Production of middle distillate from synthesis gas in a dual-bed reactor through hydrocracking of wax over mesoporous Pd-Al2O3 composite catalyst

Catalysis Letters

Volumn 130, Issue 1-2, 2009, Pages 192-197

  Nam, Insung ^a   Cho, Kyung Min ^a   Seo, Jeong Gil ^a   Hwang, Sunhwan ^a   Jun, Ki Won ^b   Song, In Kyu ^a  

^a Seoul National University   (South Korea)

^b Korea Research Institute of Chemical Technology   (South Korea)

Author keywords

Fischer Tropsch synthesis; Hydrocracking of wax; Mesoporous Pd Al2O3 catalyst; Middle distillate

Indexed keywords

ALUMINA COMPOSITES; BED REACTORS; CATALYTIC PERFORMANCE; COMPOSITE CATALYSTS; DUAL-BED REACTOR; EFFICIENT CATALYSTS; MESOPOROUS; MESOPOROUS ALUMINA; MESOPOROUS PD-AL2O3 CATALYST; MIDDLE DISTILLATE; MIDDLE DISTILLATES; PD CATALYST; SURFACE AREA;

ALUMINUM; CARBON MONOXIDE; CATALYST ACTIVITY; COMPLEXATION; CRACKING (CHEMICAL); FISCHER-TROPSCH SYNTHESIS; HIGH PRESSURE EFFECTS; HYDROCRACKING; PALLADIUM; SYNTHESIS GAS;

CATALYST SELECTIVITY;

EID: 65849176573     PISSN: 1011372X     EISSN: 1572879X     Source Type: Journal    
DOI: 10.1007/s10562-009-9854-9     Document Type: Article

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