Valourization of using efficiency of filtration drying for alcohol distillery stillage

Q1 Environmental Science
O.S. Ivashchuk, V.M. Atamanyuk, R.A. Chyzhovych
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引用次数: 0

Abstract

The article presents the results of the calculation of specific energy consumption for the filtration drying process of corn alcohol distillery stillage. It was determined that the optimal total energy consumption for the evaporation of 1 kg of moisture during the filtration drying of corn alcohol distillery stillage from the initial moisture content of the material ω1 = 72.78 % wt. to the final value ω2 = 14 % wt. is 9468.96 kJ/kg H2O or 2.63 kW h/kg H2O for the following process parameters: the height of the layer of dried material H = 120 mm, the thermal agent temperature T = 90 °C, the thermal agent velocity v0 = 1.76 m/sec. Based on the selected optimal parameters of the filtration drying process of corn alcohol distillery stillage at the experimental installation, an evaluation calculation of the efficiency of filtration drying in industrial conditions was made. The total amount of energy required to dry ⁓ 1000 kg of corn alcohol distillery stillage in the filtration drying installation is approximately 1923.91 kW h. The total energy consumption for the removal of 1 kg of moisture during the test material drying at an industrial filtration drying installation is approximately 2.64 kW h/kg H2O. To compare the effectiveness of the filtration method of drying for corn alcohol distillery stillage, it was calculated for drying under a similar technical task in a rotary dryer. During the drying of 1000 kg of corn alcohol distillery stillage, a total of approximately 2146.91 kW h of energy is required, and the total energy consumption for removing 1 kg of moisture during the corn alcohol distillery stillage drying in a rotary dryer is approximately 3.13 kW h/kg H2O. It was calculated that the use of the filtration drying method makes it possible to reduce the specific energy consumption for removing 1 kg of moisture by 15.65 % with the required amount of thermal agent compared to drying in a rotary dryer. The use of filtration drying in industry would have a higher economic effect, given the higher heat losses in a rotary dryer to the environment and the need for energy-intensive auxiliary equipment for rotary dryers.

酒精酿造厂蒸馏物过滤干燥使用效率的评估
文章介绍了玉米酒精蒸馏残渣过滤干燥过程中具体能耗的计算结果。结果表明,在下列工艺参数下,玉米酒精蒸馏残渣过滤干燥过程中,从物料初始含水量ω1 = 72.78 % wt.到最终含水量ω2 = 14 % wt.蒸发 1 kg 水分的最佳总能耗为 9468.96 kJ/kg H2O 或 2.63 kW h/kg H2O:干燥物料层高度 H = 120 mm,热媒温度 T = 90 °C,热媒速度 v0 = 1.76 m/sec。根据在实验装置中选定的玉米酒精蒸馏残渣过滤干燥工艺的最佳参数,对工业条件下的过滤干燥效率进行了评估计算。在过滤干燥装置中干燥⁓ 1000 千克玉米酒精蒸馏残渣所需的总能耗约为 1923.91 千瓦时。在工业过滤干燥装置中干燥试验材料时去除 1 千克水分所需的总能耗约为 2.64 千瓦时/千克水。为了比较过滤法干燥玉米酒精蒸馏残渣的效果,我们计算了在回转式干燥机中类似技术任务下的干燥效果。在干燥 1000 千克玉米酒精蒸馏残渣的过程中,总共需要约 2146.91 千瓦时的能量,而在回转式干燥器中干燥玉米酒精蒸馏残渣时,去除 1 千克水分的总能耗约为 3.13 千瓦时/千克水。据计算,与在回转式干燥器中干燥相比,使用过滤干燥法可使去除 1 千克水分所需的热能消耗减少 15.65%。考虑到回转式干燥机对环境的热损失较大,以及回转式干燥机需要高能耗的辅助设备,在工业中使用过滤干燥法会产生更高的经济效益。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Case Studies in Chemical and Environmental Engineering
Case Studies in Chemical and Environmental Engineering Engineering-Engineering (miscellaneous)
CiteScore
9.20
自引率
0.00%
发文量
103
审稿时长
40 days
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