IF 3.8 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Paolo Deiana, Leonardo Colelli, Claudia Bassano, Yuri De Pra, Giovanni Testa, Nicola Verdone, Giorgio Vilardi
{"title":"Power to Gas Pilot Plant for CO2 Methanation with a Ni-Based Catalyst","authors":"Paolo Deiana, Leonardo Colelli, Claudia Bassano, Yuri De Pra, Giovanni Testa, Nicola Verdone, Giorgio Vilardi","doi":"10.1021/acs.iecr.4c03289","DOIUrl":null,"url":null,"abstract":"In the context of power to gas (PtG) technology, different studies are developed to convert carbon dioxide and hydrogen into methane (synthetic natural gas, SNG). The aim of this technology consists of storing renewable energy and reducing greenhouse gas emissions with a net zero process. The present study focuses on the analysis of a small pilot plant designed for the methanation of CO<sub>2</sub> to produce synthetic methane. The size of this plant is set to produce 1 Nm<sup>3</sup>/h of synthetic methane by using a monotube plug flow reactor (PFR) filled with a Ni-based catalyst, which allows the CO<sub>2</sub> methanation to occur according to the Sabatier reaction. The study analyzes various process parameters over a 10 h period to assess the system’s dynamic behavior, including CO<sub>2</sub> conversion and CH<sub>4</sub> content. The experimental setup features enhanced temperature control through a diathermic oil circuit and optimized reactor design, ensuring stability and reducing hot spot risks. This configuration minimizes pressure drops, leading to an efficient performance. During the process, CO<sub>2</sub> conversion of approximately 70% and CH<sub>4</sub> composition of 63.4 vol % are reached. Overall, the system effectively handles fluctuations in renewable energy supply and demonstrates operability under constant reactants flowrates.","PeriodicalId":39,"journal":{"name":"Industrial & Engineering Chemistry Research","volume":"8 1","pages":""},"PeriodicalIF":3.8000,"publicationDate":"2025-02-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Industrial & Engineering Chemistry Research","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1021/acs.iecr.4c03289","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0

摘要

在 "电转气"(PtG)技术方面,已经开展了将二氧化碳和氢气转化为甲烷(合成天然气,SNG)的不同研究。这项技术的目的是储存可再生能源,并以净零工艺减少温室气体排放。本研究的重点是分析设计用于将二氧化碳甲烷化以生产合成甲烷的小型试验工厂。该装置采用单管塞流反应器 (PFR),内装镍基催化剂,可根据萨巴蒂尔反应进行二氧化碳甲烷化,其规模为每小时生产 1 Nm3 合成甲烷。研究分析了 10 小时内的各种工艺参数,以评估系统的动态行为,包括 CO2 转化率和 CH4 含量。实验装置通过双热油路和优化的反应器设计加强了温度控制,确保了稳定性并降低了热点风险。这种配置最大限度地减少了压降,从而实现了高效的性能。在此过程中,二氧化碳转化率达到约 70%,CH4 成分达到 63.4 vol%。总之,该系统能有效地应对可再生能源供应的波动,并证明了在反应物流量恒定的情况下的可操作性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Power to Gas Pilot Plant for CO2 Methanation with a Ni-Based Catalyst

Power to Gas Pilot Plant for CO2 Methanation with a Ni-Based Catalyst
In the context of power to gas (PtG) technology, different studies are developed to convert carbon dioxide and hydrogen into methane (synthetic natural gas, SNG). The aim of this technology consists of storing renewable energy and reducing greenhouse gas emissions with a net zero process. The present study focuses on the analysis of a small pilot plant designed for the methanation of CO2 to produce synthetic methane. The size of this plant is set to produce 1 Nm3/h of synthetic methane by using a monotube plug flow reactor (PFR) filled with a Ni-based catalyst, which allows the CO2 methanation to occur according to the Sabatier reaction. The study analyzes various process parameters over a 10 h period to assess the system’s dynamic behavior, including CO2 conversion and CH4 content. The experimental setup features enhanced temperature control through a diathermic oil circuit and optimized reactor design, ensuring stability and reducing hot spot risks. This configuration minimizes pressure drops, leading to an efficient performance. During the process, CO2 conversion of approximately 70% and CH4 composition of 63.4 vol % are reached. Overall, the system effectively handles fluctuations in renewable energy supply and demonstrates operability under constant reactants flowrates.
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
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and 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:481959085
Book学术官方微信