ROLE OF ZSM-5 AND ULTRASTABLE Y-ZEOLITES FOR INCREASING GASOLINE OCTANE NUMBER

被引:61
|
作者
MADON, RJ
机构
[1] Engelhard Corporation, Menlo Park, Edison, NJ 08818
关键词
D O I
10.1016/0021-9517(91)90030-8
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
Octane number of gasoline made in a fluid catalytic cracker can be catalytically enhanced by using an ultrastable HY zeolite instead of one containing rare earth cations or by adding small amounts of ZSM-5 to a Y zeolite catalyst. ZSM-5 addition catalyzes both normal and branched olefin cracking to give mainly propylene, butenes, 2-methyl 1-butene, and 2-methyl 2-butene. Increase in octane number is mainly due to an increase in yields of CS hydrocarbons, an increase in aromatic concentration, and a decrease in yields of C7+ paraffins and straight olefins. The decrease in paraffin yield is due to the removal of olefins which would otherwise undergo secondary hydrogen addition. The USY zeolite gives a lighter gasoline with higher yields of C5 and C6 branched olefins than the REY zeolite which gives higher yields of C7+ branched paraffins. However, the USY catalyst, unlike the ZSM-5 addition case, does not decrease the yields of C7+ olefins. Reaction pathways that affect gasoline composition are different, for the two cases; yet, in both cases, increases in C5 hydrocarbons and decreases in C7+ paraffins contribute significantly to the increase in octane number. © 1991.
引用
收藏
页码:275 / 287
页数:13
相关论文
共 50 条
  • [31] Adsorption properties of ZSM-5 zeolites
    Hudec, P
    Smieskova, A
    Zidek, Z
    Zubek, M
    Schneider, P
    Kocirik, M
    Kozankova, J
    COLLECTION OF CZECHOSLOVAK CHEMICAL COMMUNICATIONS, 1998, 63 (02) : 141 - 154
  • [32] SHAPE SELECTIVITY OF ZEOLITES ZSM-5
    BERAK, JM
    KANIK, B
    CZERWINSKA, B
    MOSTOWICZ, R
    PRZEMYSL CHEMICZNY, 1980, 59 (10): : 536 - 538
  • [33] DIFFUSION OF CYCLOHEXANES IN ZSM-5 ZEOLITES
    CHON, H
    PARK, DH
    JOURNAL OF CATALYSIS, 1988, 114 (01) : 1 - 7
  • [34] Interaction of ZnO with ZSM-5 zeolites
    Rojasová, E
    Smiesková, A
    Hudec, P
    Zidek, Z
    COLLECTION OF CZECHOSLOVAK CHEMICAL COMMUNICATIONS, 2000, 65 (09) : 1506 - 1514
  • [35] DEALUMINATION OF ZSM-5 ZEOLITES BY STEAMING
    SUZUKI, K
    SANO, T
    KIYOZUMI, Y
    HAGIWARA, H
    SHIN, S
    TAKAYA, H
    NIPPON KAGAKU KAISHI, 1989, (11) : 1818 - 1823
  • [36] The dynamics of ammonia sorption and n-octane hydroconversion over dealuminated ZSM-5 zeolites
    Onyestyák, G
    Valyon, J
    Rees, JVC
    SOLID STATE IONICS, 2001, 141 : 123 - 128
  • [37] Efficient Conversion of Light Cycle Oil into High-Octane-Number Gasoline and Light Olefins over a Mesoporous ZSM-5 Catalyst
    Xin, Li
    Liu, Xinxin
    Chen, Xiaobo
    Feng, Xiang
    Liu, Yibin
    Yang, Chaohe
    ENERGY & FUELS, 2017, 31 (07) : 6968 - 6976
  • [38] MOLECULAR SHAPE SELECTIVITY OF ZSM-5, MODIFIED ZSM-5 AND ZSM-11 TYPE ZEOLITES
    DEROUANE, EG
    DEJAIFVE, P
    GABELICA, Z
    VEDRINE, JC
    FARADAY DISCUSSIONS, 1981, 72 : 331 - 344
  • [39] Physicochemical and catalytic properties of ZSM-5/Y composite zeolites dealuminated by the steaming
    Chen, HL
    Shen, BJ
    Pan, HF
    ACTA PHYSICO-CHIMICA SINICA, 2004, 20 (08) : 854 - 859
  • [40] Monomolecular cracking of n-hexane on Y, MOR, and ZSM-5 zeolites
    Department of Chemical Engineering, Northwestern University, 2145 Sheridan Road, Evanston, IL 60208-3120, United States
    不详
    不详
    Appl Catal A Gen, 1-2 (71-86):