Effect of feed nozzle configuration on n-butane to maleic anhydride yield: From lab scale to commercial

Applied Catalysis A: General

Volumn 376, Issue 1, 2010, Pages 83-90

  Shekari, Ali ^b   Patience, Gregory S ^b   Bockrath, Richard E ^a  

^a DUPONT COMPANY   (United States)

^b ÉCOLE POLYTECHNIQUE DE MONTRÉAL   (Canada)

Author keywords

Circulating fluidized bed; Fluidized bed; Maleic anhydride; n Butane partial oxidation; Oxygen sparger; Vanadyl pyrophosphate

Indexed keywords

CIRCULATING FLUIDIZED BED; CIRCULATING FLUIDIZED BED REACTOR; FEED GAS; FEED NOZZLES; LABORATORY SCALE; MALEIC ACIDS; N-BUTANE; N-BUTANE CONVERSION; PARTIAL OXIDATIONS; VANADYL PYROPHOSPHATE;

BUTANE; CATALYST SELECTIVITY; CHEMICAL REACTORS; FLUID CATALYTIC CRACKING; FLUIDIZED BED PROCESS; FLUIDIZED BEDS; LIQUEFIED PETROLEUM GAS; MALEIC ANHYDRIDE; OXIDATION; OXYGEN; VANADIUM COMPOUNDS;

FLUIDIZATION;

EID: 77649325478     PISSN: 0926860X     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.apcata.2009.11.033     Document Type: Article

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