Study of catalytic behaviour and deactivation of vanadyl-aluminum binary phosphates in selective oxidation of o-xylene

被引:11
作者
Bautista, F. M. [1 ]
Campelo, J. M. [1 ]
Luna, D. [1 ]
Luque, J. [1 ]
Marinas, J. M. [1 ]
Siles, M. T. [1 ]
机构
[1] Univ Cordoba, Dept Quim Organ, E-14014 Cordoba, Spain
关键词
vanadyl-aluminum binary phosphates; o-xylene selective oxidation; catalyst deactivation; H-2-TPR;
D O I
10.1016/j.cej.2006.03.020
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study involved the catalytic behaviour and the deactivation of aluminum-vanadium-phosphorus (Al-V-P-O) systems obtained by the sol-gel method with several P/Al/V molar ratios and calcined at 450 degrees C in the selective oxidation of o-xylene. Activity values as well as the reducibility of Al-V-P-O systems were influenced by the Al/V ratio, increasing with Al content, while selectivity to phthalic anhydride and phthalide values only changed slightly. All catalysts always showed a high degree of resistance to deactivation in function of time on-stream. Furthermore. water in the feed or coke generation treatment negatively affected catalytic activity, although the initial conversion values were recovered. This fact along with the unchanged textural properties and XRD patterns of the catalysts after such treatments suggest that reversible deactivation could be attributed to partial poisoning of active sites. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:3 / 9
页数:7
相关论文
共 23 条
[1]   Vanadium phosphorus oxides for n-butane oxidation to maleic anhydride [J].
Abon, M ;
Volta, JC .
APPLIED CATALYSIS A-GENERAL, 1997, 157 (1-2) :173-193
[2]   Deactivation of an industrial V2O5-TiO2 catalyst for oxidation of o-xylene into phthalic anhydride [J].
Anastasov, AI .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2003, 42 (06) :449-460
[3]   Vanadyl-aluminum binary phosphate:: Al/V ratio influence on their structure and catalytic behavior in the 2-propanol conversion [J].
Bautista, FM ;
Campelo, JM ;
García, A ;
Luna, D ;
Marinas, JM ;
Romero, AA ;
Siles, MT .
CATALYSIS TODAY, 2003, 78 (1-4) :269-280
[4]  
BAUTISTA FM, 1994, STUD SURF SCI CATAL, V82, P759
[5]   KINETICS AND MECHANISM OF CATALYTIC OXYDEHYDROGENATION OF ALKYLBENZENES [J].
BAUTISTA, FM ;
CAMPELO, JM ;
GARCIA, A ;
LUNA, D ;
MARINAS, JM .
JOURNAL OF CATALYSIS, 1989, 116 (02) :338-349
[6]   1-BUTANOL DEHYDRATION ON ALPO4 AND MODIFIED ALPO4 - CATALYTIC BEHAVIOR AND DEACTIVATION [J].
BAUTISTA, FM ;
DELMON, B .
APPLIED CATALYSIS A-GENERAL, 1995, 130 (01) :47-65
[7]   ORIGINS AND OBJECTIVES [J].
BOND, GC ;
VEDRINE, JC .
CATALYSIS TODAY, 1994, 20 (01) :1-6
[8]   INFLUENCE OF THE STARTING ALUMINUM SALT ON THE SURFACE AND ACID PROPERTIES OF ALPO4 CATALYSTS PRECIPITATED WITH AMMONIUM HYDROXIDE [J].
CAMPELO, JM ;
GARCIA, A ;
LUNA, D ;
MARINAS, JM .
JOURNAL OF CATALYSIS, 1988, 111 (01) :106-119
[9]   The characterization of the surface properties of V-P-O-based catalysts by probe molecules [J].
Cavani, F ;
Trifiro, F .
APPLIED CATALYSIS A-GENERAL, 1997, 157 (1-2) :195-221
[10]   ACIDITY AND CATALYTIC BEHAVIOR OF VANADIUM PHOSPHORUS OXYGEN CATALYSTS [J].
CORNAGLIA, LM ;
LOMBARDO, EA ;
ANDERSON, JA ;
FIERRO, JLG .
APPLIED CATALYSIS A-GENERAL, 1993, 100 (01) :37-50