化工学报 ›› 2018, Vol. 69 ›› Issue (10): 4342-4352.DOI: 10.11949/j.issn.0438-1157.20180512

• 能源和环境工程 • 上一篇    下一篇

基于乙醇压缩的超重力热泵精馏热集成系统性能分析

刘军1,2,3, 张钰1,3, 毛祥1,3,4, 张振涛1,3, 杨鲁伟1,3,4   

  1. 1. 中国科学院理化技术研究所, 北京 100190;
    2. 北京林业大学材料科学与技术学院, 北京 100083;
    3. 热力过程节能技术北京市重点实验室, 北京 100190;
    4. 中国科学院大学, 北京 100049
  • 收稿日期:2018-05-15 修回日期:2018-07-28 出版日期:2018-10-05 发布日期:2018-10-05
  • 通讯作者: 张振涛
  • 基金资助:

    国家重点研发计划项目(2016YFC1402500)。

Performance analysis of high-gravity heat pump distillation heat integrated system based on ethanol compression

LIU Jun1,2,3, ZHANG Yu1,3, MAO Xiang1,3,4, ZHANG Zhentao1,3, YANG Luwei1,3,4   

  1. 1. Technical Institute of Physics and Chemistry, Chinese Academy of Sciences, Beijing 100190, China;
    2. College of Materials Science and Technology, Beijing Forestry University, Beijing 100083, China;
    3. Beijing Key Laboratory of Thermal Science and Technology, Beijing 100190, China;
    4. University of Chinese Academy of Sciences, Beijing 100049, China
  • Received:2018-05-15 Revised:2018-07-28 Online:2018-10-05 Published:2018-10-05
  • Supported by:

    supported by the National Key Project of Research and Development Plan (2016YFC1402500).

摘要:

将超重力精馏塔、单螺杆压缩机与新型热泵工艺技术创新性地相结合,提出超重力热泵精馏的概念。设计并搭建一套处理量为300 kg·h-1的超重力热泵精馏热集成系统。以乙醇-水溶液为研究对象,使用单螺杆压缩机直接压缩乙醇蒸气。通过对超重力精馏塔不同转动频率的全回流实验和工业条件下系统的不同进料位置、不同回流比实验的研究,综合分析系统各影响参数的变化情况、节能特性和经济效益。结果表明,fHG在40 Hz下运转时系统性能最佳;进料位置下移或增加回流比,都可提高yD;如果仅从yD值大小考虑,FL03位置最佳;相比于低浓度乙醇-水溶液,处理高浓度优势更大;系统节能及经济效益显著,可为超重力热泵精馏在乙醇精馏的工艺流程选择、设计和应用方面提供理论指导。

关键词: 乙醇, 超重力, 热泵, 精馏, 热集成

Abstract:

Combining with the high-gravity distillation column, single screw compressor and new heat pump technology, and then the concept of high-gravity heat pump distillation was proposed. Firstly, high-gravity heat pump distillation heat integrated system was designed and built, which treatment capacity was about 300 kg·h-1. Ethanol-water solution was taken as the actual research object. The single screw compressor was used to directly compress ethanol vapor. Afterwards, based on the full reflux experiments under the different rotational frequency of high-gravity distillation column, and different feed positions and reflux ratios experiments under the industrial condition, the changes of the affected parameters, energy-saving characteristics and economic benefits of the system were analyzed synthetically. Present results clearly show that the performance of the system is optimal when the frequency of high-gravity distillation column (fHG) is operated at 40 Hz. By moving down the feed position or increasing reflux ratio, mass fraction of the vapor at the top of the column (yD) can be improved. If only yD is considered, feed location 03 (FL03) is the best. In comparison with the low concentration of ethanol-water solution, it has a great advantage in treating the high concentration. In addition, energy-saving and economic benefits of the system are obvious, which can provide theoretical guidance for the high-gravity heat pump distillation in the selection, design and application of the ethanol distillation process.

Key words: ethanol, high-gravity, heat pump, distillation, heat integration

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