JUSTIFICATION OF HEAT AND ENERGY PARAMETERS OF CONTACT DRYING PROCESS OF GRAIN

P. Ageev, V. Dolgov, V. Kurdyumov, A. Pavlushin
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Abstract

The purpose of the research is to identify factors that directly affect the thermophysical characteristics of the developed means for grain contact drying. In case of system analysis, this goal is achieved by widespread usage of modeling, which allows to substantiate not only the parameters of the appropriate process mode, but also to choose the most suitable way to control the drying process under production conditions. The conditions for heat transfer from the heating surface to the grain depend on the heat given off by the heating surface of the drying chamber, W; heat transfer coefficient W/(m2 ºС), temperature of the heating surface and the grain at the outlet from the drying chamber, °С; heating surface area, m2. In addition, in case of contact heat transfer, the problem of grain heating is linear (tgr2 = f(z, )), where z is the distance from the grain to the heating surface, m;  - time from the drying process start, s. It was found that the heating temperature limit of the surface of the drying chamber (made in the form of a cylinder, with a screw transporting working body) should not exceed 61С to ensure the grain temperature at the chamber outlet of 39С. In case of using a belt conveyor in the drying chamber and if it is in the form of a rectangular parallelepiped, the temperature limit of the chamber surface heating is 69 С. When the drying chamber is made in the form of a stepped surface enclosed in a box with vibration induction of grain movement, the heating temperature of this surface can be increased to 129 С without harm to the dried grain quality. It also allows to increase the throughput of the device compared to the first version of the drying chamber: from 0.2 t/h to 0.4 t/h.
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粮食接触干燥过程热能参数的确定
研究的目的是找出直接影响所开发的谷物接触干燥装置热物理特性的因素。在系统分析中,通过广泛使用建模来实现这一目标,建模不仅可以确定适当的工艺模式参数,还可以选择最合适的方式来控制生产条件下的干燥过程。从受热面向颗粒传热的条件取决于干燥室受热面放出的热量W;换热系数W/(m2ºС),干燥室出口受热面与颗粒的温度,°С;加热表面积,m2。此外,在接触传热情况下,晶粒受热问题是线性的(tgr2 = f(z,)),其中z为晶粒到受热面的距离,m;-从干燥过程开始的时间,s。发现干燥室表面的加热温度极限(制成圆筒形式,带螺杆输送工作体)不应超过61 С,以保证干燥室出口的谷物温度39 С。在干燥室内使用带式输送机时,如果是矩形平行六面体的形式,则干燥室内表面加热的温度极限为69 С。当将干燥室制作成具有振动感应谷物运动的箱式阶梯式表面时,可以将该表面的加热温度提高到129 С而不影响干燥后的谷物质量。与第一版干燥室相比,它还可以增加设备的吞吐量:从0.2 t/h到0.4 t/h。
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