Study of coke behaviour of catalyst during methanol-to-olefins process based on a special TGA reactor

Chemical Engineering Journal

Volumn 160, Issue 2, 2010, Pages 770-778

  Hu, Hao ^a   Cao, Fahai ^a   Ying, Weiyong ^a   Sun, Qiwen ^b   Fang, Dingye ^a  

^a EAST CHINA UNIVERSITY OF SCIENCE AND TECHNOLOGY   (China)

^b State Key Laboratory of Coal Liquefaction and Coal Chemical Technology   (China)

Author keywords

Coke deposition; Coking model; Methanol to olefins; SAPO 34; TGA reactor

Indexed keywords

COKE DEPOSITION; COKE FORMATION; DEACTIVATION PHENOMENA; EFFECT OF TEMPERATURE; FIXED-BED REACTORS; IN-SITU; KINETIC MODELING; MATHEMATICAL EXPRESSIONS; METHANOL CONCENTRATION; METHANOL TO OLEFIN; MTO PROCESS; PRODUCT DISTRIBUTIONS; REACTION CONDITIONS; REACTION TEMPERATURE; SAPO-34; WEIGHT CHANGE;

CATALYST ACTIVITY; CHEMICAL REACTORS; COKE; GRAVIMETRIC ANALYSIS; METHANOL; OLEFINS;

ATMOSPHERIC TEMPERATURE;

EID: 77955155666     PISSN: 13858947     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cej.2010.04.017     Document Type: Article

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