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Article(id=1295064972799791248, tenantId=1146029695717560320, journalId=1210938733613449225, issueId=1295064874678252123, articleNumber=null, orderNo=null, doi=10.19666/j.rlfd.202505077, pmid=null, cstr=null, oa=null, hot=null, price=null, onlineType=0, articleFormat=0, articleType=null, articleTypeStr=null, receivedDate=1747411200000, receivedDateStr=2025-05-17, revisedDate=1749225600000, revisedDateStr=2025-06-07, acceptedDate=1750003200000, acceptedDateStr=2025-06-16, onlineDate=1786697150658, onlineDateStr=2026-08-14, pubDate=1774368000000, pubDateStr=2026-03-25, doiRegisterDate=null, doiRegisterDateStr=null, onlineIssueDate=1786697150658, onlineIssueDateStr=2026-08-14, onlineJustAcceptDate=null, onlineJustAcceptDateStr=null, onlineFirstDate=null, onlineFirstDateStr=null, sourceXml=null, magXml=null, createTime=1786697150658, creator=13701087609, updateTime=1786697150658, updator=13701087609, issue=Issue{id=1295064874678252123, tenantId=1146029695717560320, journalId=1210938733613449225, year='2026', volume='55', issue='3', pageStart='1', pageEnd='184', issueExtLink='null', onlineDate='null', pubDate='1774368000000', pubDateStr='2026-03-25', beforeIssueId=null, nextIssueId=null, price=null, status=1, issueComplete=1, articleOrder=1, issueType=-1, specialIssue=null, createTime=1786697127264, creator='13701087609', updateTime=1786698874628, updator='13701087609', preIssue=null, nextIssue=null, articleTotal=null, ext={EN=IssueExt(id=1295072203708592834, tenantId=1146029695717560320, journalId=1210938733613449225, issueId=1295064874678252123, language=EN, specialIssueTitle=, coverIllustrator=null, specialIssueEditor=, specialIssueAbout=), CN=IssueExt(id=1295072203708592835, tenantId=1146029695717560320, journalId=1210938733613449225, issueId=1295064874678252123, language=CN, specialIssueTitle=, coverIllustrator=null, specialIssueEditor=, specialIssueAbout=)}, issueFiles=null, downloadFileDto=null}, startPage=1, endPage=5, ext={EN=ArticleExt(id=1295064973248581778, articleId=1295064972799791248, tenantId=1146029695717560320, journalId=1210938733613449225, language=EN, title=Design and performance analysis of a novel solar polygeneration system based on S-CO2 Brayton cycle, columnId=1211002405299294959, journalTitle=Thermal Power Generation, columnName=Thermal Energy Science Research, runingTitle=null, highlight=null, articleAbstract=
[Objective]

To improve the comprehensive energy utilization efficiency of solar thermal power generation, this paper presents a novel linear Fresnel reflector (LFR) concentrated solar polygeneration system using supercritical carbon dioxide (S-CO2) Brayton cycle and organic Rankine cycle (ORC), which is designed for producing electricity, fresh water and hydrogen.

[Methods]

By using the Ebsilon code, the operation performance of the polygeneration system is investigated.

[Results]

The results show that the output power and Brayton cycle efficiency of the polygeneration system are 50.0 MW and 44.0%, respectively. The hydrogen production rate and freshwater production rate of the polygeneration system are 18.34 kg/h and 311.61 t/h, respectively. The LFR solar section, Brayton cycle, ORC hydrogen production section and multistage flash desalination facility can achieve the coordinated operation effectively during a long term.

[Conclusion]

The economic performance evaluation results show that for the polygeneration system, its levelized costs of electricity, hydrogen and freshwater are 0.72 yuan/(kW·h), 28.8 yuan/kg and 7.75 yuan/t, respectively, revealing the economic feasibility of the polygeneration system.

, authors=Gang WANG, Chenxu XU, Chuntian GAO, authorsList=Gang WANG, Chenxu XU, Chuntian GAO, authorCompany=null, correspAuthors=Chuntian GAO, authorNote=null, correspAuthorsNote=null, copyrightStatement=null, copyrightOwner=null, extLink=null, articleAbsUrl=null, sourceXml=null, magXml=null, pdfUrl=null, pdf=null, pdfFileSize=null, pdfExtLink=null, richHtmlUrl=null, mobilePdfUrl=null, reviewReport=null, pdfFirstPage=null, abstractGraph=null, abstractGraphContent=null, abstractVideo=null, citation=null, cebUrl=null, magXmlContent=null, mapNumber=null, fund=null), CN=ArticleExt(id=1295064977459663004, articleId=1295064972799791248, tenantId=1146029695717560320, journalId=1210938733613449225, language=CN, title=基于S-CO2布雷顿循环的新型多联产系统设计与性能分析, columnId=1211002405437706993, journalTitle=热力发电, columnName=热能科学研究, runingTitle=null, highlight=null, articleAbstract=
【目的】

为提升太阳能光热发电的综合能源利用效率，提出了一种利用超临界二氧化碳（S-CO2）布雷顿循环和有机朗肯循环（ORC）的新型线性菲涅尔反射镜聚光太阳能多联产系统，用于同时生产电力、淡水和氢气。

【方法】

利用Ebsilon程序，对多联产系统进行了运行性能分析。

【结果】

多联产系统的输出功率和布雷顿循环效率分别为50.0 MW和44.0%；多联产系统的产氢率和产水率分别为18.34 kg/h和311.61 t/h；线性菲涅尔反射式太阳能模块、布雷顿循环、ORC制氢模块和多级闪蒸海水淡化装置可以实现长期有效的协调运行。

【结论】

多联产系统的电力、氢气和淡水的平准化成本分别为0.72元/（kW·h）、28.8元/kg和7.75元/t，表明该多联产系统具有经济可行性。

, authors=王刚, 徐晨旭, 高春天, authorsList=王刚, 徐晨旭, 高春天, authorCompany=null, correspAuthors=高春天, authorNote=

王刚（1984），男，博士，教授，主要研究方向为太阳能利用技术，。

, correspAuthorsNote=
高春天（1994），男，博士，副教授，主要研究方向为超临界二氧化碳发电技术，。
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王刚（1984），男，博士，教授，主要研究方向为太阳能利用技术，。

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王刚（1984），男，博士，教授，主要研究方向为太阳能利用技术，。

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Distribution & Utilization, 2022, 39(1): 17-23., articleTitle=Performance assessment of hydrogen-cooling -heating-electricity integrated energy system driven by solar energy, refAbstract=null)], funds=[Fund(id=1295064989623144656, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, awardId=12305175, language=EN, fundingSource=National Natural Science Foundation of China(12305175), fundOrder=null, country=null), Fund(id=1295064989967077586, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, awardId=12305175, language=CN, fundingSource=国家自然科学基金项目(12305175), fundOrder=null, country=null)], companyList=[AuthorCompany(id=1295064978227220638, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, xref=null, ext=[AuthorCompanyExt(id=1295064978239803551, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, companyId=1295064978227220638, language=EN, country=null, province=null, city=null, postcode=null, companyName=null, departmentName=null, remark=School of Energy and Power Engineering, Northeast Electric Power University, Jilin 132012, China), AuthorCompanyExt(id=1295064978243997856, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, companyId=1295064978227220638, language=CN, country=null, province=null, city=null, postcode=null, companyName=null, departmentName=null, remark=东北电力大学能源与动力工程学院，吉林 吉林 132012)])], figs=[ArticleFig(id=1295064985814716608, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=EN, label=Fig.1, caption=The novel linear Fresnel reflector solar polygeneration system using S-CO2 Brayton cycle and organic Rankine cycle, figureFileSmall=MsahtmblaL7w5EWKjNjNGA==, figureFileBig=49Rc5KCH+akmUX5FanfMkA==, tableContent=null), ArticleFig(id=1295064985877631169, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=CN, label=图1, caption=基于S-CO2布雷顿循环和ORC的新型线性菲涅尔反射式太阳能多联产系统, figureFileSmall=MsahtmblaL7w5EWKjNjNGA==, figureFileBig=49Rc5KCH+akmUX5FanfMkA==, tableContent=null), ArticleFig(id=1295064986313838787, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=EN, label=Fig.2, caption=Ebsilon-based simulation model of the polygeneration system, figureFileSmall=es5AhC3EU1YNJMWOsFfNEQ==, figureFileBig=Ys26J1mct5h77i2ikcbSxg==, tableContent=null), ArticleFig(id=1295064986666160325, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=CN, label=图2, caption=基于Ebsilon的多联产系统仿真模型, figureFileSmall=es5AhC3EU1YNJMWOsFfNEQ==, figureFileBig=Ys26J1mct5h77i2ikcbSxg==, tableContent=null), ArticleFig(id=1295064987026870470, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=EN, label=Fig.3, caption=Operation simulation results of the polygeneration system, figureFileSmall=b1IorIBTRFMnueIemvJctA==, figureFileBig=cKLHfvjASvADM1gJWn+oxA==, tableContent=null), ArticleFig(id=1295064987119145159, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=CN, label=图3, caption=多联产系统运行模拟结果, figureFileSmall=b1IorIBTRFMnueIemvJctA==, figureFileBig=cKLHfvjASvADM1gJWn+oxA==, tableContent=null), ArticleFig(id=1295064987442106568, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=EN, label=Tab.1, caption=

Parameters of the polygeneration system

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参数数值
线性菲涅尔式太阳能光场面积/m21.822×106
储热罐体积/m32.741×104
S-CO2的质量流量/（kg·s–1）451.0
主压缩机的入口温度/℃32.0
主压缩机的入口压力/MPa7.6
气轮机的入口温度/℃631.7
气轮机的入口压力/MPa20.0
发电功率/MW50.0
ORC输出功率/MW3.13
PEM反应温度/℃80.00
产氢率/（kg·h–1）18.34
淡水产率/（t·h–1）311.61
), ArticleFig(id=1295064987546964170, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=CN, label=表1, caption=

多联产系统参数

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参数数值
线性菲涅尔式太阳能光场面积/m21.822×106
储热罐体积/m32.741×104
S-CO2的质量流量/（kg·s–1）451.0
主压缩机的入口温度/℃32.0
主压缩机的入口压力/MPa7.6
气轮机的入口温度/℃631.7
气轮机的入口压力/MPa20.0
发电功率/MW50.0
ORC输出功率/MW3.13
PEM反应温度/℃80.00
产氢率/（kg·h–1）18.34
淡水产率/（t·h–1）311.61
), ArticleFig(id=1295064987605684427, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=EN, label=Tab.2, caption=

Simulation results of the polygeneration system under design condition

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项目数值
主换热器的换热功率/MW113.6
海水淡化换热器的换热功率/MW125.3
蒸发器的换热功率/MW32.9
布雷顿循环输出功率/MW50.0
布雷顿循环效率/%44.0
ORC输出功率/MW3.13
ORC效率/%9.5
产水比1.5
日产氢量/kg183.4
日产水量/t3 116.1
), ArticleFig(id=1295064987660210380, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=CN, label=表2, caption=

多联产系统设计工况模拟结果

, figureFileSmall=null, figureFileBig=null, tableContent=
项目数值
主换热器的换热功率/MW113.6
海水淡化换热器的换热功率/MW125.3
蒸发器的换热功率/MW32.9
布雷顿循环输出功率/MW50.0
布雷顿循环效率/%44.0
ORC输出功率/MW3.13
ORC效率/%9.5
产水比1.5
日产氢量/kg183.4
日产水量/t3 116.1
), ArticleFig(id=1295064989358903502, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=EN, label=Tab.3, caption=

Economic analysis results of the polygeneration system

, figureFileSmall=null, figureFileBig=null, tableContent=
项目数值
发电系统建设成本/元9.130×108
发电系统固定运维成本/元2.334×107
发电系统可变运维成本/（元·（kW·h）–1）0.288
平准化电价/（元·（kW·h）–1）0.720
海水淡化系统固定投资成本/元5.847×106
海水淡化系统的热力成本/元1.870×106
平准化水价/（元·t–1）7.750
ORC制氢系统固定投资成本/元3.384×107
ORC制氢系统的热力成本/元1.754×107
平准化氢价/（元·kg–1）28.800
), ArticleFig(id=1295064989446983887, tenantId=1146029695717560320, journalId=1210938733613449225, articleId=1295064972799791248, language=CN, label=表3, caption=

多联产系统经济性分析结果

, figureFileSmall=null, figureFileBig=null, tableContent=
项目数值
发电系统建设成本/元9.130×108
发电系统固定运维成本/元2.334×107
发电系统可变运维成本/（元·（kW·h）–1）0.288
平准化电价/（元·（kW·h）–1）0.720
海水淡化系统固定投资成本/元5.847×106
海水淡化系统的热力成本/元1.870×106
平准化水价/（元·t–1）7.750
ORC制氢系统固定投资成本/元3.384×107
ORC制氢系统的热力成本/元1.754×107
平准化氢价/（元·kg–1）28.800
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基于S-CO2布雷顿循环的新型多联产系统设计与性能分析
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王刚 , 徐晨旭 , 高春天
热力发电 | 热能科学研究 2026,55(3): 1-5
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热力发电 |热能科学研究 2026 , 55 (3) : 1 -5
基于S-CO2布雷顿循环的新型多联产系统设计与性能分析
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王刚 , 徐晨旭, 高春天
作者信息
  • 东北电力大学能源与动力工程学院，吉林 吉林 132012
通讯作者:
高春天（1994），男，博士，副教授，主要研究方向为超临界二氧化碳发电技术，。
作者简介:

王刚（1984），男，博士，教授，主要研究方向为太阳能利用技术，。

Design and performance analysis of a novel solar polygeneration system based on S-CO2 Brayton cycle
Gang WANG , Chenxu XU, Chuntian GAO
Affiliations
  • School of Energy and Power Engineering, Northeast Electric Power University, Jilin 132012, China
出版时间: 2026-03-25 doi: 10.19666/j.rlfd.202505077
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摘要
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【目的】

为提升太阳能光热发电的综合能源利用效率，提出了一种利用超临界二氧化碳（S-CO2）布雷顿循环和有机朗肯循环（ORC）的新型线性菲涅尔反射镜聚光太阳能多联产系统，用于同时生产电力、淡水和氢气。

【方法】

利用Ebsilon程序，对多联产系统进行了运行性能分析。

【结果】

多联产系统的输出功率和布雷顿循环效率分别为50.0 MW和44.0%；多联产系统的产氢率和产水率分别为18.34 kg/h和311.61 t/h；线性菲涅尔反射式太阳能模块、布雷顿循环、ORC制氢模块和多级闪蒸海水淡化装置可以实现长期有效的协调运行。

【结论】

多联产系统的电力、氢气和淡水的平准化成本分别为0.72元/（kW·h）、28.8元/kg和7.75元/t，表明该多联产系统具有经济可行性。

多联产系统  /  超临界二氧化碳  /  布雷顿循环  /  多级闪蒸海水淡化  /  制氢  /  太阳能发电
[Objective]

To improve the comprehensive energy utilization efficiency of solar thermal power generation, this paper presents a novel linear Fresnel reflector (LFR) concentrated solar polygeneration system using supercritical carbon dioxide (S-CO2) Brayton cycle and organic Rankine cycle (ORC), which is designed for producing electricity, fresh water and hydrogen.

[Methods]

By using the Ebsilon code, the operation performance of the polygeneration system is investigated.

[Results]

The results show that the output power and Brayton cycle efficiency of the polygeneration system are 50.0 MW and 44.0%, respectively. The hydrogen production rate and freshwater production rate of the polygeneration system are 18.34 kg/h and 311.61 t/h, respectively. The LFR solar section, Brayton cycle, ORC hydrogen production section and multistage flash desalination facility can achieve the coordinated operation effectively during a long term.

[Conclusion]

The economic performance evaluation results show that for the polygeneration system, its levelized costs of electricity, hydrogen and freshwater are 0.72 yuan/(kW·h), 28.8 yuan/kg and 7.75 yuan/t, respectively, revealing the economic feasibility of the polygeneration system.

polygeneration system  /  supercritical carbon dioxide  /  Brayton cycle  /  multistage flash desalination  /  hydrogen production  /  solar power generation
王刚, 徐晨旭, 高春天. 基于S-CO2布雷顿循环的新型多联产系统设计与性能分析. 热力发电, 2026 , 55 (3) : 1 -5 . DOI: 10.19666/j.rlfd.202505077
Gang WANG, Chenxu XU, Chuntian GAO. Design and performance analysis of a novel solar polygeneration system based on S-CO2 Brayton cycle[J]. Thermal Power Generation, 2026 , 55 (3) : 1 -5 . DOI: 10.19666/j.rlfd.202505077
正文
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为应对全球能源危机和气候变化问题，国家提出“碳中和”战略。为促进“碳中和”目标的实现，减少化石能源的使用，增加可再生能源[1]的使用成为必然。近年来，得益于储能技术[2-3]的日益成熟，太阳能[4]和风能[5]成为发展较为成熟的2种可再生能源发电方式。对于太阳能发电，目前大多数的聚光太阳能发电（CSP）系统使用蒸汽朗肯循环，这限制了CSP系统的能量转换效率。为了获得更高的循环效率，同时考虑到S-CO2用作循环介质时的特性所提供的优势以及布雷顿循环设备的特点，未来的聚光太阳能发电场有望利用不同的S-CO2布雷顿循环代替朗肯循环发电[6]。Calle等人[7]对利用超临界CO2再压缩布雷顿循环的CSP系统进行了技术经济分析，其储热装置中的传热流体和储热材料分别为钠和相变材料。Abid等人[8]利用碟式太阳能集热器与超临界二氧化碳布雷顿循环进行结合，分析了集成再热再压缩和无再热再压缩的S-CO2布雷顿循环系统的经济性、产氢率、发电功率等。
除了太阳能发电外，太阳能也能驱动其他生产技术。例如太阳能驱动的海水淡化[9]、太阳能驱动的制氢[10]和太阳能驱动的制冷[11]等。为了满足更多的需求，研究了各种基于太阳能的多能互补系统[12]，以及基于太阳能的多联产系统[13]。例如，Wang等人[14]提出了太阳能-燃气混合发电制氢系统，并分析了混合发电系统的热力学性能。卞飞宇等[15]提出了一种集电、热、冷、氢于一体的太阳能集热多联产系统，研究工作主要集中于该系统的热力学分析。
本文提出了一种利用S-CO2布雷顿循环和有机朗肯循环（ORC）的新型线性菲涅尔反射式聚光太阳能多联产系统，该系统旨在生产电力、淡水和氢气；介绍了多联产系统的工作流程和原理，并进行运行性能分析，考察该系统的技术可行性和热力学性能；并从经济性角度对系统进行评估，证明多联产系统的经济可行性。
1　多联产系统原理
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本文提出了一种新型的基于线性菲涅尔式太阳能聚光的发电、制氢与淡水多联产系统，具体耦合布局结构如图1所示。该多联产系统主要由太阳能镜场、S-CO2布雷顿循环、ORC制氢和海水淡化系统4部分组成，通过多种方式实现能量梯度利用，进一步提高了太阳能的利用率。
多联产系统工作原理为：线性菲涅尔反射镜将太阳光照反射到集热器上并将太阳辐射能聚集起来，当熔盐吸收热量后温度上升，实现光热的转换，随后进入主熔盐换热器对S-CO2进行加热，升温后的S-CO2驱动气轮机发电，气轮机排气后的S-CO2依次流经布雷顿循环的其余部件。从主熔盐换热器换热后的熔盐依次经过有机朗肯循环换热器和海水淡化换热器，分别加热环己烷和冷海水，加热后的环己烷驱动涡轮机进行发电，为质子交换膜（PEM）电解槽提供电能。有机朗肯循环介质为环己烷（cyclo-C6H12）。海水淡化系统的工作流体为冷海水。冷海水加热后形成蒸汽，蒸汽进入闪蒸室冷凝后成为淡水。
2　多联产系统建模
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根据多联产系统的工作原理，表1给出了多联产系统在设计工况下（环境温度为293.15 K，太阳辐照强度为900.0 W/m2）的节点设计参数。利用Ebsilon软件对多联产系统建模，仿真模型如图2所示。多联产系统仿真模拟运行成功后，各主要管道、部件内工质的焓值、质量流量、温度、压力均在图2中给出。
布雷顿循环的效率ηbrayton为：
ηbrayton=PeQhx
式中：Pe为布雷顿循环的输出功率；Qhx为主换热器中的换热功率。
ORC效率ηorc为：
ηorc=PorcQeva
式中：Porc为ORC功率；Qeva为ORC蒸发器换热功率。
3　系统运行性能分析
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利用多联产系统参数及专业热力系统建模软件Ebsilon建立仿真模型，对系统在设计工况下的运行进行模拟。由于不同地区的太阳辐照情况不同，为了对多联产系统的长期运行进行模拟，首先需要制定该系统的运行策略。本文多联产系统初步运行策略如下：
1）白天阳光充足时系统按100.0%发电功率运行，在夜间和阳光不足的白天按30.0%功率运行。
2）ORC制氢和淡水生产系统每天工作时间为8：00—17：00。
3）储热罐内工质体积不能小于200.0 m3。
4）当光照强度和储热罐容量同时不足时，多联产系统需停止工作。
根据上述的运行策略，选取某地全年日照数据，对多联产系统在全年的运行进行模拟计算，结果见表2。假设海水淡化系统和ORC制氢系统每天连续运行10.0 h。从表2中可以看出：当系统在设计工况下运行时，主熔盐换热器的换热量为113.6 MW，海水淡化换热器的换热量为125.3 MW，蒸发器的换热量为32.93 MW；S-CO2布雷顿循环输出功率为50.0 MW，效率为44.0%，ORC发电功率和循环效率分别为3.13 MW和9.5%；ORC制氢系统和海水淡化系统的日产氢量和产水量分别为183.4 kg和3 116.1 t，海水淡化系统的产水比为1.5。模拟运行的计算结果合理，验证了多联产系统各子系统能够协同工作，此系统具有一定的技术可行性。
全年模拟运行模拟结果：多联产系统年发电量为245 890.0 MW·h，年产氢量为59.54 t，年产水量为996 339.57 t。这表明从长期运行考虑，多联产系统也具备技术可行性。图3给出了多联产系统的全年运行模拟结果中9月份连续7天运行参数的归一化数据。图3中各归一化参数由图3中7天内多联产系统各参数的仿真结果数值与其相应参数仿真结果的最大值相除得到。从图3可以看到，在阳光充足的白天时段多联产系统运行在额定功率水平，而在其余规定时段则多联产系统运行在30%额定功率水平。储热罐中热罐液位的变化同时受到布雷顿循环、多级闪蒸装置和ORC的运行以及太阳辐照强度变化的影响。
4　系统经济性分析
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本文对多联产系统进行经济性分析，利用平准化成本作为系统经济性指标。在此系统中主要包括平准化电价、平准化水价、平准化氢价。平准化电价CLCOE计算式：
CLCOE=(R×Ccons+CFOMC)Wann+CVOMC
式中：Wann为发电系统的全年发电量；R为折现率；Ccons为不包括海水淡化和制氢系统所用镜场部分的发电模块总建筑成本；CFOMC和CVOMC分别为太阳能发电机组的年固定运维成本和可变运维成本。
平准化水价CLCOW计算式：
CLCOW=Cmsf+Cw,thMann
式中：Mann为海水淡化系统年产水量；Cmsf为海水淡化系统固定投资成本；Cw，th为海水淡化系统的热力成本，即为多联产系统中驱动海水淡化系统所需要的太阳能镜场部分的建设成本。
对于ORC制氢子系统，假设系统的寿命为30年，平准化氢价CLCOH可表示为：
CLCOH=Ch,fix+Ch,thtlife⋅Mh,ann+EoP
式中：Ch，fix为ORC制氢系统的固定投资成本，主要由有机朗肯循环系统、PEM制氢系统和储氢罐3部分建设成本组成；Mh，ann为ORC制氢系统年产氢量；Ch，th为有机朗肯循环制氢系统的热力成本，即驱动制氢系统所需的镜场的建设成本；EOP为制氢系统所需要的额外电力，对于ORC制氢系统EOP=0。
多联产系统经济性分析结果见表3。
从表3可见：多联产系统的平准化电价为0.720元/（kW·h），如果考虑当地对太阳能光热发电的政策补助，平准化电价会更低；平准化水价为7.750元/t；平准化氢价为28.800元/kg。多联产系统子系统的平准化成本都处于合理范围内，证明此多联产系统在经济性上具有一定可行性。
5　结论
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本文提出了一种基于S-CO2布雷顿循环和ORC的新型线性菲涅尔反射式聚光太阳能多联产系统，用于生产电力、淡水和氢气，主要结论如下。
1）该多联产系统由线性菲涅尔反射镜太阳能部分、S-CO2布雷顿循环、ORC制氢子系统和多级闪蒸海水淡化装置组成。对多联产系统进行了数值建模和运行性能分析，结果表明，多联产系统的输出功率和布雷顿循环效率分别为50.0 MW和44.0%，多联产系统的产氢率和产水率分别为18.34 kg/h和311.61 t/h。
2）多联产系统的太阳能模块、布雷顿循环、ORC制氢模块和海水淡化装置可以实现协同运行。多联产系统的年发电量、年产氢量和年产淡水量分别为245 890.0 MW·h、59.54 t和996 339.57 t。
3）经济性分析表明，多联产系统的电力、氢气和淡水的平准化成本分别为0.72元/（kW·h），28.8元/kg和7.75元/t，均较为合理，一定程度上证明了多联产系统的经济可行性。
对于该多联产系统未来的研究，可考虑开展多联产系统的㶲分析，以考察多联产系统的热力学特性，并为系统的优化提供依据。另外，还可对该多联产系统进行在某些典型工况下的动态分析，以揭示系统在这些工况下的动态特性。
基金
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  • 国家自然科学基金项目(12305175)
文献
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2026年第55卷第3期
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doi: 10.19666/j.rlfd.202505077
  • 接收时间：2025-05-17
  • 首发时间：2026-08-14
  • 出版时间：2026-03-25
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  • 收稿日期：2025-05-17
  • 修回日期：2025-06-07
  • 录用日期：2025-06-16
基金
National Natural Science Foundation of China(12305175)
国家自然科学基金项目(12305175)
作者信息
    东北电力大学能源与动力工程学院，吉林 吉林 132012

通讯作者:

高春天（1994），男，博士，副教授，主要研究方向为超临界二氧化碳发电技术，。
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