Athanasios A. Tountas, Geoffrey A. Ozin and Mohini M. Sain
{"title":"为可持续运输选择液氢载体†","authors":"Athanasios A. Tountas, Geoffrey A. Ozin and Mohini M. Sain","doi":"10.1039/D4SE00731J","DOIUrl":null,"url":null,"abstract":"<p >Liquid hydrogen carriers (LHCs) are important shuttles for molecular hydrogen (H<small><sub>2</sub></small>) as they are convenient to transport as energy-dense liquids over distances greater than 10 000 km. Herein, we provide comprehensive insights into the comparative practicality and safety of irreversible LHCs. From a gas purification standpoint, fewer products in the released H<small><sub>2</sub></small> stream result in less separation complexity and lower cost. Unit operational complexities of methanol (MeOH) steam reforming <em>versus</em> fossil steam-methane reforming were analyzed in depth to highlight gas-cleaning complexities. The main challenge is to estimate the costs of LHC reforming, cleaning and compression (RC&C) steps for H<small><sub>2</sub></small> production in order to break even with other energy scenarios. To achieve this, two techno-economic analyses (TEA) were performed from the ‘vehicle’ and ‘fuel’ points of view. ‘Vehicle’ analysis compares the use of MeOH-to-H<small><sub>2</sub></small> for proton-exchange membrane fuel-cell vehicles (FCVs) with the use of MeOH directly as drop-in fuel for conventional vehicles (ICEVs). ‘Fuel’ analysis compares renewable MeOH and dimethyl ether LHC transport with pressurized and cryogenic H<small><sub>2</sub></small> transport for FCVs. For the analyses in which H<small><sub>2</sub></small> gas is produced as a fuel, RC&C steps are assumed to be accomplished off-board or before fueling the vehicles. ‘Vehicle’ analysis findings indicate that with a moderate tax on carbon emissions, in the year 2035 and beyond, FCVs can be competitive with ICEVs with an RC&C cost of ∼US $ 2–6 per kg H<small><sub>2</sub></small>. From the ‘fuel’ analysis perspective, LHCs break-even with gaseous and liquid H<small><sub>2</sub></small> transport at a more flexible RC&C cost of US $ 7.9–11.4 per kg H<small><sub>2</sub></small>.</p>","PeriodicalId":104,"journal":{"name":"Sustainable Energy & Fuels","volume":" 22","pages":" 5181-5194"},"PeriodicalIF":5.0000,"publicationDate":"2024-09-20","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Choosing a liquid hydrogen carrier for sustainable transportation†\",\"authors\":\"Athanasios A. Tountas, Geoffrey A. Ozin and Mohini M. Sain\",\"doi\":\"10.1039/D4SE00731J\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p >Liquid hydrogen carriers (LHCs) are important shuttles for molecular hydrogen (H<small><sub>2</sub></small>) as they are convenient to transport as energy-dense liquids over distances greater than 10 000 km. Herein, we provide comprehensive insights into the comparative practicality and safety of irreversible LHCs. From a gas purification standpoint, fewer products in the released H<small><sub>2</sub></small> stream result in less separation complexity and lower cost. Unit operational complexities of methanol (MeOH) steam reforming <em>versus</em> fossil steam-methane reforming were analyzed in depth to highlight gas-cleaning complexities. The main challenge is to estimate the costs of LHC reforming, cleaning and compression (RC&C) steps for H<small><sub>2</sub></small> production in order to break even with other energy scenarios. To achieve this, two techno-economic analyses (TEA) were performed from the ‘vehicle’ and ‘fuel’ points of view. ‘Vehicle’ analysis compares the use of MeOH-to-H<small><sub>2</sub></small> for proton-exchange membrane fuel-cell vehicles (FCVs) with the use of MeOH directly as drop-in fuel for conventional vehicles (ICEVs). ‘Fuel’ analysis compares renewable MeOH and dimethyl ether LHC transport with pressurized and cryogenic H<small><sub>2</sub></small> transport for FCVs. For the analyses in which H<small><sub>2</sub></small> gas is produced as a fuel, RC&C steps are assumed to be accomplished off-board or before fueling the vehicles. ‘Vehicle’ analysis findings indicate that with a moderate tax on carbon emissions, in the year 2035 and beyond, FCVs can be competitive with ICEVs with an RC&C cost of ∼US $ 2–6 per kg H<small><sub>2</sub></small>. From the ‘fuel’ analysis perspective, LHCs break-even with gaseous and liquid H<small><sub>2</sub></small> transport at a more flexible RC&C cost of US $ 7.9–11.4 per kg H<small><sub>2</sub></small>.</p>\",\"PeriodicalId\":104,\"journal\":{\"name\":\"Sustainable Energy & Fuels\",\"volume\":\" 22\",\"pages\":\" 5181-5194\"},\"PeriodicalIF\":5.0000,\"publicationDate\":\"2024-09-20\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Sustainable Energy & Fuels\",\"FirstCategoryId\":\"88\",\"ListUrlMain\":\"https://pubs.rsc.org/en/content/articlelanding/2024/se/d4se00731j\",\"RegionNum\":3,\"RegionCategory\":\"材料科学\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"CHEMISTRY, PHYSICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Sustainable Energy & Fuels","FirstCategoryId":"88","ListUrlMain":"https://pubs.rsc.org/en/content/articlelanding/2024/se/d4se00731j","RegionNum":3,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"CHEMISTRY, PHYSICAL","Score":null,"Total":0}
Choosing a liquid hydrogen carrier for sustainable transportation†
Liquid hydrogen carriers (LHCs) are important shuttles for molecular hydrogen (H2) as they are convenient to transport as energy-dense liquids over distances greater than 10 000 km. Herein, we provide comprehensive insights into the comparative practicality and safety of irreversible LHCs. From a gas purification standpoint, fewer products in the released H2 stream result in less separation complexity and lower cost. Unit operational complexities of methanol (MeOH) steam reforming versus fossil steam-methane reforming were analyzed in depth to highlight gas-cleaning complexities. The main challenge is to estimate the costs of LHC reforming, cleaning and compression (RC&C) steps for H2 production in order to break even with other energy scenarios. To achieve this, two techno-economic analyses (TEA) were performed from the ‘vehicle’ and ‘fuel’ points of view. ‘Vehicle’ analysis compares the use of MeOH-to-H2 for proton-exchange membrane fuel-cell vehicles (FCVs) with the use of MeOH directly as drop-in fuel for conventional vehicles (ICEVs). ‘Fuel’ analysis compares renewable MeOH and dimethyl ether LHC transport with pressurized and cryogenic H2 transport for FCVs. For the analyses in which H2 gas is produced as a fuel, RC&C steps are assumed to be accomplished off-board or before fueling the vehicles. ‘Vehicle’ analysis findings indicate that with a moderate tax on carbon emissions, in the year 2035 and beyond, FCVs can be competitive with ICEVs with an RC&C cost of ∼US $ 2–6 per kg H2. From the ‘fuel’ analysis perspective, LHCs break-even with gaseous and liquid H2 transport at a more flexible RC&C cost of US $ 7.9–11.4 per kg H2.
期刊介绍:
Sustainable Energy & Fuels will publish research that contributes to the development of sustainable energy technologies with a particular emphasis on new and next-generation technologies.