节点文献
采用序半连续反应器进行硝化和反硝化工艺的数学模拟
Modeling of nitrification and denitrification in sequential fed-batch reactor
【摘要】 研究了生物废水处理应用于序半连续式反应器(SFBR)工艺中的微生物生长、硝化和反硝化动力学。基于活性污泥1号模型(ASMNo. 1)中的原理和结论,导出了在有氧阶段和缺氧阶段微生物生长速率、铵、硝酸盐、易生物降解基质等的反应速率及它们的物料平衡方程。在实验的基础上,对模型中的各参数采用了合适的方法进行参数估值,即:龙格库塔法解常微分方程组和黄金分割法搜索最小误差,该模型的最小误差ε≈4 799;得出了应用于本工艺中数学模型中的各动力学参数和化学计量系数,如KS 39. 997,KNO 0 .397,KNH 1 997,KOA 0 .404,KOH 0. 297, μA 0 .0026,μH 0. 207,YA 0 .24,YH. 0 6。
【Abstract】 The kinetics of growth rates of microorganisms, the rates of nitrification and denitrification which applied in biological wastewater treatment of sequential fed-batch reactor were studied. The growth rate of microorganisms, the rates of nitrification and denitrification,the rates of reaction for readily biodegradable substrate and their material balance in aerobic and anoxic period were developed, respectively, according to the principle and result in activated sludge model No. 1 (ASM1).The adequate methods of parameter estimation were adopted from the experiment results. The group of differential equations was dissolved with Ronge-Kutta method and minimum error was searched with Gold Division method on the base of experimental result. The minimum error ε was about 4.799. The value of kinetics parameters and stoichiometric coefficient such as μ_A、μ_H、Y_A 、Y_H 、K_S 、K_ NO 、K_ NH、K_ OA、K_ OH in the model were estimated and parameters in the model were estimated from the result of the experiment.
【Key words】 sequential fed-batch reactor; activated sludge; nitrification; denitrification; kinetics;
- 【文献出处】 环境污染治理技术与设备 ,Techniques and Equipment for Environmental Pollution Control , 编辑部邮箱 ,2005年04期
- 【分类号】X703
- 【被引频次】11
- 【下载频次】214