4.7 Article

Simulation and energy consumption analysis of chemical looping air separation system on Aspen Plus

期刊

JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY
卷 124, 期 3, 页码 1555-1560

出版社

SPRINGER
DOI: 10.1007/s10973-016-5237-9

关键词

Chemical looping air separation; Oxygen carrier; Simulation; Energy consumption; Aspen Plus

资金

  1. National Natural Science Foundation of China [51576035]
  2. National Science & Technology Pillar Program of China [2013BAA03B03]

向作者/读者索取更多资源

Chemical looping air separation is a new method to separate oxygen from air. In the process, oxygen carrier releases oxygen in the reduction reactor and absorbs oxygen in the oxidation reactor. The reduction is endothermic, and the oxidation is exothermic. The heat transfer from oxidation reactor to reduction reactor is essential to design the CLAS process with low energy consumption. In this paper, the optimization CLAS process of CuO/ZrO2 oxygen carrier was established based on thermal analysis and pressure analysis. In the system, the heat can achieve self-balance with little heat supplied from outside. The effects of the technological parameters on the system energy consumption were investigated using Aspen Plus software. The results show that the energy consumption decreases with reduction temperature increasing and oxidation temperature decreasing. Moreover, the smaller the difference of temperature between the two reactors is, the lower energy consumption is. Under negative pressure, with the decreasing reduction pressure, the energy consumption decreases. Under positive pressure, with the increasing oxidation pressure, the energy consumption decreases firstly and then increases. The optimization operating parameters are obtained. The lowest energy consumption of the system is 0.132 kWh m(-3) at the conditions of 990 degrees C reduction and 1000 degrees C oxidation temperatures and 0.5 atm. reduction and 1.7 atm. oxidation pressures.

作者

我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。

评论

主要评分

4.7
评分不足

次要评分

新颖性
-
重要性
-
科学严谨性
-
评价这篇论文

推荐

暂无数据
暂无数据