{"title":"热管中冷旋转填料床中试碳捕集","authors":"James R. Hendry*, and , Jonathan G.M. Lee, ","doi":"10.1021/acs.iecr.4c0161410.1021/acs.iecr.4c01614","DOIUrl":null,"url":null,"abstract":"<p >The equipment size and energy penalties of carbon-capture processes can be reduced substantially by using rotating packed beds (RPB) and high-concentration amines. However, intercooling the absorption process is necessary to remove the heat-of-reaction that would otherwise halt CO<sub>2</sub> absorption in full-scale processes. This paper presents pilot-scale experimental results in carbon capture, using a novel intercooled RPB rotor design that incorporates thermosyphon heat pipes and a variable-area packing. Tests outline the performance benefits of the design and present a correlation for the effects of rotation speed and liquid flow on overall gas-side mass-transfer coefficient (K<sub>g</sub>a<sub>e</sub>). The results show that K<sub>g</sub>a<sub>e</sub> is improved by 130% in comparison to previous conventional RPB rotor designs, providing an experimental demonstration of the benefits of intercooled RPBs in intensified carbon-capture processes.</p>","PeriodicalId":39,"journal":{"name":"Industrial & Engineering Chemistry Research","volume":"64 5","pages":"2872–2879 2872–2879"},"PeriodicalIF":3.9000,"publicationDate":"2025-01-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acs.iecr.4c01614","citationCount":"0","resultStr":"{\"title\":\"Pilot-Scale Carbon Capture in a Heat-Pipe-Intercooled Rotating Packed Bed\",\"authors\":\"James R. Hendry*, and , Jonathan G.M. Lee, \",\"doi\":\"10.1021/acs.iecr.4c0161410.1021/acs.iecr.4c01614\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p >The equipment size and energy penalties of carbon-capture processes can be reduced substantially by using rotating packed beds (RPB) and high-concentration amines. However, intercooling the absorption process is necessary to remove the heat-of-reaction that would otherwise halt CO<sub>2</sub> absorption in full-scale processes. This paper presents pilot-scale experimental results in carbon capture, using a novel intercooled RPB rotor design that incorporates thermosyphon heat pipes and a variable-area packing. Tests outline the performance benefits of the design and present a correlation for the effects of rotation speed and liquid flow on overall gas-side mass-transfer coefficient (K<sub>g</sub>a<sub>e</sub>). The results show that K<sub>g</sub>a<sub>e</sub> is improved by 130% in comparison to previous conventional RPB rotor designs, providing an experimental demonstration of the benefits of intercooled RPBs in intensified carbon-capture processes.</p>\",\"PeriodicalId\":39,\"journal\":{\"name\":\"Industrial & Engineering Chemistry Research\",\"volume\":\"64 5\",\"pages\":\"2872–2879 2872–2879\"},\"PeriodicalIF\":3.9000,\"publicationDate\":\"2025-01-23\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://pubs.acs.org/doi/epdf/10.1021/acs.iecr.4c01614\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Industrial & Engineering Chemistry Research\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://pubs.acs.org/doi/10.1021/acs.iecr.4c01614\",\"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}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Industrial & Engineering Chemistry Research","FirstCategoryId":"5","ListUrlMain":"https://pubs.acs.org/doi/10.1021/acs.iecr.4c01614","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}
Pilot-Scale Carbon Capture in a Heat-Pipe-Intercooled Rotating Packed Bed
The equipment size and energy penalties of carbon-capture processes can be reduced substantially by using rotating packed beds (RPB) and high-concentration amines. However, intercooling the absorption process is necessary to remove the heat-of-reaction that would otherwise halt CO2 absorption in full-scale processes. This paper presents pilot-scale experimental results in carbon capture, using a novel intercooled RPB rotor design that incorporates thermosyphon heat pipes and a variable-area packing. Tests outline the performance benefits of the design and present a correlation for the effects of rotation speed and liquid flow on overall gas-side mass-transfer coefficient (Kgae). The results show that Kgae is improved by 130% in comparison to previous conventional RPB rotor designs, providing an experimental demonstration of the benefits of intercooled RPBs in intensified carbon-capture processes.
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.