Dual-reflux pressure swing adsorption in biogas upgrading—a parametric optimization

IF 4.1 4区 工程技术 Q3 ENERGY & FUELS
Mohd Hardyianto Vai Bahrun, Awang Bono, Norasikin Othman, Muhammad Abbas Ahmad Zaini
{"title":"Dual-reflux pressure swing adsorption in biogas upgrading—a parametric optimization","authors":"Mohd Hardyianto Vai Bahrun,&nbsp;Awang Bono,&nbsp;Norasikin Othman,&nbsp;Muhammad Abbas Ahmad Zaini","doi":"10.1007/s13399-025-06727-x","DOIUrl":null,"url":null,"abstract":"<div><p>The efficient upgrading of biogas is critical for advancing renewable energy technologies, reducing greenhouse gas emissions, and enhancing the circular carbon economy. This study systematically investigates the application of dual-reflux pressure swing adsorption (DR-PSA) for biogas upgrading, enabling simultaneous enrichment of CH<sub>4</sub> and CO<sub>2</sub> to high purities. A two-bed, six-step P<sub>H</sub>A (feed to high-pressure, <i>P</i><sub><i>H</i></sub>, and pressure reversal using heavy component, A) was analyzed using rigorous non-isothermal numerical simulations framework within the Aspen Adsorption software. To systematically enhance the process performance, a two-level fractional factorial design was employed to identify the most influential parameters, followed by the Box-Behnken design optimization to determine optimal operating conditions. The screening analysis identified the feed/light reflux (FE/LR) time, light reflux ratio, and bed column height as the most influential parameters governing separation efficiency. Under optimized conditions of FE/LR time of 49 s, light reflux ratio of 0.259, and bed column height of 1.97 m, the DR-PSA achieved a CH<sub>4</sub> purity of 91.69% in the light product and CO<sub>2</sub> purity of 89.36% in the heavy product, marking improvements of 15% and 19%, respectively, over the base case. Additionally, the optimized conditions demonstrated a bed productivity of 1.09 mol CH<sub>4</sub>/h/kg silica gel and an energy-efficient cycle work of 56.25 kJ/mol CH<sub>4</sub> captured, highlighting its potential for scalable deployment. Compared to other PSA systems of similar purpose, the DR-PSA process exhibited comparable separation performance, operating as a single train process, with a moderate pressure ratio, and without vacuum operation, making it a promising alternative for sustainable and cost-effective biogas upgrading. This study represents the first systematic optimization of DR-PSA for biogas upgrading using a statistical design of experiments approach, offering a novel and practical pathway for enhancing renewable energy technologies.</p></div>","PeriodicalId":488,"journal":{"name":"Biomass Conversion and Biorefinery","volume":"15 16","pages":"22987 - 23016"},"PeriodicalIF":4.1000,"publicationDate":"2025-03-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Biomass Conversion and Biorefinery","FirstCategoryId":"5","ListUrlMain":"https://link.springer.com/article/10.1007/s13399-025-06727-x","RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0

Abstract

The efficient upgrading of biogas is critical for advancing renewable energy technologies, reducing greenhouse gas emissions, and enhancing the circular carbon economy. This study systematically investigates the application of dual-reflux pressure swing adsorption (DR-PSA) for biogas upgrading, enabling simultaneous enrichment of CH4 and CO2 to high purities. A two-bed, six-step PHA (feed to high-pressure, PH, and pressure reversal using heavy component, A) was analyzed using rigorous non-isothermal numerical simulations framework within the Aspen Adsorption software. To systematically enhance the process performance, a two-level fractional factorial design was employed to identify the most influential parameters, followed by the Box-Behnken design optimization to determine optimal operating conditions. The screening analysis identified the feed/light reflux (FE/LR) time, light reflux ratio, and bed column height as the most influential parameters governing separation efficiency. Under optimized conditions of FE/LR time of 49 s, light reflux ratio of 0.259, and bed column height of 1.97 m, the DR-PSA achieved a CH4 purity of 91.69% in the light product and CO2 purity of 89.36% in the heavy product, marking improvements of 15% and 19%, respectively, over the base case. Additionally, the optimized conditions demonstrated a bed productivity of 1.09 mol CH4/h/kg silica gel and an energy-efficient cycle work of 56.25 kJ/mol CH4 captured, highlighting its potential for scalable deployment. Compared to other PSA systems of similar purpose, the DR-PSA process exhibited comparable separation performance, operating as a single train process, with a moderate pressure ratio, and without vacuum operation, making it a promising alternative for sustainable and cost-effective biogas upgrading. This study represents the first systematic optimization of DR-PSA for biogas upgrading using a statistical design of experiments approach, offering a novel and practical pathway for enhancing renewable energy technologies.

双回流变压吸附在沼气提质过程中的参数优化研究
沼气的有效升级对于推进可再生能源技术、减少温室气体排放和加强循环碳经济至关重要。本研究系统地研究了双回流变压吸附(DR-PSA)在沼气升级中的应用,使CH4和CO2同时富集到高纯度。在Aspen吸附软件中使用严格的非等温数值模拟框架分析了一个两床、六步PHA(进料到高压、PH和使用重组分A的压力反转)。为了系统地提高工艺性能,采用两水平分数因子设计来确定最具影响的参数,然后采用Box-Behnken设计优化来确定最佳操作条件。筛选分析表明,进料/光回流(FE/LR)时间、光回流比和床柱高度是影响分离效率的主要参数。在FE/LR时间为49 s、轻回流比为0.259、床柱高度为1.97 m的优化条件下,DR-PSA轻产物中CH4纯度为91.69%,重产物中CO2纯度为89.36%,分别比基准情况提高了15%和19%。此外,优化后的条件表明,床层产能为1.09 mol CH4/h/kg硅胶,捕获的节能循环功为56.25 kJ/mol CH4,突出了其可扩展部署的潜力。与其他类似目的的PSA系统相比,DR-PSA工艺具有相当的分离性能,作为单一流程运行,压力比适中,不需要真空操作,使其成为可持续且具有成本效益的沼气升级替代方案。本研究首次采用实验统计设计方法对DR-PSA进行了系统优化,为提高可再生能源技术提供了一条新颖实用的途径。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 求助全文
来源期刊
Biomass Conversion and Biorefinery
Biomass Conversion and Biorefinery Energy-Renewable Energy, Sustainability and the Environment
CiteScore
7.00
自引率
15.00%
发文量
1358
期刊介绍: Biomass Conversion and Biorefinery presents articles and information on research, development and applications in thermo-chemical conversion; physico-chemical conversion and bio-chemical conversion, including all necessary steps for the provision and preparation of the biomass as well as all possible downstream processing steps for the environmentally sound and economically viable provision of energy and chemical products.
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:604180095
Book学术官方微信