Modeling and Optimization of Evaporation Process in Sugar Industries

G. Sebastian, D. N. Kyatanavar
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Abstract

Model preparation of evaporation process and optimizing the same have been a challenging task for researchers. Evaporation process in sugar industries is characterized by its highly non-linear nature and conventional control strategies do not yield good results for the control of the same. With the evaporator being the most energy consuming unit in sugar manufacturing process, it has direct impact on sugar quality as well as steam economy. In this paper, a simulation model of an evaporator having four effects has been developed in Simulink. For optimizing this model, Taguchi technique combined with Grey relational analysis has been employed. The level of influence of variables like Temperature of the feed, Rate of flow of the feed and Rate of steam flow, on the steam economy and sugarcane juice concentration has been determined using ANOVA (Analysis of Variance). Minitab 17 software has been used for this. Finally, the relative contribution of each process parameter on the performance characteristics of the evaporator has also been determined.
制糖工业蒸发过程建模与优化
蒸发过程模型的制备和优化一直是一个具有挑战性的课题。制糖工业蒸发过程具有高度非线性的特点,传统的控制策略对蒸发过程的控制效果不佳。蒸发器是制糖过程中耗能最大的设备,直接影响制糖的质量和蒸汽经济性。本文在Simulink中建立了具有四种效应的蒸发器仿真模型。为优化该模型,采用了田口法和灰色关联分析相结合的方法。采用方差分析(ANOVA)确定了诸如进料温度、进料流量和蒸汽流量等变量对蒸汽经济性和甘蔗汁浓度的影响程度。Minitab 17软件已用于此。最后,确定了各工艺参数对蒸发器性能特性的相对贡献。
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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