Energy-Efficient Helium Extraction and Boil-off Gas Recovery from Liquefied Natural Gas Based on Low-Temperature Pressure Swing Adsorption

Helium is widely used in industry, but extraction of it from natural gas remains complex and energy-intensive. This work proposes an energy-saving helium extraction and boil-off gas (BOG) recovery process based on low-temperature pressure swing adsorption (PSA). The integrated scheme combines BOG recovery and compression, crude helium separation, catalytic dehydrogenation and drying, and low-temperature PSA purification using LNG cold energy. BOG is primarily adsorbed and recovered in the first-stage PSA, while helium is enriched and purified through a two-stage low-temperature PSA system, achieving crude helium separation with a helium content above 2.71% and final helium purity up to 99.99%. Numerical energy and exergy analyses show a unit energy consumption of 6.54 kWh/m3, 21.7% lower than a conventional liquefaction-based process, with cold energy utilization efficiency improved by 21.6%.

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Publication Details

Journal
Industrial & Engineering Chemistry Research
Published
2026-02-17
DOI
https://doi.org/10.1021/acs.iecr.5c03057
Primary Topic
Carbon Dioxide Capture Technologies
Type
article
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article

Energy-Efficient Helium Extraction and Boil-off Gas Recovery from Liquefied Natural Gas Based on Low-Temperature Pressure Swing Adsorption

Yongxiang Zhu, Qi Hong, Jiake Wu, Long Jiang
Industrial & Engineering Chemistry Research
Carbon Dioxide Capture Technologies
article

Energy-Efficient Helium Extraction and Boil-off Gas Recovery from Liquefied Natural Gas Based on Low-Temperature Pressure Swing Adsorption

Yongxiang Zhu, Qi Hong, Jiake Wu, Long Jiang
article en

Abstract

Helium is widely used in industry, but extraction of it from natural gas remains complex and energy-intensive. This work proposes an energy-saving helium extraction and boil-off gas (BOG) recovery process based on low-temperature pressure swing adsorption (PSA). The integrated scheme combines BOG recovery and compression, crude helium separation, catalytic dehydrogenation and drying, and low-temperature PSA purification using LNG cold energy. BOG is primarily adsorbed and recovered in the first-stage PSA, while helium is enriched and purified through a two-stage low-temperature PSA system, achieving crude helium separation with a helium content above 2.71% and final helium purity up to 99.99%. Numerical energy and exergy analyses show a unit energy consumption of 6.54 kWh/m3, 21.7% lower than a conventional liquefaction-based process, with cold energy utilization efficiency improved by 21.6%.

Industrial & Engineering Chemistry ResearchVol. 65(8)
Qinghai New Energy (China) (CN), Institute of Refrigeration (GB), Zhejiang University (CN)
Affordable and clean energy
Openalex Percentile: Top 54%
Carbon Dioxide Capture Technologies
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