期刊文献+

以呼吸速率为基础活性污泥抑制动力学常数的测定研究 被引量:1

Study on measurement of inhibition kinetic constant based on respiration rate in activated sludge process
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摘要 通过对活性污泥不同抑制情况下呼吸速率变化的分析,对不同的抑制类型提出了利用呼吸速率确定抑制动力学模型中动力学常数的不同方法。产物抑制通过已知起始浓度和呼吸速率曲线,来构建以1/KP′为斜率,KS为截距的直线方程来求解KS和抑制常数。底物抑制先通过呼吸速率求解最值点的底物浓度,然后根据呼吸速率变化最大值点的关系公式求解抑制常数的方法。竞争性抑制和非竞争性抑制通过求解等速点底物浓度的方法求解抑制常数。对于非竞争性抑制还可以通过简单的最大呼吸速率比值法来求解抑制常数。同时选择非竞争性抑制进行了试验验证和常数求解。最终通过2种方法得到葡萄糖降解时NaC l的抑制常数为20.2 g/L,或者0.02倍的KS。 In this article, through theoretical analysis about respiration rate of different inhibition in activated sludge process, different kinds of measurement methods of inhibition kinetic constant on different inhibition are put forward based on respiration rate. The inhibition kinetic constant of product inhibition and Ks is get through the line fitting. The line, of which the slope and interception is 1/K'e and Ks respectively, is constructed with the known starting concentration of substrate and the curve of respiration rate. In the course of solution of substrate inhibition constant, the substrate concentration on the maximum of respiration rate is calculated firstly and the kinetic constant of substrate inhibition is solved through the relation equation on the maximum of respiration rate. The inhibition kinetic constant about competitive and non-competitive inhibition is figured out by calculating the substrate concentration on the same speed point. The another way of non-competitive inhibition is the ratio method of maximal respiration rate. At the same time, inhibition kinetic constant of non-competitive inhibition is testified by force of a experiment. Finally, the inhibition kinetic constant of NaCl inhibition on degradation of glucose is 20.2 g/L, or 0.02Ks which are calculated by the three different methods.
出处 《环境工程学报》 CAS CSCD 北大核心 2008年第4期493-497,共5页 Chinese Journal of Environmental Engineering
关键词 呼吸速率 抑制动力学 抑制常数 活性污泥 respiration rate inhibition kinetics inhibition kinetic constant activated sludge
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参考文献4

  • 1[2]IAW Task Group.Respirometry in Control of the Activated Sludge Process:Benchmarking Control Strategies.London:IWA Publishing,2002
  • 2[3]Henry Spanjers,et al.Towards a simulation-benchmark for evaluating respirometry-based control strategies.War.Sci.Tech.,1998,37(12):219~226
  • 3[4]Nancy I.Lopez,et al.Controls on nitrification in a waterlimited ecosystem:Experimental inhibition of ammonia-oxidising bacteria in the Patagonian steppe.Soil Biology & Bi-ochemistry,2003,35:1609~1613
  • 4崔有为,王淑莹,甘湘庆,姜桂莲,李桂星,袁一星.生物处理含盐污水的盐抑制动力学[J].环境污染治理技术与设备,2005,6(5):38-41. 被引量:14

二级参考文献13

  • 1Stewart M. J.,Ludwing H. F.,Keams W. H. Effect of varying salinity on extended aeration process.WPCF,1962, 34:1131 - 1177.
  • 2Ludzack F. J. and Noran D. K. Tolerance of high salinities by conventional wastewater treatment processes. WPCF,1965,37(10):1404 - 1416.
  • 3Lawton G. W. ,Eggert E. V. Some effect of high sodium chloride concentrations on trickling filter slimes. WPCF,1957, 29 : 1228 - 1236.
  • 4Kargi F. , Dincer A. R. Effect of sludge recycle on performance of a rotating biodisc contactor treating saline wastewater. Bioprocess Engineering, 1998, 18 : 235 - 239.
  • 5Kargi F.and Dincer A.R.Enhancement of biological treatment performance of saline wastewater by halophilic bacteria. Bioprocess Engineering, 1996, 17:325 - 330.
  • 6Kargi F. ,Dincer A. R. Effect of salt concentration on biological treatment of saline wastewater by fed-batch operation. Enzyme & Microbial Technol. ,1996, 19:529 - 537.
  • 7Dincer A. R. ,Kargi F. Salt inhibition kinetics in nitrification of synthetic saline wastewater. Enzyme & Microbial Technol.,2001, 28:661 -665.
  • 8文湘华,占新民,王建龙,钱易.含盐废水的生物处理研究进展[J].环境科学,1999,20(3):104-106. 被引量:101
  • 9崔有为,王淑莹,于德爽,祝贵兵,彭永臻.以溶解氧作为SBR法处理含盐污水的计算机控制参数可行性研究[J].给水排水,2003,29(6):54-57. 被引量:7
  • 10王淑莹,崔有为,于德爽,祝贵兵,王海东.无机盐对活性污泥沉降性的影响[J].环境工程,2003,21(5):7-9. 被引量:28

共引文献13

同被引文献25

  • 1Shi X Y,Yu H Q, Sun Y J,et al. Characteristices of aerobic granules rich in autotrophic ammonium-oxidizing bacteria in a sequencing batch reactor[J]. Chemical Engineering Jour- nal, 2009,147(2/3) : 102- 109.
  • 2Su K Z,Yu H Q. Formation and characterization of aerobic granules in a sequencing batch reactor treating soybean-pro- cessing wastewater[J]. Environmental Science & Technolo- gy, 2005,39 (8) : 2818- 2827.
  • 3Su K Z, Yu H Q. A generalized model for aerobic granule based sequencing hatch reactor: 1. model development [J ]. Environmental Science &. Technology, 2006, 40 ( 15 ) : 4703-4708.
  • 4Lim J J,Kim M H, Kim M J,et al. A systematic model cali- bration methodology based on multiple errors minimization method for the optimal parameter estimation of ASMI[J]. Korean Journal of Chemical Engineering, 2012, 29 ( 3 ) : 291-303.
  • 5Moy B Y,Tay J H,Toh S K,et al. High organic loading in- fluences the physical characteristics of aerobic sludge gran- ules[ J ]. Letters in Applied Microbiology, 2002, 34 ( 6 ) : 407-412.
  • 6Sun X F, Liu C Y, Ma Y, et al. Enhanced Cu( Ⅱ ) and Cr ( Ⅵ ) biosorption capacity on poly (ethylenimine) grafted aerobic granular sludge [J]. Colloids and Surface B: Bioint- erfaces,2011,82(2) :456-462.
  • 7de Urzedo A P,Diniz M E,Nascentes C C,et al. Photolytic degradation of the insecticides thiamethoxam in aqueous medium monitored by directinfusion electrospray ionization mass spectrometry [J]. Journal of Mass Spectrometry, 2007, 42(10): 1319-1323.
  • 8Reichert P. AQUASIM2.0-user manual: computer pro- gram for the identification and simulation of aquatic systems[Z]. Swiss Federal Institute for Environmental Sci- ence & Technology (EAWAG),1998.
  • 9国际水协废水生物处理设计与运行数学模型课题组.活性污泥数学模型[M].张亚雷,李咏梅,译.上海:同济大学出版社,2003:9-11.
  • 10Nicolella C, van Loosdrecht M C M, Heijnen J J. Mass transfer and reaction in a biofilm airlift suspension reactor [J]. Chemical Engineering Science, 1998, 53 (15): 2743-2753.

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