Reversible Liquid Carriers for an Integrated Production ...
Liquid Storage Tank LQ*H 2 ∆∆ LQ* LQ*H 2 + heat (∆H) LQ* + H 2 P > 50 atm. P < 10 atm. Catalyst Catalyst Maximum overall energy efficiency; by (a) Recovering heat from the hydrogenation exotherm (-∆H) and (b) utilizing the FC’s waste heat to drive the endothermic (∆H) dehydrogenation. ................
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