选择搅拌器并优化沼气装置发酵罐中的基质混合过程

A. A. Rubcov, D. A. Nemuschenko
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引用次数: 0

摘要

这项工作的相关性与牲畜粪便污染造成的土壤退化问题以及将粪便及时处理成有效有机肥料和沼气的必要性有关。提高有机肥料的使用比例使发展有机农业技术成为可能,从而生产出健康的农作物产品。这项工作研究了运行中的试点沼气厂发酵罐中的基质混合过程。该技术生产线的设计目的是通过厌氧消化处理液态有机废物,主要是粪便或垃圾,以工业规模生产创新型环保有机肥料。研究的目的是选择一种搅拌器,并优化沼气厂发酵罐中基质的混合条件。通过实验室方法研究了基质的物理化学特性。混合过程的数学模型是基于对反应器中流动的流体力学的半经验描述,并根据具有特定几何特征的发酵罐条件下的问题现状进行了更新。通过这项工作,确定了搅拌器几何尺寸的最佳选择(叶片角度为 30° 的三叶间歇式搅拌器的三种变体,叶轮尺寸和转速各不相同),并计算了混合过程的参数。根据实验室实验和沉淀率的计算结果,确定了搅拌器的开启频率(每天一次)和搅拌器连续工作以均匀悬浮液的时间。这项工作的结果可用于设计生物反应器中的混合装置和基质混合模式。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Selecting a stirrer and optimizing the process of mixing the substrate in the fermenter of biogas unit
The relevance of the work is related to the problem of soil degradation as a result of pollution by livestock waste and the need for timely disposal of waste into effective organic fertilizer and biogas. Increasing the share of the use of organic fertilizers makes it possible to develop organic farming technologies, and accordingly leads to the production of healthy crop products. The work investigated the process of substrate mixing in the fermenters of an operating pilot biogas plant. The technological line is designed for processing liquid organic waste, mainly manure or litter, by anaerobic digestion to produce innovative environmentally friendly organic fertilizers on an industrial scale. The purpose of the study was to select a stirrer and optimize the conditions for mixing the substrate in the fermenters of a biogas plant. The physicochemical properties of the substrate were studied by laboratory methods. The mathematical model of the mixing process is based on a semi-empirical description of the hydrodynamics of flows in the reactor, modernized taking into account the current state of the issue under the conditions of a fermenter with specific geometric characteristics. As a result of the work carried out, the optimal options for the geometric dimensions of the stirrers were determined (three variants for three-blade stirrers intermittent with a blade angle of 30°, differing in the size of the impeller and rotation speed) and the parameters of the mixing process were calculated. Based on a laboratory experiment and the results of calculating the sedimentation rate, the frequency of turning on the stirrer (once a day) and the time of its continuous operation to homogenize the suspension were determined. The results of the work can be used in the design of mixing devices and substrate mixing modes in bioreactors.
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