Ph.D., Prof. Phan Anh Duong, Ph.D. Bo Rim Ryu, Prof. Jinuk Lee, Ph.D., Prof. Hokeun Kang
{"title":"船用直接氨固体氧化物燃料电池集成系统的技术经济分析","authors":"Ph.D., Prof. Phan Anh Duong, Ph.D. Bo Rim Ryu, Prof. Jinuk Lee, Ph.D., Prof. Hokeun Kang","doi":"10.1002/ceat.12013","DOIUrl":null,"url":null,"abstract":"<p>To achieve the ambitious goal of net-zero greenhouse gas emissions in the shipping industry by 2050, the getting to zero coalition prioritizes the adoption of zero-emission fuels and technologies. Ammonia stands out as a viable zero-carbon marine fuel, owing to its carbon-free composition and higher energy density relative to hydrogen. This paper presents a thorough techno-economic analysis of a direct ammonia solid oxide fuel cell (SOFC) system, which is enhanced by a gas turbine (GT) and integrated with a multi-generation system, including proton exchange membrane fuel cells (PEMFC), organic Rankine cycle (ORC), Kalina cycle (KC), steam Rankine cycle (SRC), and waste heat boiler (WHB). The study employs a multi-stage approach that includes dynamic computational analysis, techno-economic evaluation, and assessments of environmental and social impacts to determine the optimal system implementation. Economic viability is evaluated through indicators such as net present value, internal rate of return and payback period, highlighting the critical role of fuel cell capital costs in investment feasibility, and repayment timelines. The levelized cost of electricity (LCOE) spans from 0.482 to 0.554 $ (kW h)<sup>−1</sup>, showing a variation of approximately 6.2 % from the average LCOE. For unsubsidized and subsidized utility costs, the discounted payback period is calculated to be between 6.7 and 9.5 years, respectively.</p>","PeriodicalId":10083,"journal":{"name":"Chemical Engineering & Technology","volume":"48 4","pages":""},"PeriodicalIF":1.8000,"publicationDate":"2025-03-25","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Techno-Economic Analysis of a Direct Ammonia Solid Oxide Fuel Cell–Integrated System for Marine Vessels\",\"authors\":\"Ph.D., Prof. Phan Anh Duong, Ph.D. Bo Rim Ryu, Prof. Jinuk Lee, Ph.D., Prof. Hokeun Kang\",\"doi\":\"10.1002/ceat.12013\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p>To achieve the ambitious goal of net-zero greenhouse gas emissions in the shipping industry by 2050, the getting to zero coalition prioritizes the adoption of zero-emission fuels and technologies. Ammonia stands out as a viable zero-carbon marine fuel, owing to its carbon-free composition and higher energy density relative to hydrogen. This paper presents a thorough techno-economic analysis of a direct ammonia solid oxide fuel cell (SOFC) system, which is enhanced by a gas turbine (GT) and integrated with a multi-generation system, including proton exchange membrane fuel cells (PEMFC), organic Rankine cycle (ORC), Kalina cycle (KC), steam Rankine cycle (SRC), and waste heat boiler (WHB). The study employs a multi-stage approach that includes dynamic computational analysis, techno-economic evaluation, and assessments of environmental and social impacts to determine the optimal system implementation. Economic viability is evaluated through indicators such as net present value, internal rate of return and payback period, highlighting the critical role of fuel cell capital costs in investment feasibility, and repayment timelines. The levelized cost of electricity (LCOE) spans from 0.482 to 0.554 $ (kW h)<sup>−1</sup>, showing a variation of approximately 6.2 % from the average LCOE. For unsubsidized and subsidized utility costs, the discounted payback period is calculated to be between 6.7 and 9.5 years, respectively.</p>\",\"PeriodicalId\":10083,\"journal\":{\"name\":\"Chemical Engineering & Technology\",\"volume\":\"48 4\",\"pages\":\"\"},\"PeriodicalIF\":1.8000,\"publicationDate\":\"2025-03-25\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemical Engineering & Technology\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://onlinelibrary.wiley.com/doi/10.1002/ceat.12013\",\"RegionNum\":4,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q3\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering & Technology","FirstCategoryId":"5","ListUrlMain":"https://onlinelibrary.wiley.com/doi/10.1002/ceat.12013","RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
Techno-Economic Analysis of a Direct Ammonia Solid Oxide Fuel Cell–Integrated System for Marine Vessels
To achieve the ambitious goal of net-zero greenhouse gas emissions in the shipping industry by 2050, the getting to zero coalition prioritizes the adoption of zero-emission fuels and technologies. Ammonia stands out as a viable zero-carbon marine fuel, owing to its carbon-free composition and higher energy density relative to hydrogen. This paper presents a thorough techno-economic analysis of a direct ammonia solid oxide fuel cell (SOFC) system, which is enhanced by a gas turbine (GT) and integrated with a multi-generation system, including proton exchange membrane fuel cells (PEMFC), organic Rankine cycle (ORC), Kalina cycle (KC), steam Rankine cycle (SRC), and waste heat boiler (WHB). The study employs a multi-stage approach that includes dynamic computational analysis, techno-economic evaluation, and assessments of environmental and social impacts to determine the optimal system implementation. Economic viability is evaluated through indicators such as net present value, internal rate of return and payback period, highlighting the critical role of fuel cell capital costs in investment feasibility, and repayment timelines. The levelized cost of electricity (LCOE) spans from 0.482 to 0.554 $ (kW h)−1, showing a variation of approximately 6.2 % from the average LCOE. For unsubsidized and subsidized utility costs, the discounted payback period is calculated to be between 6.7 and 9.5 years, respectively.
期刊介绍:
This is the journal for chemical engineers looking for first-hand information in all areas of chemical and process engineering.
Chemical Engineering & Technology is:
Competent with contributions written and refereed by outstanding professionals from around the world.
Essential because it is an international forum for the exchange of ideas and experiences.
Topical because its articles treat the very latest developments in the field.