Advancing CO2 Capture from Natural Gas Combined Cycle Power Plants with Piperazine Scrubbing

B. Pun, Ibrahim Ali, R. Jadhav, G. Moure, E. Chen, Joseph L. Selinger, Yue Zhang, G. Rochelle
{"title":"Advancing CO2 Capture from Natural Gas Combined Cycle Power Plants with Piperazine Scrubbing","authors":"B. Pun, Ibrahim Ali, R. Jadhav, G. Moure, E. Chen, Joseph L. Selinger, Yue Zhang, G. Rochelle","doi":"10.2139/ssrn.3365573","DOIUrl":null,"url":null,"abstract":"Carbon dioxide capture and storage is widely recognized as an essential technology for limiting the global temperature rise to 2 °C by the end of the century. Technology development efforts so far focus on coal-fired power plants and other industrial sources with relatively high CO2 partial pressures. However, natural gas is increasingly used in power generation because of its abundance and low greenhouse gas impacts among the fossil fuels. For deep decarbonization that is required in the future, fossil fuels with CCS continue to play a relevant role in scenarios that balance cost of energy with climate impacts. \n \nCarbon capture from natural gas sources has been an ongoing interest to CO2 Capture Project (CCP) and its members from the oil and gas industry. This paper describes the work related to solvent-based natural gas carbon capture sponsored by CCP and pilot studies performed in collaboration with University of Texas at Austin researchers. \n \nThe collaboration with University of Texas at Austin (UT) is aimed at demonstrating the application of an aqueous piperazine solution-a second-generation solvent-in a pilot plant. The goal is to test CO2 separation from synthetic flue gas representative of the exhausts from natural gas-fired combined cycle power plant (i.e. ~4 mol% CO2). The low CO2 concentration in NGCC flue gas is considered to be a challenge for many capture technologies. This work tested the performance of 5m piperazine in the UT pilot plant at a range of operating conditions, including solvent loadings, gas and liquid flow rates, assessing two different absorber configurations. High CO2 capture rates above 90% were confirmed. The pilot test results were used to verify and extend the range of applicability of the thermodynamic model developed by UT. This work increases the confidence for the application of the process models to design CCS processes for low CO2 concentrations. The model’s predictions of the pilot plant tests at low concentrations are now as accurate and reliable as those for higher CO2 concentrations where much of the data have been collected until now. Further pilot tests at NCCC are being designed to supplement the model evaluation data set for NGCC flue gas as well as to address questions related to oxidation/corrosion and cooling scheme optimization for NGCC applications.","PeriodicalId":411095,"journal":{"name":"EngRN: Natural Gas Engineering (Topic)","volume":"40 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2018-10-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"EngRN: Natural Gas Engineering (Topic)","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.2139/ssrn.3365573","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0

Abstract

Carbon dioxide capture and storage is widely recognized as an essential technology for limiting the global temperature rise to 2 °C by the end of the century. Technology development efforts so far focus on coal-fired power plants and other industrial sources with relatively high CO2 partial pressures. However, natural gas is increasingly used in power generation because of its abundance and low greenhouse gas impacts among the fossil fuels. For deep decarbonization that is required in the future, fossil fuels with CCS continue to play a relevant role in scenarios that balance cost of energy with climate impacts. Carbon capture from natural gas sources has been an ongoing interest to CO2 Capture Project (CCP) and its members from the oil and gas industry. This paper describes the work related to solvent-based natural gas carbon capture sponsored by CCP and pilot studies performed in collaboration with University of Texas at Austin researchers. The collaboration with University of Texas at Austin (UT) is aimed at demonstrating the application of an aqueous piperazine solution-a second-generation solvent-in a pilot plant. The goal is to test CO2 separation from synthetic flue gas representative of the exhausts from natural gas-fired combined cycle power plant (i.e. ~4 mol% CO2). The low CO2 concentration in NGCC flue gas is considered to be a challenge for many capture technologies. This work tested the performance of 5m piperazine in the UT pilot plant at a range of operating conditions, including solvent loadings, gas and liquid flow rates, assessing two different absorber configurations. High CO2 capture rates above 90% were confirmed. The pilot test results were used to verify and extend the range of applicability of the thermodynamic model developed by UT. This work increases the confidence for the application of the process models to design CCS processes for low CO2 concentrations. The model’s predictions of the pilot plant tests at low concentrations are now as accurate and reliable as those for higher CO2 concentrations where much of the data have been collected until now. Further pilot tests at NCCC are being designed to supplement the model evaluation data set for NGCC flue gas as well as to address questions related to oxidation/corrosion and cooling scheme optimization for NGCC applications.
利用哌嗪洗涤技术推进天然气联合循环电厂二氧化碳捕集
二氧化碳捕获和储存被广泛认为是到本世纪末将全球气温上升限制在2°C以内的一项关键技术。迄今为止,技术开发的重点是燃煤电厂和其他二氧化碳分压相对较高的工业来源。然而,在化石燃料中,天然气因其储量丰富且温室气体排放量低而越来越多地用于发电。对于未来需要的深度脱碳,具有CCS的化石燃料将继续在平衡能源成本和气候影响的情景中发挥重要作用。从天然气中捕获碳一直是二氧化碳捕获项目(CCP)及其石油和天然气行业成员的兴趣所在。本文描述了由CCP赞助的溶剂型天然气碳捕集的相关工作,以及与德克萨斯大学奥斯汀分校的研究人员合作进行的试点研究。与德克萨斯大学奥斯汀分校(UT)的合作旨在演示第二代溶剂——哌嗪水溶液在中试工厂的应用。目的是测试从天然气联合循环发电厂废气的合成烟气中分离CO2(即~4 mol% CO2)。NGCC烟气中的低二氧化碳浓度被认为是许多捕集技术面临的挑战。这项工作在UT中试装置中测试了5m哌嗪在一系列操作条件下的性能,包括溶剂负载、气体和液体流速,评估了两种不同的吸收器配置。二氧化碳捕获率高达90%以上。利用中试结果验证和扩展了UT开发的热力学模型的适用范围。这项工作增加了应用过程模型设计低二氧化碳浓度CCS过程的信心。目前,该模型对低浓度试点工厂试验的预测与迄今为止收集的大部分数据的高浓度二氧化碳试验的预测一样准确和可靠。正在设计在国家天然气加工中心进行的进一步试点测试,以补充国家天然气加工中心烟气模型评估数据集,并解决与氧化/腐蚀和优化国家天然气加工中心应用的冷却方案有关的问题。
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
自引率
0.00%
发文量
0
×
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