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Title: Fluid catalytic cracking catalyst for reformulated gasolines: Kinetic modeling

Conference · · Industrial and Engineering Chemistry Research; (United States)
OSTI ID:6627077
 [1];  [2];  [3];  [4]
  1. EniChem, Baytown, TX (United States)
  2. Norwegian Inst. of Technology, Trondheim (Norway). Dept. of Chemical Engineering
  3. Univ. de La Patagonia, Chubut (Argentina). Dept. de Procesos
  4. Univ. of Western Ontario, London, Ontario (Canada). Faculty of Engineering Science

Changes of the relative importance of intradiffusion on USY zeolite crystals were studied as a way of affecting selectivity of catalytic cracking reactions. Zeolite crystals were synthesized (Si/Al = 2.4), activated and stabilized using ion exchange and steam calcination to obtain USSY (Ultra Stable Submicron Y) zeolites. After the activation the zeolites were pelletized (45--60 [mu]m particles). USSYs were tested in a novel Riser Simulator. Results obtained show that total aromatics (BTX), benzene, C[sub 4] olefins, and coke were significantly affected with the change of zeolite crystal sizes. Gasolines produced with USSY zeolites contain less aromatics and particularly lower benzene levels. Experimental results were analyzed with a model including several lumps: unconverted gas oil, gasoline, light gases, and coke. This model also accounts for catalyst deactivation as a function of coke on catalyst. Various kinetic parameters were determined with their corresponding spans for the 95% level of confidence.

OSTI ID:
6627077
Report Number(s):
CONF-940301-; CODEN: IECRED
Journal Information:
Industrial and Engineering Chemistry Research; (United States), Vol. 33:12; Conference: 207. spring national meeting of the American Chemical Society (ACS), San Diego, CA (United States), 13-18 Mar 1994; ISSN 0888-5885
Country of Publication:
United States
Language:
English