Catalytic cracking of Arabian Light VGO over novel zeolites as FCC catalyst additives for maximizing propylene yield

被引:74
作者
Hussain, A. I. [1 ,3 ]
Aitani, A. M. [1 ]
Kubu, Martin [2 ]
Cejka, Jiri [1 ,2 ]
Al-Khattaf, S. [1 ,3 ]
机构
[1] King Fahd Univ Petr & Minerals, Ctr Res Excellence Petr Refining & Petrochem, Dhahran 31261, Saudi Arabia
[2] Acad Sci Czech Republ, J Heyrovsky Inst Phys Chem, Vvi, CZ-18223 Prague 8, Czech Republic
[3] King Fahd Univ Petr & Minerals, Dept Chem Engn, Dhahran 31261, Saudi Arabia
关键词
Catalytic cracking; FCC additives; 10-ring zeolites; MCM-36; Propylene; Light olefins; GAS OIL; KINETIC-MODEL; SELECTIVE CATALYST; OLEFINS PRODUCTION; ZSM-5; ADDITION; PORE TOPOLOGY; TEMPERATURE; NAPHTHA; IM-5; DEACTIVATION;
D O I
10.1016/j.fuel.2015.11.065
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Catalytic cracking of vacuum gas oil (VGO) was carried out in a microactivity test (MAT) unit. Commercial FCC USY catalyst (E-Cat) is used and modified by various zeolites with different pore structures, namely SSZ-74, SSZ-33, MCM-22, MCM-36, ZSM-5, TNU-9, IM-5, and ferrierite to enhance propylene yield. Adding zeolite additives to E-Cat increased catalyst activity. The highest propylene yield of similar to 11 wt.% was achieved over ferrierite and MCM-36 compared with 7 wt.% over E-Cat. An increase in light olefins yield over all additives was associated with a decrease in gasoline yield due to the cracking of gasoline-range reactive species (mainly olefins and iso-paraffins). Zeolite SSZ-74 showed a good enhancement in light olefins yield up to 21.3 wt.% compared with 16.1 wt.% over E-Cat. It is found that additives with lower ability to carry bimolecular reactions are more selective to light olefins. Gasoline quality was improved as the octane number increased over E-Cat with all additives except MCM-36. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:226 / 239
页数:14
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