A new model for thermodynamic analysis of a drying process

被引:269
作者
Dincer, I
Sahin, AZ
机构
[1] Univ Ontario, Sch Mfg Engn, Inst Technol, Oshawa, ON L1H 7K4, Canada
[2] King Fahd Univ Petr & Minerals, Dept Mech Engn, Dhahran 31261, Saudi Arabia
关键词
D O I
10.1016/j.ijheatmasstransfer.2003.08.013
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this paper we present a new model for thermodynamic analysis, in terms of exergy, of a drying process. Exergy efficiencies are derived as functions of heat and mass transfer parameters. An illustrative example is considered to verify the present model and to illustrate the applicability of the model to actual drying processes at different drying air temperatures, specific exergies of drying air, exergy differences of inlet and outlet products, product weights, moisture contents of drying air, and humidity ratios of drying air. As a result, this work is intended not only to demonstrate the usefulness of exergy analysis in thermodynamic assessments of drying processes, but also to provide insights into their performances and efficiencies. It is believed that the present model should be useful to people seeking (i) to optimize the design of drying systems and their components and (ii) to identify appropriate applications and optimal configurations for drying systems. (C) 2003 Elsevier Ltd. All rights reserved.
引用
收藏
页码:645 / 652
页数:8
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