Conversion of xylose and xylose-phenol mixtures to hydrogen-rich gas by supercritical water in an isothermal microtube flow reactor

Energy and Fuels

Volumn 23, Issue 7, 2009, Pages 3818-3825

  Goodwin, Aaron K ^a   Rorrer, Gregory L ^a  

^a Oregon State University   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

316 STAINLESS STEEL; APPARENT RATE CONSTANT; BIOMASS COMPONENTS; ENDOTHERMIC REFORMING REACTION; GAS YIELDS; HASTELLOY C-276; HEAT TRANSFER RATE; HIGH RATE; HYDROGEN GAS; HYDROGEN-RICH GAS; INNER DIAMETERS; ISOTHERMAL TEMPERATURE; MICRO CHANNEL REACTORS; MICROTUBE; MICROTUBE FLOWS; MODEL COMPOUND; MODELING STUDIES; PHENOL CONVERSION; PHENOL MIXTURES; PRODUCT GAS; RESIDENCE TIME; SUPERCRITICAL WATER; SUPERCRITICAL WATER GASIFICATION;

ACTIVATION ENERGY; BIOMASS; CELLULOSE; CELLULOSIC ETHANOL; ETHANOL; GASES; HEAT EXCHANGERS; HEAT TRANSFER; HYDROGEN; LIGNIN; MIXTURES; PHENOLS; POLYSULFONES; RATE CONSTANTS; REACTION KINETICS; REFORMING REACTIONS; STAINLESS STEEL; SUGAR (SUCROSE); SUGARS;

MICROCHANNELS;

ACTIVATION ENERGY; BIOMASS; CELLULOSE; ETHANOL; GAS; HEAT EXCHANGERS; HEAT TRANSFER; HYDROGEN; POLYSULFONES; REACTION KINETICS; STAINLESS STEEL; SUGAR;

EID: 67749148944     PISSN: 08870624     EISSN: None     Source Type: Journal    
DOI: 10.1021/ef900227u     Document Type: Article

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