Influencing mechanism of temperature on the degradation of nitrobenzene in aqueous solution by ceramic honeycomb catalytic ozonation

被引:42
作者
Zhao, Lei [1 ]
Ma, Jun [1 ,2 ]
Sun, Zhizhong [3 ]
Liu, Huiling [1 ]
机构
[1] Harbin Inst Technol, Sch Municipal & Environm Engn, Harbin 150090, Peoples R China
[2] Harbin Inst Technol, State Key Lab Urban Water Resources & Environm, Natl Engn Res Ctr Urban Water Resources, Harbin 150090, Peoples R China
[3] Heilongjiang Univ, Sch Chem & Mat Sci, Harbin 150080, Peoples R China
基金
中国博士后科学基金; 中国国家自然科学基金;
关键词
Ceramic honeycomb; Catalytic ozonation; Nitrobenzene; Temperature; Hydroxyl radical ((OH)-O-center dot); ACTIVATED CARBON; WATER-TREATMENT; DRINKING-WATER; OXALIC-ACID; OXIDATION; OZONE; MANGANESE; EFFICIENCY; KINETICS; IRON;
D O I
10.1016/j.jhazmat.2009.01.116
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The heterogeneous catalytic ozonation of nitrobenzene in aqueous solution has been carried out at different reaction temperatures in a semi-continuous batch reactor where ceramic honeycomb has been used as a catalyst. The experimental results indicated that the presence of ceramic honeycomb catalyst significantly improved the degradation efficiency of nitrobenzene compared to the results from non-catalytic ozonation, and the adsorption of nitrobenzene on the catalytic surface has no significant effect on its degradation efficiency. The degradation of nitrobenzene followed the pseudo-first-order kinetic model in both the processes of ozone alone and ozone/ceramic honeycomb. With the increase of reaction temperature from 278 K to 328 K, the degradation efficiency of nitrobenzene, the reaction rate constants, the utilization efficiency of ozone, the formation of hydroxyl radicals ((OH)-O-center dot) and the removal of total organic carbon (TOC) all increased in the process of ozone/ceramic honeycomb. The enhancement of reaction rate constant and the enhancement of (OH)-O-center dot formation exhibited a good correlation in the reaction temperature scope of 278-328 K. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:1119 / 1125
页数:7
相关论文
共 36 条
  • [1] Advanced oxidation processes (AOP) for water purification and recovery
    Andreozzi, R
    Caprio, V
    Insola, A
    Marotta, R
    [J]. CATALYSIS TODAY, 1999, 53 (01) : 51 - 59
  • [2] Andreozzi R, 2000, J CHEM TECHNOL BIOT, V75, P59, DOI 10.1002/(SICI)1097-4660(200001)75:1<59::AID-JCTB175>3.3.CO
  • [3] 2-O
  • [4] DETERMINATION OF OZONE IN WATER BY THE INDIGO METHOD
    BADER, H
    HOIGNE, J
    [J]. WATER RESEARCH, 1981, 15 (04) : 449 - 456
  • [5] Iron type catalysts for the ozonation of oxalic acid in water
    Beltrán, FJ
    Rivas, FJ
    Montero-de-Espinosa, R
    [J]. WATER RESEARCH, 2005, 39 (15) : 3553 - 3564
  • [6] Catalytic ozonation of oxalic acid in an aqueous TiO2 slurry reactor
    Beltrán, FJ
    Rivas, FJ
    Montero-de-Espinosa, R
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2002, 39 (03) : 221 - 231
  • [7] An investigation of catalytic ozonation for the oxidation of halocarbons in drinking water preparation
    Cooper, C
    Burch, R
    [J]. WATER RESEARCH, 1999, 33 (18) : 3695 - 3700
  • [8] Catalytic ozonation of refractory organic model compounds in aqueous solution by aluminum oxide
    Ernst, M
    Lurot, F
    Schrotter, JC
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2004, 47 (01) : 15 - 25
  • [9] Mineralisation of coloured aqueous solutions by ozonation in the presence of activated carbon
    Faria, PCC
    Orfao, JJM
    Pereira, MFR
    [J]. WATER RESEARCH, 2005, 39 (08) : 1461 - 1470
  • [10] TiO2-catalysed ozonation of raw Ebro river water
    Gracia, R
    Cortes, S
    Sarasa, J
    Ormad, P
    Ovelleiro, JL
    [J]. WATER RESEARCH, 2000, 34 (05) : 1525 - 1532