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生物膜反应器:活性炭颗粒流化床反应器中废水反硝化的实验与模型研究。

Biofilm reactors: an experimental and modeling study of wastewater denitrification in fluidized-bed reactors of activated carbon particles.

机构信息

Laboratory of Separation and Reaction Engineering, Department of Chemical Engineering, University of Porto, 4099 Porto Codex, Portugal.

出版信息

Biotechnol Bioeng. 1992 Aug;40(5):625-33. doi: 10.1002/bit.260400510.

Abstract

A fluidized-bed biofilm reactor using activated carbon particles of 1.69 mm diameter as the support for biomass growth and molasses as the carbon source is used for wastewater denitrification.The start-up of the reactor was successfully achieved in 1 week by using a liquor from garden soil leaching as the inoculum and a superficial velocity u(0) = 5u(mf). Typical biofilm thickness is 800 mum; therefore covered activated carbon particles have 3.3 mm in diameter.Reactor hydrodynamics was studied by tracer (KCl solution) experiments. The analysis based on residence time distribution theory involved a model with axial dispersion flow and tracer diffusion with linear adsorption inside the biofilm. Peclet numbers higher than 100 were found, allowing the plug flow assumption for the reactor model.Experimental profiles of nitrate and nitrite species were explained by a kinetic model of two consecutive zero-order reactions coupled with substrate diffusion inside the biofilm. Under the operating conditions used thick biofilms were obtained working in a diffusion-controlled regime.Comparison is made with results obtained in the same reactor with sand particles as the support for biomass growth. Activated carbon as the support has the following advantages: good adsorptive characteristics, homogeneous biofilm thickness along the reactor, and easy restart-up of the reactor.

摘要

采用粒径为 1.69 毫米的活性炭颗粒作为生物量生长的载体,利用糖蜜作为碳源,利用流化床生物膜反应器进行废水脱氮。通过使用菜园土浸出液作为接种物和表面速度 u(0) = 5u(mf),在 1 周内成功启动了该反应器。典型的生物膜厚度为 800 µm;因此,被覆盖的活性炭颗粒的直径为 3.3 毫米。通过示踪剂(KCl 溶液)实验研究了反应器的流体动力学。基于停留时间分布理论的分析涉及一个模型,其中包括轴向扩散流和生物膜内示踪剂扩散的线性吸附。发现了高于 100 的佩克莱数,允许对反应器模型进行推流假设。通过与生物膜内基质扩散相耦合的两个连续零级反应的动力学模型,解释了硝酸盐和亚硝酸盐物种的实验曲线。在使用的操作条件下,获得了在扩散控制条件下工作的厚生物膜。与使用砂粒作为生物量生长载体的相同反应器中获得的结果进行了比较。活性炭作为载体具有以下优点:良好的吸附特性、沿反应器均匀的生物膜厚度和反应器的容易重新启动。

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