{"title":"等离子体碳中和石脑油裂化气化生命周期评价及技术经济分析","authors":"Serang Kwon and Seong-kyun Im","doi":"10.1039/D5GC02106E","DOIUrl":null,"url":null,"abstract":"<p >Plasma cracking of naphtha represents a promising electrification pathway for carbon-neutral ethylene production. It operates at high temperatures (3000–6000 K) in non-oxidative environments, achieving superior ethylene yields (50–60%) while eliminating direct greenhouse gas emissions. However, the energy-intensive nature of plasma reactors necessitates evaluating environmental and economic trade-offs. This study evaluates the performances of a modeled plasma naphtha cracking plant across varied operating conditions. When paired with renewable electricity, the emission intensity of produced ethylene decreased to 0.15 kg CO<small><sub>2</sub></small> eq. per kg C<small><sub>2</sub></small>H<small><sub>4</sub></small>, equivalent to 7.8–11.4% of conventional steam cracking levels. While the levelized cost of ethylene (1.75–2.00 $ per kg C<small><sub>2</sub></small>H<small><sub>4</sub></small>) at an electricity cost of 100 $ per MWh<small><sub>el</sub></small> exceeded the conventional steam cracking by 18–35%, cost parity could be achieved at electricity costs of 40.3–47.9 $ per MWh<small><sub>el</sub></small> under the optimized conditions that also minimized naphtha feedstock requirements. These findings highlight the dual advantages of plasma technology: eliminating direct emissions while enhancing ethylene yield. This research establishes plasma naphtha cracking as a viable decarbonization strategy for ethylene production, underscoring the need for affordable renewable electricity to unlock its full environmental and economic potential.</p>","PeriodicalId":78,"journal":{"name":"Green Chemistry","volume":" 37","pages":" 11530-11546"},"PeriodicalIF":9.2000,"publicationDate":"2025-08-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Life cycle assessment and technoeconomic analysis of naphtha cracking electrification using plasma for carbon neutrality\",\"authors\":\"Serang Kwon and Seong-kyun Im\",\"doi\":\"10.1039/D5GC02106E\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p >Plasma cracking of naphtha represents a promising electrification pathway for carbon-neutral ethylene production. It operates at high temperatures (3000–6000 K) in non-oxidative environments, achieving superior ethylene yields (50–60%) while eliminating direct greenhouse gas emissions. However, the energy-intensive nature of plasma reactors necessitates evaluating environmental and economic trade-offs. This study evaluates the performances of a modeled plasma naphtha cracking plant across varied operating conditions. When paired with renewable electricity, the emission intensity of produced ethylene decreased to 0.15 kg CO<small><sub>2</sub></small> eq. per kg C<small><sub>2</sub></small>H<small><sub>4</sub></small>, equivalent to 7.8–11.4% of conventional steam cracking levels. While the levelized cost of ethylene (1.75–2.00 $ per kg C<small><sub>2</sub></small>H<small><sub>4</sub></small>) at an electricity cost of 100 $ per MWh<small><sub>el</sub></small> exceeded the conventional steam cracking by 18–35%, cost parity could be achieved at electricity costs of 40.3–47.9 $ per MWh<small><sub>el</sub></small> under the optimized conditions that also minimized naphtha feedstock requirements. These findings highlight the dual advantages of plasma technology: eliminating direct emissions while enhancing ethylene yield. This research establishes plasma naphtha cracking as a viable decarbonization strategy for ethylene production, underscoring the need for affordable renewable electricity to unlock its full environmental and economic potential.</p>\",\"PeriodicalId\":78,\"journal\":{\"name\":\"Green Chemistry\",\"volume\":\" 37\",\"pages\":\" 11530-11546\"},\"PeriodicalIF\":9.2000,\"publicationDate\":\"2025-08-19\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Green Chemistry\",\"FirstCategoryId\":\"92\",\"ListUrlMain\":\"https://pubs.rsc.org/en/content/articlelanding/2025/gc/d5gc02106e\",\"RegionNum\":1,\"RegionCategory\":\"化学\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"CHEMISTRY, MULTIDISCIPLINARY\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Green Chemistry","FirstCategoryId":"92","ListUrlMain":"https://pubs.rsc.org/en/content/articlelanding/2025/gc/d5gc02106e","RegionNum":1,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"CHEMISTRY, MULTIDISCIPLINARY","Score":null,"Total":0}
引用次数: 0
摘要
等离子体裂解石脑油为碳中性乙烯生产提供了一条有前途的电气化途径。它在非氧化环境下的高温(3000-6000 K)下运行,在消除直接温室气体排放的同时,实现了优异的乙烯收率(50-60%)。然而,等离子体反应器的能源密集型特性需要对环境和经济进行权衡。本研究评估了模拟等离子体石脑油裂解装置在不同操作条件下的性能。当与可再生电力相结合时,产生的乙烯的排放强度降低到每千克C2H4 0.15千克二氧化碳当量,相当于传统蒸汽裂解水平的7.8-11.4%。虽然在电力成本为100美元/ mwheel的条件下,乙烯的平准化成本(1.75-2.00美元/ kg C2H4)比传统的蒸汽裂解成本高出18-35%,但在优化条件下,每mwheel的电力成本为40.3-47.9美元,同时也最大限度地减少了石脑原料的需求。这些发现突出了等离子体技术的双重优势:消除直接排放,同时提高乙烯产量。这项研究确定了等离子体石脑油裂解是乙烯生产的一种可行的脱碳策略,强调需要负担得起的可再生电力来释放其全部环境和经济潜力。
Life cycle assessment and technoeconomic analysis of naphtha cracking electrification using plasma for carbon neutrality
Plasma cracking of naphtha represents a promising electrification pathway for carbon-neutral ethylene production. It operates at high temperatures (3000–6000 K) in non-oxidative environments, achieving superior ethylene yields (50–60%) while eliminating direct greenhouse gas emissions. However, the energy-intensive nature of plasma reactors necessitates evaluating environmental and economic trade-offs. This study evaluates the performances of a modeled plasma naphtha cracking plant across varied operating conditions. When paired with renewable electricity, the emission intensity of produced ethylene decreased to 0.15 kg CO2 eq. per kg C2H4, equivalent to 7.8–11.4% of conventional steam cracking levels. While the levelized cost of ethylene (1.75–2.00 $ per kg C2H4) at an electricity cost of 100 $ per MWhel exceeded the conventional steam cracking by 18–35%, cost parity could be achieved at electricity costs of 40.3–47.9 $ per MWhel under the optimized conditions that also minimized naphtha feedstock requirements. These findings highlight the dual advantages of plasma technology: eliminating direct emissions while enhancing ethylene yield. This research establishes plasma naphtha cracking as a viable decarbonization strategy for ethylene production, underscoring the need for affordable renewable electricity to unlock its full environmental and economic potential.
期刊介绍:
Green Chemistry is a journal that provides a unique forum for the publication of innovative research on the development of alternative green and sustainable technologies. The scope of Green Chemistry is based on the definition proposed by Anastas and Warner (Green Chemistry: Theory and Practice, P T Anastas and J C Warner, Oxford University Press, Oxford, 1998), which defines green chemistry as the utilisation of a set of principles that reduces or eliminates the use or generation of hazardous substances in the design, manufacture and application of chemical products. Green Chemistry aims to reduce the environmental impact of the chemical enterprise by developing a technology base that is inherently non-toxic to living things and the environment. The journal welcomes submissions on all aspects of research relating to this endeavor and publishes original and significant cutting-edge research that is likely to be of wide general appeal. For a work to be published, it must present a significant advance in green chemistry, including a comparison with existing methods and a demonstration of advantages over those methods.