OCTANE ENHANCEMENT IN FLUID CATALYTIC CRACKING .1. ROLE OF ZSM-5 ADDITION AND REACTOR TEMPERATURE

被引:74
作者
BISWAS, J [1 ]
MAXWELL, IE [1 ]
机构
[1] SHELL INT RES MAATSCHAPPIJ BV, KONINKLIJKE SHELL LAB, BADHUISWEG 3, 1031 CM AMSTERDAM, NETHERLANDS
来源
APPLIED CATALYSIS | 1990年 / 58卷 / 01期
关键词
D O I
10.1016/S0166-9834(00)82274-5
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Addition of ZSM-5 to an ultra-stabilized fluid catalytic cracking (FCC) catalyst leads to significant losses in gasoline yield, the gasoline being cracked preferentially to propylene, iso-butane and butylene. The octane boost resulting from ZSM-5 addition is due to an increase in gasoline aromatics concentration as well as a decrease in molecular weight. Rather than being due to a particular reaction mechanism, the increase in aromatics concentration is in essence a concentration effect resulting from preferential removal of the non-cyclic gasoline components through cracking. No increase in gasoline component branching is observed on ZSM-5 addition. Of particular importance is the effect of ZSM-5 addition on the octane potential of the low-octane gasoline heart-cut (b.p. 70-130°C) from the FCC unit. A boost in motor octane number (MON) is observed due to cracking of low-MON components, e.g. olefins, to gas. However, no effect on heart-cut research octane number (RON) is seen, since these olefins have a significant RON contribution. A comparative study has been made of the effects of ZSM-5 addition and operation at higher reactor temperatures on gasoline octane enhancement in fluid catalytic cracking. Higher FCC reactor temperatures give rise to higher research octane levels than ZSM-5 addition does due to the catalytic formation of gasoline aromatics and preservation of olefins; the latter are preferentially cracked out in the presence of ZSM-5. Hence, a higher gasoline yield is realized, even at high motor octane levels. One detrimental factor, however, is the increased production of dry gas. © 1990.
引用
收藏
页码:1 / 18
页数:18
相关论文
共 6 条
[1]  
AKBAR M, 1986, MAY KETJ CAT S KURH
[2]  
DWYER FG, 1987, JUN KETJ WORKSH SCHI
[3]  
HENZ HF, 1986, MAY KETJ CAT S KURH
[4]  
LIPPERT R, COMMUNICATION
[5]   SHAPE-SELECTIVE CATALYSIS AND PROCESS TECHNOLOGY VIA MOLECULAR INCLUSION IN ZEOLITES [J].
MAXWELL, IE .
JOURNAL OF INCLUSION PHENOMENA, 1986, 4 (01) :1-29
[6]  
YANIK SJ, 1985, OIL GAS J 0513, P108