中间气两步充压对快速真空变压吸附制氧的影响

祝显强; 刘应书; 杨雄; 刘文海; 李永玲

doi:10.11949/j.issn.0438-1157.20160191

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中间气两步充压对快速真空变压吸附制氧的影响

分离工程 | 更新时间：2025-11-26

- 中间气两步充压对快速真空变压吸附制氧的影响
- Effect of two-step pressurization with intermediate gas on rapid vacuum pressure swing adsorption process for oxygen generation
- 化工学报 2016年67卷第10期页码：4264-4272
- 作者机构：
  
  1. 北京科技大学能源与环境工程学院,北京,100083
  2. 江苏昊泰气体设备科技有限公司, 江苏丹阳,212300
  3. 北京科技大学冶金工业节能减排北京市重点实验室,北京,100083
- 作者简介：
- 基金信息：
- DOI：10.11949/j.issn.0438-1157.20160191
  中图分类号： Q028.1
- 网络首发：2016-10-05，
  
  纸质出版：2016-10-05
- 稿件说明：
移动端阅览
祝显强, 刘应书, 杨雄, 等. 中间气两步充压对快速真空变压吸附制氧的影响[J]. 化工学报, 2016,67(10):4264-4272.

ZHU Xianqiang, LIU Yingshu, YANG Xiong, et al. Effect of two-step pressurization with intermediate gas on rapid vacuum pressure swing adsorption process for oxygen generation[J]. CIESC Journal, 2016, 67(10): 4264-4272.
祝显强, 刘应书, 杨雄, 等. 中间气两步充压对快速真空变压吸附制氧的影响[J]. 化工学报, 2016,67(10):4264-4272. DOI： 10.11949/j.issn.0438-1157.20160191.

ZHU Xianqiang, LIU Yingshu, YANG Xiong, et al. Effect of two-step pressurization with intermediate gas on rapid vacuum pressure swing adsorption process for oxygen generation[J]. CIESC Journal, 2016, 67(10): 4264-4272. DOI： 10.11949/j.issn.0438-1157.20160191.

摘要

针对快速变压吸附制氧浓度和回收率低问题，提出了用于提高产氧浓度和回收率的中间气两步充压的快速真空变压吸附流程，并对该流程进行了研究。结果表明：在快速真空变压吸附制氧过程中，中间气先在出气端充压可以有效提高产氧浓度，之后再在进气端充压可提高氧气回收率。出气端充压前中间气压力及氧浓度和进气端充压后床层压力是影响产氧浓度和回收率提高的关键参数。当吸附和解吸压力分别为240、60 kPa时，循环氧气回收率为34.57%，且每天产单位吨氧需吸附剂量为61.18 kg·TPD-1。

Abstract

An improved rapid vacuum pressure swing adsorption (RVPSA) process

namely

two-step pressurization with intermediate gas

was proposed to improve performance of miniature oxygen concentrators

which were based on rapid pressure swing adsorption (RPSA) technology. The experimental results on the new process show that pressurization with intermediate gas at the exhaust end could effectively improve oxygen purity and re-pressurization with intermediate gas at the feed end could improve recovery. The pressure and oxygen purity of intermediate gas at the exhaust end before pressurization as well as the bed pressure after re-pressurization of intermediate gas at the feed end were key parameters for improving oxygen purity and recovery of the production. At the adsorption pressure of 240 kPa and the desorption pressure of 60 kPa

the improved RVPSA process exhibited recovery of recycling oxygen up to 34.57% and the BSF at 61.18 kg·TPD-1 for producing a ton of oxygen per day.

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