...
首页> 外文期刊>Processes >Model-Based Cost Optimization of Double-Effect Water-Lithium Bromide Absorption Refrigeration Systems
【24h】

Model-Based Cost Optimization of Double-Effect Water-Lithium Bromide Absorption Refrigeration Systems

机译:双模型水-溴化锂吸收式制冷系统的基于模型的成本优化

获取原文
   

获取外文期刊封面封底 >>

       

摘要

This work presents optimization results obtained for a double-effect H 2 O-LiBr absorption refrigeration system considering the total cost as minimization criterion, for a wide range of cooling capacity values. As a model result, the sizes of the process units and the corresponding operating conditions are obtained simultaneously. In this paper, the effectiveness factor of each proposed heat exchanger is considered as a model optimization variable which allows (if beneficial, according to the objective function to be minimized) its deletion from the optimal solution, therefore, helping us to determine the optimal configuration. Several optimization cases considering different target levels of cooling capacity are solved. Among the major results, it was observed that the total cost is considerably reduced when the solution heat exchanger operating at low temperature is deleted compared to the configuration that includes it. Also, it was found that the effect of removing this heat exchanger is comparatively more significant with increasing cooling capacity levels. A reduction of 9.8% in the total cost was obtained for a cooling capacity of 16 kW (11,537.2 $·year ?1 vs. 12,794.5 $·year ?1 ), while a reduction of 12% was obtained for a cooling capacity of 100 kW (31,338.1 $·year ?1 vs. 35,613.9 $·year ?1 ). The optimization mathematical model presented in this work assists in selecting the optimal process configuration, as well as determining the optimal process unit sizes and operating conditions of refrigeration systems.
机译:这项工作提出了以总成本作为最小化标准的双效H 2 O-LiBr吸收式制冷系统获得的优化结果,适用于各种制冷量值。作为模型结果,可以同时获得处理单元的大小和相应的操作条件。在本文中,每个拟议的换热器的效率因子均被视为模型优化变量,该变量允许(如果有益的话,根据目标函数将其最小化)从最佳解决方案中删除,因此有助于我们确定最佳配置。解决了考虑不同制冷量目标水平的几种优化案例。在主要结果中,观察到,与包括它的构造相比,当删除在低温下运行的溶液热交换器时,总成本大大降低。另外,发现随着冷却能力水平的提高,去除该热交换器的效果相对更显着。制冷能力为16 kW时,总成本降低了9.8%(11,537.2 $·年-1与12,794.5 $·年-1),而制冷量为100 kW的降低了12% (31,338.1 $·年1与35,613.9 $·年1)。在这项工作中提出的优化数学模型有助于选择最佳的过程配置,以及确定最佳的过程单元尺寸和制冷系统的运行条件。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号