current state-of-the-art liquefiers. Nevertheless, the predicted work of approximately 18 MJ/kg is half as much the requirement of those liquefiers and corresponds to a second-law efficiency of almost 48%.

PROPOSAL OF AN INNOVATIVE, HIGHLY-EFFICIENT, LARGE-SCALE HYDROGEN LIQUEFIER

VALENTI, GIANLUCA;MACCHI, ENNIO
2008-01-01

Abstract

An innovative, efficient and large hydrogen liquefier is described. Innovations lie in the fact (i) the feed, 10 kg/s, is refrigerated in heat exchangers catalytically promoting the ortho-para conversion (ii) down to the low temperature of 20.5 K and at the high pressure of 60 bar at which it is available and (iii) lastly expanded to the storage conditions of 1.5 bar and 20 K through a liquid-phase turbomachine; (iv) refrigeration is via four helium recuperative Joule-Brayton cycles arranged so that the refrigerant follows the cooling curve of hydrogen and the volume flow rates in compression and expansion processes are typical of axial-flow high-efficiency turbomachines; (v) compression is accomplished in 15 intercooled 8-stage devices derived from gas turbine technology. Heat exchangers require specific surfaces comparable to current state-of-the-art liquefiers. Nevertheless, the predicted work of approximately 18 MJ/kg is half as much the requirement of those liquefiers and corresponds to a second-law efficiency of almost 48%.
2008
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11311/525338
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