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废水中起始惰性溶解有机物的测定 被引量：2

Measurement of the initial soluble inert organic matter in wastewater
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摘要 介绍了4种测定起始惰性溶解有机物的方法,即Ekama和国际水质协会提出的两种直接测定法和排除溶解性残留物干扰的两种间接测定法。通过分析比较,指出了4种方法的优缺点及适用情况。其中直接测定法适用于有机物浓度较低的生活污水,间接测定法适用于有机物浓度较高的工业废水。 Four methods are presented to measure the soluble inert organic matter in the influent wastewater. Some are direct measurements which are offered by Ekama and IAWQ, the others are indirect measurements which exclude the interference of soluble residua, meanwhile the advantages and disadvantages of each method are presented. Direct measurements can be used to municipal wastewater, however indirect measurements can be used to strong industrial wastewater.
作者 于静洁 顾国维 张志峰
机构地区 同济大学污染控制与资源化研究国家重点实验室
出处 《环境污染与防治》 CAS CSCD 北大核心 2005年第5期395-396,i0006,共3页 Environmental Pollution & Control
基金 国家自然科学基金重点资助项目(No.50138010)。
关键词 废水 起始惰性溶解有机物 排放标准 间接测定法 溶解有机物 工业废水 惰性 起始 直接测定法 有机物浓度 Wastewater Initial soluble Inert organic matter Effluent limitation criteria
分类号 X703 [环境科学与工程—环境工程] TS207.3 [轻工技术与工程—食品科学]
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参考文献8

  • 1Henze M, Grady C P L, Gujer W, et al. Activated sludge model No. 1. London: IAWPRC,1987.
  • 2Ekama G A,Marais G V R. Theory design and operation of nutrient removal activated sludge processes. WRC,Pretoria,South Africa, 1984.
  • 3Ekama G A,Dold P L,Marais G V R. Procedures for determining influent COD fractions and the maximum specific growth rate of heterotrophs in activated sludge systems. Wat. Sci. Tech. , 1986,18:91-114.
  • 4Chudoba J. Residual organic matter in activated sludge process effluent. Ⅰ. Degradation of saccharides, fatty acids, and amino acids under batch conditions. Technol. of Water, 1967,12 : 39 - 75.
  • 5Grady C P L,Williams D R. Effects of influent substrate concentration on the kinetics of natural microbial populations in continuous culture. Wat. Res. ,1975,9:171-180.
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  • 8Germirli F,Orhon D,Artan N. Assessment of the initial inert soluble COD in industial wastewaters. Wat. Sci. Tech. , 1991,23:1077-1086.

同被引文献21

  • 1HENZE M,GUJER W, MINO T, et al. Activated sludge models ASM1 ,ASM2,ASM2d and ASM3[M]. London: IAW Publishing, 2000.
  • 2EKAMA G A,DOLD P L,MARAIS G V R. Procedures for determining influent COD fractions and the maximum specific growth rate of heterotrophs in activated sludge process[J]. Water Sci. Technol. ,1986,18(6) :91-114.
  • 3SIEGRIST H,TSCHUI M. Interpretation of experimental data with regard to the Activated Sludge Model No. 1 and calibration of the model for municipal wastewater treatment plants[J]. Water Sci. Technol. , 1992,25(6) : 167-183.
  • 4HENZE M. Characterization of wastewater for modeling of activated sludge processes[J]. Water Sci. Technol. , 1992,25 (6) : 1-15.
  • 5ROELEVELD P J, VAN LOOSDERCHT M C M. Experience with guidelines for wastewater characterization in the Netherlands[J]. Water Sci. Technol. ,2002,45(6) :77-87.
  • 6BOERO V J, ECKENFELDER W W, BOWERS A R. Soluble microbial product formation in biological systems[J]. Water Sci. Technol. ,1991,23(4/6) : 1067-1076.
  • 7NOGUERA D R,ARAKI N,RITTMANN B E. Soluble microbial products (SMP) in anaerobic chemostats[J]. Biotechnol. Bioeng. , 1994,44(9) : 1040-1047.
  • 8BARKER D J, STUCKEY D C. A review of soluble microbial products (SMP) in wastewater treatment systems[J]. Water Res. ,1999,33(14) :3063-3082.
  • 9ORHON D,KARAHAN O,SOZEN S. The effect of residual microbial products on the experimental assessment of the particulate inert COD in wastewaters[J]. Water Res. , 1999,33 (14).
  • 10DOGRUEL S,GENCELI E A,BABUNA F G,et al. An investigation on the optimal location of ozonation within biological treatment for a tannery wastewater[J]. J. Chem. Tech. Biotechnol. ,2006,81(12):1877-1885.

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环境污染与防治
2005年 第5期

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