酸化破乳-萃取-蒸氨预处理用于催化湿式过氧化氢氧化处理煤气化废水

赵颖, 孙承林, 王亚旻, 卫皇曌, 韩劲, 于永辉, 于杨. 酸化破乳-萃取-蒸氨预处理用于催化湿式过氧化氢氧化处理煤气化废水[J]. 环境工程学报, 2017, 11(9): 5049-5056. doi: 10.12030/j.cjee.201611028
引用本文: 赵颖, 孙承林, 王亚旻, 卫皇曌, 韩劲, 于永辉, 于杨. 酸化破乳-萃取-蒸氨预处理用于催化湿式过氧化氢氧化处理煤气化废水[J]. 环境工程学报, 2017, 11(9): 5049-5056. doi: 10.12030/j.cjee.201611028
ZHAO Ying, SUN Chenglin, WANG Yamin, WEI Huangzhao, HAN Jin, YU Yonghui, YU Yang. Acidification demulsion-extraction-steamed ammonia pretreatment for catalytic wet peroxide oxidation of coal gasification wastewater treatment[J]. Chinese Journal of Environmental Engineering, 2017, 11(9): 5049-5056. doi: 10.12030/j.cjee.201611028
Citation: ZHAO Ying, SUN Chenglin, WANG Yamin, WEI Huangzhao, HAN Jin, YU Yonghui, YU Yang. Acidification demulsion-extraction-steamed ammonia pretreatment for catalytic wet peroxide oxidation of coal gasification wastewater treatment[J]. Chinese Journal of Environmental Engineering, 2017, 11(9): 5049-5056. doi: 10.12030/j.cjee.201611028

酸化破乳-萃取-蒸氨预处理用于催化湿式过氧化氢氧化处理煤气化废水

  • 基金项目:
  • 中图分类号: X703

Acidification demulsion-extraction-steamed ammonia pretreatment for catalytic wet peroxide oxidation of coal gasification wastewater treatment

  • Fund Project:
  • 摘要: 调酸-萃取-蒸氨工序预处理煤气化废水温度达87~95℃,联合高温催化湿式过氧化氢氧化(catalitic wet peroxide oxidation,CWPO)处理煤气化废水,可显著提高废水可生化性。比较了3% Fe/椰壳炭、3% Fe/Al2O3在CWPO过程中的催化性能。实验结果表明,在反应条件为80℃、pH0为4、H2O2加入量为7.8~10.5 mg·L-1、空速(LHSV)为0.5 h-1时,3% Fe/椰壳炭对预处理煤气化出水COD去除率高达60%,对总酚的去除率高达90%以上,H2O2利用率大于99%,色度由初始1 000倍降至2倍,此外,出水B/C为0.51,达到进入生化处理系统的水质要求。
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  • [1] ZHANG W Q, MA J, YANG S D, et al. Pretreatment of coal gasification wastewater by acidification demulsion[J]. Chinese Journal of Chemical Engineering, 2006, 14(3):398-401
    [2] GAI H J, JIANG Y B, QIAN Y, et al. Conceptual design and retrofitting of the coal-gasification wastewater treatment process[J]. Chemical Engineering Journal, 2008, 138(1/2/3):84-94
    [3] ZHANG W H, WEI C H, CHAI X S, et al. The behaviors and fate of polycyclic aromatic hydrocarbons (PAHs) in a coking wastewater treatment plant[J]. Chemosphere, 2012, 88(2):174-182
    [4] 何锋. 煤化工废水的来源与特点及其相应的处理技术探究[J]. 科技视界, 2012(23):320-321
    [5] CAUDO S, CENTI G, GENOVESE C, et al. Copper-and iron-pillared clay catalysts for the WHPCO of model and real wastewater streams fromolive oil milling production[J]. Applied Catalysis B:Environmental, 2007, 70(1/2/3/4):437-446
    [6] KENNEDYA L J,VIJAYAB J J, SEKARANA G, et al. Equilibrium, kinetic and thermodynamic studies on the adsorption of m-cresol onto micro-and mesoporous carbon[J]. Journal of Hazardous Materials, 2007, 149(1):134-143
    [7] CEZAR C, CARMEN T, MATEI M, et al. Catalytic wet peroxide oxidation of phenol over Fe-exchanged pillared beidellite[J]. Water Resource, 2003, 37(5):1154-1160
    [8] SERGIO N, MERCEDES A, HERMENEGILDO G. Heterogeneous Fenton catalysts based on clays, silicas and zeolites[J]. Applied Catalysis B:Environmental, 2010, 99(1):1-26
    [9] ZAZO J A,BEDIA J,FIERRO C M, et al. Highly stable Fe on activated carbon catalysts for CWPO upon FeCl3 activation of lignin from black liquors[J]. Catalysis Today, 2012, 187(1):115-121
    [10] ANISSA D, NAFAÂ A. Heterogeneous catalytic wet peroxide oxidation of paraquat in the presence of modified activated carbon[J]. Applied Catalysis B:Environmental, 2010, 97(1/2):227-235
    [11] MACARENA M, ZAHARA M P, JOSE A C, et al. Improved wet peroxide oxidation strategies for the treatment of chlorophenols[J]. Chemical Engineering Journal, 2013, 228(14):646-654
    [12] MACARENA M, ZAHARA M P, NIEVES M, et al. A ferromagnetic gamma-alumina-supported iron catalyst for CWPO. Application to chlorophenols[J]. Applied Catalysis B:Environmental, 2013, 136:218-224
    [13] CARLA D L, FERNANDO I, PAOLA M, et al. Alumina supported Fenton-like systems for the catalytic wet peroxide oxidation of phenol solutions[J]. Industrial & Engineering Chemistry Research, 2012, 51(26):8979-8984
    [14] 国家环境保护总局. 水和废水监测分析方法[M]. 4版. 北京:中国环境科学出版社,2002
    [15] 姜成春, 庞素艳, 马军,等. 钛盐光度法测定Fenton氧化中的过氧化氢[J]. 中国给水排水, 2006, 22(4):88-91
    [16] LI Y M, GU G W, ZHAO J F, et al. Anoxic degradation of nitrogenous heterocyclic compoundsby acclimated activated sludge[J]. Process Biochemistry, 2001, 37(1):81-86
    [17] BOSSMANN S H, OLIVEROS E, GOEB S, et al. New evidence against hydroxyl radicals as reactive intermediates in the thermal and photochemically enhanced Fenton reactions[J]. Journal of Physical Chemistry A, 1998, 102(28):5542-5550
    [18] FEMANDO M, ISABEL P, CHRISTINA B, et al. Chemical surface modified-activated carbon cloth for catalytic wet peroxide oxidation of phenol[J]. Journal of Chemical Technology and Biotechnology, 2014, 89(8):1182-1188
    [19] BAUTISTA P, MOHEDANO A F, CASAS J A, et al. An overview of the application of Fenton oxidation to industrial wastewaters treatment[J]. Journal of Chemical Technology and Biotechnology, 2008, 83(10):1323-1338
    [20] CRISTINA F, PERE-LLUÍS C, FRANCESC C, et al. Solar photoelectro-Fenton degradation of cresols using a flow reactor with a boron-doped diamond anode[J]. Applied Catalysis B:Environmental, 2007, 75(1/2):17-28
    [21] CHU Y Y,ZHANG D M,LIU L, et al. Electrochemical degradation of m-cresol using porous carbon-nanotube-containing cathode and Ti/SnO2-Sb2O5-IrO2 anode:Kinetics, byproducts and biodegradability[J]. Journal of Hazardous Materials, 2013, 252-253:306-312
    [22] LIU P J, HE S B, WEI H Z, et al. Characterization of α-Fe2O3/γ-Al2O3 catalysts for catalytic wet peroxide oxidation of m-cresol[J]. Industrial & Engineering Chemistry Research, 2015, 54(1):130-136
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  • 收稿日期:  2016-12-31
  • 刊出日期:  2017-08-26

酸化破乳-萃取-蒸氨预处理用于催化湿式过氧化氢氧化处理煤气化废水

  • 1.  中国科学院大连化学物理研究所, 大连 116023
  • 2.  中国科学院大学, 北京 100049
  • 3.  辽宁工程技术大学环境科学与工程学院, 阜新 123000
基金项目:

摘要: 调酸-萃取-蒸氨工序预处理煤气化废水温度达87~95℃,联合高温催化湿式过氧化氢氧化(catalitic wet peroxide oxidation,CWPO)处理煤气化废水,可显著提高废水可生化性。比较了3% Fe/椰壳炭、3% Fe/Al2O3在CWPO过程中的催化性能。实验结果表明,在反应条件为80℃、pH0为4、H2O2加入量为7.8~10.5 mg·L-1、空速(LHSV)为0.5 h-1时,3% Fe/椰壳炭对预处理煤气化出水COD去除率高达60%,对总酚的去除率高达90%以上,H2O2利用率大于99%,色度由初始1 000倍降至2倍,此外,出水B/C为0.51,达到进入生化处理系统的水质要求。

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