Effects of operational conditions on sludge degradation and organic acids formation in low-critical wet air oxidation

被引:67
作者
Chung, Jinwook [2 ]
Lee, Mikyung [3 ]
Ahn, Jaehwan
Bae, Wookeun [4 ]
Lee, Yong-Woo [2 ]
Shim, Hojae [1 ]
机构
[1] Univ Macau, Fac Sci & Technol, Dept Civil & Environm Engn, Taipa, Peoples R China
[2] Samsung Engn Co Ltd, Seoul, South Korea
[3] Korea Water Resources Corp, Lake Sihwa Environm Res Ctr, Taejon, South Korea
[4] Hanyang Univ, Dept Civil & Environm Engn, Seoul, South Korea
关键词
Organic acids; Sludge degradation; Thermal hydrolysis; Wet air oxidation; PHENOL;
D O I
10.1016/j.jhazmat.2008.05.038
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Wet air oxidation processes are to treat highly concentrated organic compounds including refractory materials, sludge, and night soil. and usually operated at supercritical water conditions of high temperature and pressure. In this study, the effects of operational conditions including temperature, pressure, and oxidant dose on sludge degradation and conversion into subsequent intermediates such as organic acids were investigated at low critical wet oxidation conditions. The reaction time and temperature in the wet air oxidation process was shown an important factor affecting the liquefaction of volatile solids, with more significant effect on the thermal hydrolysis reaction rather than the oxidation reaction. The degradation efficiency of sludge and the formation of organic acids were improved with longer reaction time and higher reaction temperature. For the sludge reduction and the organic acids formation under the wet air oxidation, the optimal conditions for reaction temperature, time. pressure, and oxidant dose were shown approximately 240 degrees C, 30 min, 60 atm, and 2.0 L/min, respectively. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:10 / 16
页数:7
相关论文
共 19 条
  • [1] *AM PUBL HLTH ASS, 2001, STAND METH EX WAT WA
  • [2] Thermal hydrolysate as a carbon source for denitrification
    Barlindhaug, J
    Odegaard, H
    [J]. WATER SCIENCE AND TECHNOLOGY, 1996, 33 (12) : 99 - 108
  • [3] Wet air oxidation (WAO) for the treatment of industrial wastewater and domestic sludge.: Design of bubble column reactors
    Debellefontaine, H
    Crispel, S
    Reilhac, P
    Périé, F
    Foussard, JN
    [J]. CHEMICAL ENGINEERING SCIENCE, 1999, 54 (21) : 4953 - 4959
  • [4] EFFICIENT ELIMINATION OF ORGANIC LIQUID WASTES - WET AIR OXIDATION
    FOUSSARD, JN
    DEBELLEFONTAINE, H
    BESOMBESVAILHE, J
    [J]. JOURNAL OF ENVIRONMENTAL ENGINEERING-ASCE, 1989, 115 (02): : 367 - 385
  • [5] FRIEDMAN AA, 1998, J WATER POLLUT CONTR, V60, P1971
  • [6] KINETICS OF WET AIR OXIDATION OF PHENOL AND SUBSTITUTED PHENOLS
    JOGLEKAR, HS
    SAMANT, SD
    JOSHI, JB
    [J]. WATER RESEARCH, 1991, 25 (02) : 135 - 145
  • [7] TOXICITY TO DAPHNIA OF THE END PRODUCTS OF WET OXIDATION OF PHENOL AND SUBSTITUTED PHENOLS
    KEEN, R
    BAILLOD, CR
    [J]. WATER RESEARCH, 1985, 19 (06) : 767 - 772
  • [8] Wet oxidation of activated sludge
    Khan, Y
    Anderson, GK
    Elliott, DJ
    [J]. WATER RESEARCH, 1999, 33 (07) : 1681 - 1687
  • [9] GENERALIZED KINETIC-MODEL FOR WET OXIDATION OF ORGANIC-COMPOUNDS
    LI, LX
    CHEN, PS
    GLOYNA, EF
    [J]. AICHE JOURNAL, 1991, 37 (11) : 1687 - 1697
  • [10] Wet air oxidation: past, present and future
    Luck, F
    [J]. CATALYSIS TODAY, 1999, 53 (01) : 81 - 91