Catalytic hydrolysis of trifluoromethane over alumina

被引:27
作者
Han, Wenfeng [1 ]
Chen, Yuliang [1 ]
Jin, Bibo [1 ]
Liu, Huazhang [1 ]
Yu, Hai [2 ]
机构
[1] Zhejiang Univ Technol, Hangzhou 310014, Zhejiang, Peoples R China
[2] CSIRO Energy Ctr, Mayfield West, NSW, Australia
来源
GREENHOUSE GASES-SCIENCE AND TECHNOLOGY | 2014年 / 4卷 / 01期
关键词
Trifluoromethane; Catalytic hydrolysis; Alumina; HFC-23; Waste gas treatment; Zn promoter; GREENHOUSE-GAS; DECOMPOSITION; CHF3; CF4; HYDRODECHLORINATION; ADSORPTION; PYROLYSIS; MECHANISM;
D O I
10.1002/ghg.1376
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Catalytic hydrolysis over alumina was carried out at temperatures between 350 degrees C and 520 degrees C and gas hourly space velocity (GHSV) of 6000 h(-1). The effects of water vapor concentration, alumina phase, and Zn promoter as well as the reaction mechanism were investigated in detail. The results show that the presence of small amounts of water vapor (0.8%) significantly improves the activity of -Al2O3, while higher water vapor concentration (>2.8%) does not further enhance the decomposition of CHF3. Compared with -Al2O3 and AlOOH, -Al2O3 is inactive for the targeted reaction although it is stable under conditions studied (with the presence of HF product). Zn is an efficient promoter for the improvement of activity and stability of alumina catalyst. More attention is paid to the reaction and deactivation mechanism. Based on the experimental results and thermodynamic analysis, a reaction mechanism is proposed which explains the effect of water vapor and deactivation of catalyst reasonably.
引用
收藏
页码:121 / 130
页数:10
相关论文
共 36 条
  • [1] Catalytic Hydrodefluorination of Fluoromethanes at Room Temperature by Silylium-ion-like Surface Species
    Ahrens, Mike
    Scholz, Gudrun
    Braun, Thomas
    Kemnitz, Erhard
    [J]. ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2013, 52 (20) : 5328 - 5332
  • [2] [Anonymous], PROJ THERM OX SYNTH
  • [3] Surface Interactions of C2 and C3 Polyols with γ-Al2O3 and the Role of Coadsorbed Water
    Copeland, John R.
    Shi, Xue-Rong
    Sholl, David S.
    Sievers, Carsten
    [J]. LANGMUIR, 2013, 29 (02) : 581 - 593
  • [4] Hydrolytic decomposition of CF4 over alumina-based binary metal oxide catalysts:: high catalytic activity of gallia-alumina catalyst
    El-Bahy, ZM
    Ohnishi, R
    Ichikawa, M
    [J]. CATALYSIS TODAY, 2004, 90 (3-4) : 283 - 290
  • [5] Hydrolysis of CF4 over alumina-based binary metal oxide catalysts
    El-Bahy, ZM
    Ohnishi, R
    Ichikawa, M
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2003, 40 (02) : 81 - 91
  • [6] DEACTIVATION OF A PT/AL2O3 CATALYST DURING THE OXIDATION OF HEXAFLUOROPROPYLENE
    FARRIS, MM
    KLINGHOFFER, AA
    ROSSIN, JA
    TEVAULT, DE
    [J]. CATALYSIS TODAY, 1992, 11 (04) : 501 - 516
  • [7] The catalytic decomposition of CHF3 over ZrO2-SO4
    Feaver, WB
    Rossin, JA
    [J]. CATALYSIS TODAY, 1999, 54 (01) : 13 - 22
  • [8] Influence of O2 concentration on non-thermal plasma decomposition of halide gases containing Cl and F
    Fujita, T
    Hari, T
    Kojima, Y
    Matsuda, H
    Huang, LW
    [J]. KAGAKU KOGAKU RONBUNSHU, 2005, 31 (03) : 226 - 230
  • [9] Production of CaF2 by the Destructive Adsorption of Trifluoromethane and a Binary Mixture of Trifluoromethane/Chlorodifluoromethane with CaO Powder under Air-Flow
    Furusawa, Takeshi
    Ogawa, Tatsuya
    Numao, Takashi
    Sato, Masahide
    Suzuki, Noboru
    [J]. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2012, 45 (06) : 459 - 465
  • [10] Treatment of the potent greenhouse gas, CHF3-An overview
    Han, Wenfeng
    Li, Ying
    Tang, Haodong
    Liu, Huazhang
    [J]. JOURNAL OF FLUORINE CHEMISTRY, 2012, 140 : 7 - 16