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Steam Methane Reforming Design Parameters

Solsvik J, Jakobsen HA (2011) A numerical study of a two property catalyst/sorbent pellet design for the sorption-enhanced steam-methane reforming process modeling complexity and parameter sensitivity study. Chem Eng J 178 407-422... [Pg.364]

SOFC systems can be designed to include a heat recovery component such as an adsorption chiller heater for CHP applications [72-76]. An example is a small (1-lOkW) methane-fueled residential CHP SOFC system that integrates CGR, AGR, and internal reforming [73]. The system consists of a fuel-cell stack, steam prereformer, various fluid delivery devices (blowers, ejectors, compressor, and water pump), heat exchangers, and catalytic combustor and power conditioning device along with a heat recovery component. Based on certain system parameters (50active area, nominal cell temperature of 800 °G, current density of 0.57 A cm , power density of0.40-0.43 Wcm , S/G ratio of 2.0, SOFC... [Pg.997]


See other pages where Steam Methane Reforming Design Parameters is mentioned: [Pg.266]    [Pg.714]    [Pg.209]    [Pg.258]    [Pg.461]    [Pg.190]    [Pg.125]    [Pg.264]   
See also in sourсe #XX -- [ Pg.343 , Pg.344 , Pg.345 , Pg.346 , Pg.347 , Pg.348 , Pg.349 ]




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Steam methane reformation

Steam methane reformer

Steam reformation

Steam reforming

Steam-methane

Steaming methane reforming

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