Characterization of modified nanoscale ZSM-5 zeolite and its application in the olefins reduction in FCC gasoline

被引:1
作者
Zhang, PQ
Wang, XS
Guo, XW [1 ]
Guo, HC
Zhao, LP
Hu, YK
机构
[1] Dalian Univ Technol, Dept Catalysis Chem & Engn, State Key Lab Fine Chem, Dalian 116012, Peoples R China
[2] Fushun Petr & Petrochem, Res Inst, Fushun 130001, Peoples R China
关键词
nanoscale HZSM-5 zeolite; hydrothermal treatment; ammonia; modification; fluidized catalytic cracking gasoline; olefins reduction; lanthanum; nickel;
D O I
10.1023/B:CATL.0000011089.56057.02
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
Nanoscale HZSM-5 zeolite was hydrothermally treated with steam containing 0.8 wt% NH3 at 773 K and then loaded with La2O3 and NiO. Both the parent nanoscale HZSM-5 and the modified nanoscale HZSM-5 zeolites catalysts were characterized by TEM, XRD, IR, NH3-TPD and XRF, and then the performance of olefins reduction in fluidized catalytic cracking (FCC) gasoline over the modified nanoscale HZSM-5 zeolite catalyst was investigated. The IR and NH3-TPD results showed that the amount of acids of the parent nanoscale HZSM-5 zeolite decreased after the combined modification, so did the strong acid sites deactivating catalysts. The stability of the catalyst was still satisfactory, though the initial activity decreased a little after the combined modification. The modification reduced the ability of aromatization of nanoscale HZSM-5 zeolite catalyst and increased its isomerization ability. After 300 h onstream, the average olefins content in the gasoline was reduced from 56.3 vol% to about 20 vol%, the aromatics (C-7 - C-9 aromatics mainly) and paraffins contents in the product were increased from 11.6 vol% and 32.1 vol% to about 20 vol% and 60 vol% respectively. The ratio of i-paraffins/n-paraffins also increased from 3.2 to 6.6. The yield of gasoline was obtained at 97 wt%, while the Research Octane Number ( RON) remained about 90.
引用
收藏
页码:63 / 68
页数:6
相关论文
共 24 条
[1]  
ANTONIO D, 1997, APPL CATAL A-GEN, V154, P221
[2]   RECENT PROCESS-RELATED AND CATALYST-RELATED DEVELOPMENTS IN FLUID CATALYTIC CRACKING [J].
BISWAS, J ;
MAXWELL, IE .
APPLIED CATALYSIS, 1990, 63 (02) :197-258
[3]   Characterization of nanocrystalline zeolite Beta [J].
Camblor, MA ;
Corma, A ;
Valencia, S .
MICROPOROUS AND MESOPOROUS MATERIALS, 1998, 25 (1-3) :59-74
[4]  
DAVISON G, 1999, SUPPLEMENT CATALYST
[5]   HIGH-RESOLUTION SI-29 NMR OF DEALUMINATED Y-ZEOLITES .1. THE DEPENDENCE OF THE EXTENT OF DEALUMINATION ON THE DEGREE OF AMMONIUM EXCHANGE AND THE TEMPERATURE AND WATER-VAPOR PRESSURE OF THE THERMOCHEMICAL TREATMENT [J].
ENGELHARDT, G ;
LOHSE, U ;
PATZELOVA, V ;
MAGI, M ;
LIPPMAA, E .
ZEOLITES, 1983, 3 (03) :233-238
[6]  
HUANG F, 2001, PETROL REFINERY ENG, V31, P36
[7]  
Lago R.M., 1986, P 7 INT ZEOL C, P677
[8]   CONVERSION OF ETHANOL IN AQUEOUS-SOLUTION OVER ZSM-5 ZEOLITES - INFLUENCE OF REACTION PARAMETERS AND CATALYST ACIDIC PROPERTIES AS STUDIED BY AMMONIA TPD TECHNIQUE [J].
LEVANMAO, R ;
NGUYEN, TM ;
YAO, J .
APPLIED CATALYSIS, 1990, 61 (01) :161-173
[9]   Rare earth-modified bifunctional Ni/HY catalysts [J].
Li, D ;
Li, F ;
Ren, J ;
Sun, YH .
APPLIED CATALYSIS A-GENERAL, 2003, 241 (1-2) :15-24
[10]   BREAKING C-S BONDS WITH TRANSITION-METAL COMPLEXES - A REVIEW OF MOLECULAR APPROACHES TO THE STUDY OF THE MECHANISMS OF THE HYDRODESULFURIZATION REACTION [J].
SANCHEZDELGADO, RA .
JOURNAL OF MOLECULAR CATALYSIS, 1994, 86 (1-3) :287-307