Wet air oxidation of phenol using active carbon as catalyst

被引:155
作者
Fortuny, A
Font, J
Fabregat, A
机构
[1] Univ Politecn Catalunya, EUPVG, Dept Enginyeria Quim, Vilanova I La Geltru 08800, Barcelona, Spain
[2] Univ Rovira & Virgili, ETSEQ, Dept Enginyeria Quim, Tarragona, Catalunya, Spain
关键词
phenol; waste water; oxidation catalyst; carbon (active); trickle bed;
D O I
10.1016/S0926-3373(98)00072-1
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
Catalytic wet air oxidation is a promising alternative for the treatment of phenolic waste water which cannot be treated in conventional sewage plants. Catalytic wet air oxidation of an aqueous phenol solution was conducted in a fixed bed reactor operating in trickle flow regime. Either active carbon or a commercial copper oxide supported over gamma-alumina was used as catalyst. The performance of both materials was compared in terms of phenol conversion in 240 h tests. The results showed that the active carbon, without any active metal supported, gives the highest phenol conversion. The supported copper catalyst undergoes a rapid deactivation due to the dissolution of the metal active species in the acidic medium in which the reaction takes place. On the other hand, the active carbon maintains a higher activity throughout the test, although a decrease of the phenol conversion was also observed due to both the loss of active carbon by combustion and the reduction of its surface area. The phenol oxidation was proved to occur through a first order mechanism with respect to phenol. After the ten-day run, the catalytic activity of the active carbon was found to be about eight times higher than that of the commercial catalyst, also showing high selectivity to the production of carbon dioxide. (C) 1998 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:165 / 173
页数:9
相关论文
共 32 条
[1]   DISSOLVED-OXYGEN EFFECTS ON EQUILIBRIUM AND KINETICS OF PHENOLICS ADSORPTION BY ACTIVATED CARBON [J].
ABUZAID, NS ;
NAKHLA, GF .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1994, 28 (02) :216-221
[2]   Characterisation of copper catalysts and activity for the oxidation of phenol aqueous solutions [J].
Alejandre, A ;
Medina, F ;
Fortuny, A ;
Salagre, P ;
Sueiras, JE .
APPLIED CATALYSIS B-ENVIRONMENTAL, 1998, 16 (01) :53-67
[3]  
BIRBARA PJ, 1994, Patent No. 5362405
[4]   REGENERATION OF AN ACTIVATED CARBON BED EXHAUSTED BY INDUSTRIAL PHENOLIC WASTE-WATER [J].
CAMPORRO, A ;
CAMPORRO, MJ ;
COCA, J ;
SASTRE, H .
JOURNAL OF HAZARDOUS MATERIALS, 1994, 37 (01) :207-214
[5]   ACTIVATED CARBON CATALYZES REACTIONS OF PHENOLICS DURING LIQUID-PHASE ADSORPTION [J].
COONEY, DO ;
XI, ZP .
AICHE JOURNAL, 1994, 40 (02) :361-364
[6]   CARBON AS ADSORBENT AND CATALYST [J].
COUGHLIN, RW .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1969, 8 (01) :12-&
[7]  
DING J, 1987, J WATER POLLUT CON F, V59, P139
[8]   CATALYTIC REMOVAL OF PHENOL FROM AQUEOUS-PHASE USING OXYGEN OR AIR AS OXIDANT [J].
FORTUNY, A ;
FERRER, C ;
BENGOA, C ;
FONT, J ;
FABREGAT, A .
CATALYSIS TODAY, 1995, 24 (1-2) :79-83
[9]  
FORTUNY A, 1996, P 7 MED C CHEM ENG O, P291
[10]   TRICKLE-BED REACTORS - STATE OF ART AND PERSPECTIVES [J].
GIANETTO, A ;
SPECCHIA, V .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (13-14) :3197-3213