Structure and basicity of γ-Al2O3-supported MgO and its application to mercaptan oxidation

被引:69
作者
Jiang, DE
Zhao, BY [1 ]
Xie, YC
Pan, GC
Ran, GP
Min, EZ
机构
[1] Beijing Univ, Inst Phys Chem, Beijing 100871, Peoples R China
[2] SINOPEC, RIPP, Beijing 100083, Peoples R China
基金
中国国家自然科学基金;
关键词
monolayer dispersion; MgO/gamma-Al2O3; mercaptan oxidation; solid base; hydrotalcite;
D O I
10.1016/S0926-860X(01)00660-3
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
gamma -Al2O3-supported MgO samples with different MgO loading have been prepared by impregnating gamma -Al2O3 with magnesium nitrate solution and then calcining at 773 K. Resultant MgO/Al2O3 samples have been characterized with XRD, CO2-TPD, XPS, surface area and pore size distribution measurements, and compared with hydrotalcite-derived Mg-Al mixed oxide (Mg(Al)O) samples. Results show that the utmost dispersion capacity (threshold) of MgO on gamma -Al2O3 is 0.17 gMgO/gAl(2)O(3); the base amount of MgO/gamma -Al2O3 increases with MgO loading and reaches a maximum at the threshold loading; the base strength of MgO/gamma -Al2O3 with the threshold loading ((Mg/Al)O) is similar to that of Mg(Al)O (Mg/Al = 3), but its base site density is almost twice as much as that of Mg(Al)O; the pore size distributions of (Mg/Al)O and Mg(Al)O are quite different from each other. The pore size of (Mg/Al)O concentrates on a relatively narrow meso-pore range (between 30 and 60 A). When treating the real jet fuel, the catalyst of (Mg/Al)O-supported CoPcS shows a little higher conversion and much longer lifetime than Mg(Al)O-supported CoPcS. The former's lifetime is almost three times as long as the latter's and reaches over 800 h. The better performance of MgO/gamma -Al2O3 is attributed to its proper pore size distribution and to more basic sites being available. (C) 2001 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:69 / 78
页数:10
相关论文
共 44 条
[1]   Solid base catalysts for mercaptan oxidation [J].
Alcaraz, JJ ;
Arena, BJ ;
Gillespie, RD ;
Holmgren, JS .
CATALYSIS TODAY, 1998, 43 (1-2) :89-99
[2]  
Ansquer P., 1995, US, Patent No. [5,382,354, 5382354]
[3]   MEROX AND RELATED METAL PHTHALOCYANINE CATALYZED OXIDATION PROCESSES [J].
BASU, B ;
SATAPATHY, S ;
BHATNAGAR, AK .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1993, 35 (04) :571-609
[4]   Hydrotalcite decomposition mechanism: A clue to the structure and reactivity of spinel-like mixed oxides [J].
Bellotto, M ;
Rebours, B ;
Clause, O ;
Lynch, J ;
Bazin, D ;
Elkaim, E .
JOURNAL OF PHYSICAL CHEMISTRY, 1996, 100 (20) :8535-8542
[5]  
BROUWER WM, 1985, J MOL CATAL, V29, P335
[6]   HYDROTALCITE-CATALYZED ALKYLATION OF 2,4-PENTANEDIONE [J].
CATIVIELA, C ;
FIGUERAS, F ;
GARCIA, JI ;
MAYORAL, JA ;
ZURBANO, MM .
SYNTHETIC COMMUNICATIONS, 1995, 25 (11) :1745-1750
[7]   HYDROTALCITE-TYPE ANIONIC CLAYS: PREPARATION, PROPERTIES AND APPLICATIONS [J].
Cavani, F. ;
Trifiro, F. ;
Vaccari, A. .
CATALYSIS TODAY, 1991, 11 (02) :173-301
[8]   CALCINED MGALCO3-HT CATALYZED CYANOSILYLATION OF CARBONYL-COMPOUNDS AND NUCLEOPHILIC RING-OPENING OF OXIRANES USING TMSCN(+) [J].
CHOUDARY, BM ;
NARENDER, N ;
BHUMA, V .
SYNTHETIC COMMUNICATIONS, 1995, 25 (18) :2829-2836
[9]  
CHRISTIAN M, 1993, Patent No. 2688223
[10]   BASE CATALYSIS FOR FINE CHEMICALS PRODUCTION - CLAISEN-SCHMIDT CONDENSATION ON ZEOLITES AND HYDROTALCITES FOR THE PRODUCTION OF CHALCONES AND FLAVANONES OF PHARMACEUTICAL INTEREST [J].
CLIMENT, MJ ;
CORMA, A ;
IBORRA, S ;
PRIMO, J .
JOURNAL OF CATALYSIS, 1995, 151 (01) :60-66