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贫氦管输天然气提氦多元化产品耦合工艺优化设计

郭明钢 杨晓航 代岩 米盼盼 马世鑫 贺高红 肖武 崔福军

化工学报2025,Vol.76Issue(5):2251-2261,11.
化工学报2025,Vol.76Issue(5):2251-2261,11.DOI:10.11949/0438-1157.20240772

贫氦管输天然气提氦多元化产品耦合工艺优化设计

Optimal design of integration process for helium extraction from helium-poor pipeline natural gas with diversified products

郭明钢 1杨晓航 2代岩 2米盼盼 2马世鑫 3贺高红 1肖武 4崔福军2

作者信息

  • 1. 大连理工大学精细化工国家重点实验室,辽宁 大连 116024||大连理工大学盘锦产业技术研究院,辽宁 盘锦 124221
  • 2. 大连理工大学盘锦产业技术研究院,辽宁 盘锦 124221
  • 3. 沈阳化工大学化学工程学院,辽宁 沈阳 110142
  • 4. 大连理工大学精细化工国家重点实验室,辽宁 大连 116024
  • 折叠

摘要

Abstract

At present,there are some problems in the helium extraction process,such as excessive dependence on the helium-rich tail gas from liquefied natural gas production process,the introduction of new impurities by catalytic oxidation destructive dehydrogenation and high energy consumption.Therefore,a multi-stage membrane-electrochemical hydrogen pump-adsorption helium extraction integration process based on a wide range of resources for helium-poor pipeline natural gas was proposed to produce diversified products of He,H2,and CO2 by utilizing the pressure of the pipeline natural gas and a multi-technology gradient productization strategy of removing impurities and extracting helium,so as to realize the economic helium extraction from helium-poor pipeline natural gas.Aspen HYSYS software was used to simulate and optimize the helium extraction integration process for 1.00×105 m3/h helium-poor pipeline natural gas,and the effects of the recovery,membrane performance,and helium concentration on the process economy were investigated.The simulation results show that,at a typical pipeline natural gas pressure of 4.0 MPa and 0.04%(vol)He,the helium extraction integration process for helium-poor pipeline natural gas is more economical with the medium-permeable and medium-selective gas separation membrane,and the helium recovery rate is 50%—70%,the break-even price of helium is 115.5-123.2 CNY/m3,and the break-even price gradually decreases as the helium concentration increases,providing a technological route with great industrial prospects for the economic utilization of helium-poor resources.

关键词

天然气/优化设计//氦气/电化学氢泵/过程强化

Key words

natural gas/optimal design/membranes/helium/electrochemical hydrogen pump/process intensification

分类

化学化工

引用本文复制引用

郭明钢,杨晓航,代岩,米盼盼,马世鑫,贺高红,肖武,崔福军..贫氦管输天然气提氦多元化产品耦合工艺优化设计[J].化工学报,2025,76(5):2251-2261,11.

基金项目

国家自然科学基金项目(22141001) (22141001)

国家自然科学基金创新群体项目(22021005) (22021005)

营口市企业博士双创计划项目(YKSCJH2023-011) (YKSCJH2023-011)

化工学报

OA北大核心

0438-1157

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