模拟吸附增强型水气变换中试技术,从废物气化厂生产纯氢

IF 7.2 2区 工程技术 Q1 CHEMISTRY, APPLIED Fuel Processing Technology Pub Date : 2024-01-11 DOI:10.1016/j.fuproc.2024.108032
Barbara Malsegna , Alex Sebastiani , João Guilherme da Gama Paz-Dias , Francesco Di Luca , Andrea Di Giuliano , Katia Gallucci , Massimiliano Materazzi
{"title":"模拟吸附增强型水气变换中试技术,从废物气化厂生产纯氢","authors":"Barbara Malsegna ,&nbsp;Alex Sebastiani ,&nbsp;João Guilherme da Gama Paz-Dias ,&nbsp;Francesco Di Luca ,&nbsp;Andrea Di Giuliano ,&nbsp;Katia Gallucci ,&nbsp;Massimiliano Materazzi","doi":"10.1016/j.fuproc.2024.108032","DOIUrl":null,"url":null,"abstract":"<div><p>This study has analysed and optimised a 5-column sorption enhanced water gas shift (SEWGS) pilot unit, set to operate for the first time in a waste gasification facility for the production of transport-grade hydrogen and CO<sub>2</sub> streams. Full process simulation was undertaken by developing a one-dimensional model of each reactor, with boundary conditions directly informed by real plant operation. From the sensitivity analysis performed, syngas flowrate variations were seen to have a minor but temporary, impact on hydrogen product specifications, while changes to syngas composition were shown to have a longer-lasting effect on system performance. Based on full cycle operation results, the current 5-column SEWGS unit design was concluded to be inadequate for fuel-cell-grade H<sub>2</sub> production, despite obtaining a high H<sub>2</sub> purity of 99.5%, mainly due to its excessive steam consumption. However, the process achieved an exceptionally high CO<sub>2</sub> purity of 99.9%, and 88.6% hydrogen recovery rate, suggesting its potential use in carbon capture and heat-grade hydrogen production applications.</p></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"254 ","pages":"Article 108032"},"PeriodicalIF":7.2000,"publicationDate":"2024-01-11","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://www.sciencedirect.com/science/article/pii/S037838202400002X/pdfft?md5=2d922764731d2cc57ac2801be1966707&pid=1-s2.0-S037838202400002X-main.pdf","citationCount":"0","resultStr":"{\"title\":\"Simulation of a sorption-enhanced water gas-shift pilot technology for pure hydrogen production from a waste gasification plant\",\"authors\":\"Barbara Malsegna ,&nbsp;Alex Sebastiani ,&nbsp;João Guilherme da Gama Paz-Dias ,&nbsp;Francesco Di Luca ,&nbsp;Andrea Di Giuliano ,&nbsp;Katia Gallucci ,&nbsp;Massimiliano Materazzi\",\"doi\":\"10.1016/j.fuproc.2024.108032\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>This study has analysed and optimised a 5-column sorption enhanced water gas shift (SEWGS) pilot unit, set to operate for the first time in a waste gasification facility for the production of transport-grade hydrogen and CO<sub>2</sub> streams. Full process simulation was undertaken by developing a one-dimensional model of each reactor, with boundary conditions directly informed by real plant operation. From the sensitivity analysis performed, syngas flowrate variations were seen to have a minor but temporary, impact on hydrogen product specifications, while changes to syngas composition were shown to have a longer-lasting effect on system performance. Based on full cycle operation results, the current 5-column SEWGS unit design was concluded to be inadequate for fuel-cell-grade H<sub>2</sub> production, despite obtaining a high H<sub>2</sub> purity of 99.5%, mainly due to its excessive steam consumption. However, the process achieved an exceptionally high CO<sub>2</sub> purity of 99.9%, and 88.6% hydrogen recovery rate, suggesting its potential use in carbon capture and heat-grade hydrogen production applications.</p></div>\",\"PeriodicalId\":326,\"journal\":{\"name\":\"Fuel Processing Technology\",\"volume\":\"254 \",\"pages\":\"Article 108032\"},\"PeriodicalIF\":7.2000,\"publicationDate\":\"2024-01-11\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://www.sciencedirect.com/science/article/pii/S037838202400002X/pdfft?md5=2d922764731d2cc57ac2801be1966707&pid=1-s2.0-S037838202400002X-main.pdf\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Fuel Processing Technology\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S037838202400002X\",\"RegionNum\":2,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"CHEMISTRY, APPLIED\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Fuel Processing Technology","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S037838202400002X","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"CHEMISTRY, APPLIED","Score":null,"Total":0}
引用次数: 0

摘要

本研究分析并优化了一个 5 柱吸附增强型水煤气变换 (SEWGS) 试验装置,该装置将首次在废物气化设施中运行,用于生产运输级氢气和二氧化碳流。通过建立每个反应器的一维模型,并根据实际工厂的运行情况直接确定边界条件,进行了全流程模拟。从所进行的敏感性分析来看,合成气流速的变化对氢气产品规格的影响较小,但只是暂时的,而合成气成分的变化则会对系统性能产生较持久的影响。根据全循环运行结果,尽管目前的 5 塔 SEWGS 装置可获得 99.5% 的高纯度氢气,但其设计仍不足以生产燃料电池级氢气,主要原因是蒸汽消耗量过大。不过,该工艺的二氧化碳纯度特别高,达到 99.9%,氢气回收率为 88.6%,这表明它有可能用于碳捕获和热量级氢气生产应用。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
查看原文
分享 分享
微信好友 朋友圈 QQ好友 复制链接
本刊更多论文
Simulation of a sorption-enhanced water gas-shift pilot technology for pure hydrogen production from a waste gasification plant

This study has analysed and optimised a 5-column sorption enhanced water gas shift (SEWGS) pilot unit, set to operate for the first time in a waste gasification facility for the production of transport-grade hydrogen and CO2 streams. Full process simulation was undertaken by developing a one-dimensional model of each reactor, with boundary conditions directly informed by real plant operation. From the sensitivity analysis performed, syngas flowrate variations were seen to have a minor but temporary, impact on hydrogen product specifications, while changes to syngas composition were shown to have a longer-lasting effect on system performance. Based on full cycle operation results, the current 5-column SEWGS unit design was concluded to be inadequate for fuel-cell-grade H2 production, despite obtaining a high H2 purity of 99.5%, mainly due to its excessive steam consumption. However, the process achieved an exceptionally high CO2 purity of 99.9%, and 88.6% hydrogen recovery rate, suggesting its potential use in carbon capture and heat-grade hydrogen production applications.

求助全文
通过发布文献求助,成功后即可免费获取论文全文。 去求助
来源期刊
Fuel Processing Technology
Fuel Processing Technology 工程技术-工程:化工
CiteScore
13.20
自引率
9.30%
发文量
398
审稿时长
26 days
期刊介绍: Fuel Processing Technology (FPT) deals with the scientific and technological aspects of converting fossil and renewable resources to clean fuels, value-added chemicals, fuel-related advanced carbon materials and by-products. In addition to the traditional non-nuclear fossil fuels, biomass and wastes, papers on the integration of renewables such as solar and wind energy and energy storage into the fuel processing processes, as well as papers on the production and conversion of non-carbon-containing fuels such as hydrogen and ammonia, are also welcome. While chemical conversion is emphasized, papers on advanced physical conversion processes are also considered for publication in FPT. Papers on the fundamental aspects of fuel structure and properties will also be considered.
期刊最新文献
Sustainable production of biohydrogen: Feedstock, pretreatment methods, production processes, and environmental impact An experimental evaluation of thermophysical properties of colloidal suspension of carbon-rich fly ash microparticles and single-walled carbon nanotubes in Jet-A fuel and its impact on evaporation and burning rate Microwave-assisted biodiesel synthesis from waste cooking oil: Exploring the potential of carob pod-derived solid base catalyst Direct synthesis of dimethyl carbonate from methanol and carbon dioxide over Co-Ce-Zr ternary metal solid solution A bifunctional catalyst for direct CO2 conversion to clean fuels: Mechanistic insights and a comprehensive kinetic model
×
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
现在去查看 取消
×
提示
确定
0
微信
客服QQ
Book学术公众号 扫码关注我们
反馈
×
意见反馈
请填写您的意见或建议
请填写您的手机或邮箱
已复制链接
已复制链接
快去分享给好友吧!
我知道了
×
扫码分享
扫码分享
Book学术官方微信
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术
文献互助 智能选刊 最新文献 互助须知 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 Book学术 All rights reserved.
ghs 京公网安备 11010802042870号 京ICP备2023020795号-1