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CRACKING ACTIVITY OF PREPARED Y-ZEOLITE CATALYST USING CUMENE ON FLUIDIZED BED REACTOR

Iraqi Journal of Chemical and Petroleum Engineering

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Field Value
 
Title CRACKING ACTIVITY OF PREPARED Y-ZEOLITE CATALYST USING CUMENE ON FLUIDIZED BED REACTOR
 
Creator A.K. Mohammed, Abdul Halim
Ghassan Yousuf, Rawa
Khalifa Esgair, Karim
 
Description The catalytic activity of faujasite type NaY catalysts prepared from local clay (kaolin) with different Si/Al ratio was studied using cumene cracking as a model for catalytic cracking process in the temperature range of 450-525° C, weight hourly space velocity (WHSV) of 5-20 h1, particle size ≤75μm and atmospheric pressure. The catalytic activity was investigated using experimental laboratory plant scale of fluidized bed reactor.It was found that the cumene conversion increases with increasing temperature and decreasing WHSV. At 525° C and WHSV 5 h-1, the conversion was 42.36 and 35.43 mol% for catalyst with 3.54 Si/Al ratio and Catalyst with 5.75 Si/Al ratio, respectively, while at 450° C and at the same WHSV, the conversion was decreased to 29.15 and 21.86 mol% respectively, and the catalyst of 5.75 Si/Al ratio gave the higher cumene activity than the catalyst with 3.54 Si/Al ratio.
 
Publisher University of Baghdad/ College of Engineering
 
Date 2011-06-30
 
Type info:eu-repo/semantics/article
info:eu-repo/semantics/publishedVersion
 
Format application/pdf
 
Identifier http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/350
 
Source Iraqi Journal of Chemical and Petroleum Engineering; Vol 12 No 2 (2011): Iraqi Journal of Chemical and Petroleum Engineering; 9-17
المجلة العراقية للهندسة الكيمياوية وهندسة النفط; مجلد 12 عدد 2 (2011): Iraqi Journal of Chemical and Petroleum Engineering; 9-17
2618-0707
1997-4884
 
Language eng
 
Relation http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/350/351