硅胶干燥剂轮的理论性能

Zainab Mahdi Salih, Abdulsalam D. M.Hassan, Amer M. Al-Dabagh
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引用次数: 1

摘要

摘要-硅胶是一种通常用于干燥剂轮的物质,它在许多应用中用于减少从供气到特定空间的水分。在本研究中,研究了不同操作条件对硅胶轮性能的影响。已经使用过的干燥剂轮,直径55厘米,厚度20厘米。它含有34公斤的硅胶,以每小时30英里的速度旋转。研究了干燥剂轮的理论性能系数,包括除湿能力(MRC)、除湿性能(DCOP)、潜在性能系数(COPlat)和干燥剂轮的有效性(ϵ_d)。利用Novel Aire Technology软件程序(干燥剂轮模拟程序)(2012)对这些系数进行了理论研究。工艺空气(湿空气)入口温度在(30 ~ 43.4)℃之间,工艺空气入口湿度比在(0.011 ~ 0.019)kg/kg干空气之间,再生空气入口温度在(56.5 ~ 70)℃之间,工艺空气质量流量在(0.0814 ~ 0.199)kg/s之间。结果表明:随着质量流量从(0.0814 ~ 0.199)kg/s、湿度比从(11 ~ 19)g/kg空气、再生空气温度从(56 ~ 70)oC的增加,再生空气的除湿效果和除湿能力有相同的增加规律;随着进气温度从(30)℃升高到(43.4)℃,它们逐渐减小。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Theoretical Performance of Silica Gel Desiccant Wheel
Abstract— Silica gel is a substance commonly used in desiccant wheel, which in turn is used in many applications to reduce moisture from the supplied air to a specific space. In this research,  the effect of different operational conditions on the performance of silica gel wheel were studied. The desiccant wheel, which has been used, has a diameter of 55 cm and thickness of 20 cm. It contains 34 kg of silica gel and rotate at a speed of 30 rph. The theoretical performance coefficients of the desiccant wheel which have been studied include ,moisture removal capacity(MRC),dehumidification performance(DCOP),latent coefficient of performance (COPlat), and desiccant wheel effectiveness(ϵ_d). The theoretical investigation of these coefficients was done by using Novel Aire Technology software program (Simulation program of desiccant wheel) (2012). While the operational conditions like process air (humid air)inlet temperature between(30 to 43.4)0C, process air inlet humidity ratio between (0.011 to 0.019)kg/kgdry air ,regeneration air inlet temperature between (56.5 to 70)0C,and process air mass flow rate between(0.0814 to 0.199)kg/s. The results shows that the effectiveness and the moisture removal capacity have the same behavior increase with the increasing in mass flow rate from(0.0814 to 0.199) kg/s, humidity ratio from(11 to19)g/kgdry air, and regeneration air temperature from(56 t0 70)oC. But they reduces with increasing of inlet process air temperature from(30 to43.4)oC..
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