Hydrogen production from simulated hot coke oven gas by catalytic reforming over Ni/Mg(Al)O catalysts

Journal of Natural Gas Chemistry

Volumn 18, Issue 2, 2009, Pages 225-231

  Cheng, Hongwei ^a   Yue, Baohua ^a   Wang, Xueguang ^a   Lu, Xionggang ^a   Ding, Weizhong ^a  

^a SHANGHAI UNIVERSITY   (China)

Author keywords

coke oven gas; hydrogen production; hydrotalcite; tar; toluene

Indexed keywords

CATALYTIC ACTIVITY; CATALYTIC REFORMING; COKE OVEN GAS; EFFLUENT GAS; FIXED BED REACTOR; HOMOGENEOUS PRECIPITATION METHOD; HYDROTALCITE; HYDROTALCITE-TYPE PRECURSOR; MODEL TAR; MOLAR RATIO; REDUCTION TEMPERATURES; SOLUTION STRUCTURES; TEM; UREA HYDROLYSIS; XRD;

ALUMINUM; ATMOSPHERIC PRESSURE; CALCINATION; CATALYSIS; CATALYST ACTIVITY; COKE; COKE OVENS; GAS PRODUCERS; GASES; NICKEL; NICKEL COMPOUNDS; OVENS; STOVES; TAR; TOLUENE; UREA; X RAY DIFFRACTION; X RAY DIFFRACTION ANALYSIS;

HYDROGEN PRODUCTION;

EID: 67649577462     PISSN: 10039953     EISSN: None     Source Type: Journal    
DOI: 10.1016/S1003-9953(08)60104-8     Document Type: Article

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