Characterization and catalytic performance of supported molybdophosphoric acid catalysts for the oxidation of propylene to acetone

被引:24
作者
Li, MS [1 ]
Shen, JY [1 ]
Ge, X [1 ]
Chen, X [1 ]
机构
[1] Nanjing Univ, Dept Chem, Nanjing 210093, Peoples R China
基金
中国国家自然科学基金;
关键词
oxidation of propylene to acetone; H3PMo12O40/SiO2; catalyst; MoO3/gamma-Al2O3; microcalorimetric adsorption; acidity; rate-limiting step;
D O I
10.1016/S0926-860X(00)00597-4
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
The oxidation of propylene to acetone was studied over supported molybdophosphoric acid catalysts at 463 K in the presence of water. Raman spectroscopy revealed that molybdophosphoric acid retained its Keggin structure when supported on SiO2 while it decomposed to MoO3 when supported on gamma -Al2O3. Microcalorimetric adsorption of NH3 showed that the H3PMo12O40/SiO2 catalyst exhibited strong acidity (152 kJ/mol) and the MoO3/gamma -Al2O3 catalyst prepared from molybdophosphoric acid displayed fairly strong acidity (137 kJ/mol). FTIR showed that both Bronsted and Lewis acid sites were present on the surface of the two catalysts. Since the reaction can be taken as the coupling of the hydration of propylene and the oxydehydrogenation of propanol, both acid and redox sites are needed to form the active catalysts. However, the H3PMo12O40/SiO2 catalyst showed almost no activity while the MoO3/gamma -Al2O3 catalyst exhibited fairly good activity. Thus, the hydration of propylene may not be rate-limiting for the reaction on these catalysts. Microcalorimetric adsorption of propylene and acetone demonstrated that adsorption of propylene and desorption of acetone might not be rate-limiting, either. It can be concluded that the abstraction of the alpha -H of surface isopropoxy groups may be the rate-limiting step. (C) 2001 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:161 / 169
页数:9
相关论文
共 19 条
[1]  
HAN YW, 1999, THESIS NANJING U
[2]   A TIAN-CALVET HEAT-FLUX MICROCALORIMETER FOR MEASUREMENT OF DIFFERENTIAL HEATS OF ADSORPTION [J].
HANDY, BE ;
SHARMA, SB ;
SPIEWAK, BE ;
DUMESIC, JA .
MEASUREMENT SCIENCE AND TECHNOLOGY, 1993, 4 (12) :1350-1356
[3]  
KNOZINGER H, 1976, ADV CATAL, V25, P186
[4]   RECENT PROGRESS IN CATALYTIC TECHNOLOGY IN JAPAN [J].
MISONO, M ;
NOJIRI, N .
APPLIED CATALYSIS, 1990, 64 (1-2) :1-30
[5]   SURFACE PROPERTIES OF 12-MOLYBDOPHOSPHORIC ACID CATALYST [J].
MISONO, M ;
KONISHI, Y ;
FURUTA, M ;
YONEDA, Y .
CHEMISTRY LETTERS, 1978, (07) :709-712
[6]   OXIDATION OF PROPYLENE OVER CU(II)-Y MOLECULAR SIEVE UNDER HIGH STEAM CONCENTRATION [J].
MOCHIDA, I ;
HAYATA, S ;
KATO, A ;
SEIYAMA, T .
BULLETIN OF THE CHEMICAL SOCIETY OF JAPAN, 1971, 44 (08) :2282-+
[7]   ONE-STEP FORMATION OF ACETONE FROM PROPENE AND WATER ON ULTRASTABLE Y-TYPE ZEOLITE CATALYST [J].
MORI, H ;
UENO, H ;
MIZUNO, N ;
YAHIRO, H ;
IWAMOTO, M .
CHEMISTRY LETTERS, 1990, (12) :2289-2290
[8]   O-18 TRACER STUDIES OF CATALYTIC OXIDATIONS OF OLEFIN OVER TRANSITION METAL OR METAL-OXIDE CATALYSTS .19 OXIDATION OF PROPYLENE OVER SNO2-MOO3 CATALYST [J].
MOROOKA, Y ;
TAKITA, Y ;
OZAKI, A .
JOURNAL OF CATALYSIS, 1972, 27 (02) :177-&
[9]   CATALYTIC OXIDATION OF OLEFINS OVER OXIDE CATALYSTS CONTAINING MOLYBDENUM .4. CATALYSTS FOR OXIDATION OF PROPYLENE TO ACETONE [J].
MOROOKA, Y ;
TAKITA, Y ;
OZAKI, A .
JOURNAL OF CATALYSIS, 1971, 23 (02) :183-&
[10]  
Okuhara T, 1996, ADV CATAL, V41, P113, DOI 10.1016/S0360-0564(08)60041-3