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首页> 外文期刊>Journal of water chemistry and technology >Mathematical Modeling and Design of Fiber-Packed Bioreactors in Plants for Advanced Treatment of Domestic Wastewater
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Mathematical Modeling and Design of Fiber-Packed Bioreactors in Plants for Advanced Treatment of Domestic Wastewater

机译:植物中植物纤维包装生物反应器的数学建模与设计,用于国内废水的先进治疗

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摘要

-Processes of advanced treatment of domestic wastewater in fiber-packed bioreactors were studied. It was shown that, at the first stage of the operation of the bioreactors, such processes as adhesion, sorption, diffusion, decomposition, oxidation, etc. occur; and at the second stage, the biomass dies, and, together with mineral particles, is detached from the surface of Nylon 6 threads of the fiber packing, and is carried out of the bioreactors under the action of the hydrodynamic forces of the liquid flow. A mathematical model was constructed to describe the processes of the mass transfer between the wastewater flow and the surface of the biofilm formed on the threads of the fiber packing with taking into account the balance of the contaminant concentrations in the wastewater in the course of its downward movement. It was determined that, in designing the bioreactor, the distance between the axes of the threads should be chosen such that, on the one hand, the water velocity between the threads does not exceed a certain critical velocity, at which microorganisms attached to fibers are washed away, and on the other, the water velocity is sufficient for the rest of the biomass detached from the fibers to be carried out of the bioreactor. It was proposed to consider that the velocity of the water being treated in the bioreactor is in the range 1 -5 m/h. It was studied how the degree of wastewater treatment in a plant depends on the design and process parameters of the bioreactor, namely, the contents of organic contaminants of wastewater, the length of threads of the fiber packing, the water velocity between the threads, the duration of the downward movement of wastewater in the bioreactor, and the biosorption parameter. For example, the biosorption parameter at a diameter of threads of the fiber packing of 2 mm and a distance between their axes of 10 mm is nine times higher than the biosorption parameter at values of the respective parameters of 1 and 20 mm, respectively. A procedure of engineering design of a bioreactor was developed, which enables one to determine the characteristics of the main design elements ensuring the standard quality of the treated water.
机译:研究了纤维包装生物反应器中国内废水的先进治疗过程。结果表明,在生物反应器的操作的第一阶段,这种方法作为粘附,吸附,扩散,分解,氧化等。在第二阶段,生物质模具和与矿物颗粒一起从纤维填料的尼龙6螺纹的表面脱离,并且在液体流动的流体动力的作用下从生物反应器中进行。构建了一种数学模型,以描述在其向下的过程中的污染物浓度的平衡,描述了在纤维填料的螺纹上形成的废水流动和生物膜表面之间的传质的过程。移动。据确定,在设计生物反应器时,应选择螺纹轴之间的距离,使得一方面,螺纹之间的水速度不超过一定的临界速度,在该速度附着在纤维上的微生物冲走,另一个,水速足以使从纤维脱离的其余生物质脱离,以进行生物反应器。建议考虑在生物反应器中处理的水的速度为1 -5m / h。研究了植物中的废水程度如何取决于生物反应器的设计和工艺参数,即废水的有机污染物的含量,纤维包装的螺纹长度,线程之间的水速度,生物反应器中废水向下运动的持续时间,以及生物吸附参数。例如,光纤填料直径的生物吸附参数为2mm的螺母的螺母和10mm的轴之间的距离分别比相应参数为1和20mm的值的生物吸附参数高9倍。开发了一种生物反应器的工程设计程序,使人们能够确定保证处理水的标准质量的主要设计元件的特性。

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