Thermo-economic characteristics and cost-influencing mechanism analysis of an advanced nuclear-powered zero-carbon hydrogen-electricity co-production system with sulfur-iodine process and combined cycle

被引:1
|
作者
Wang, Qi [1 ,2 ]
Macian-Juan, Rafael [2 ]
Yang, Mingde [1 ,3 ]
Zhang, Ping [1 ]
Liu, Xiaoguang [4 ]
Yang, Bo [5 ]
Li, Ru [1 ]
Cheng, Hongzhang [1 ]
Wang, Ying [1 ]
Fang, Sheng [1 ]
Ye, Xuan [1 ]
Xiong, Wei [1 ]
机构
[1] Tsinghua Univ, Inst Nucl & New Energy Technol, Collaborat Innovat Ctr Adv Nucl Energy Technol, Key Lab Adv Reactor Engn & Safety,Minist Educ, Beijing 100084, Peoples R China
[2] Tech Univ Munich, Chair Nucl Technol, Sch Engn & Design, Dept Energy & Proc Engn, D-85748 Garching, Germany
[3] Tsinghua Nucl Energy Corp Ltd, Beijing 100084, Peoples R China
[4] China Natl Nucl Corp, Beijing 100045, Peoples R China
[5] Chinese Acad Engn, Ctr Strateg Studies, Beijing 100088, Peoples R China
关键词
Very high temperature reactor; Sulfur-iodine process; Combined cycle; Hydrogen-electricity co-production; Nuclear hydrogen production; Economic analysis; EXERGOECONOMIC ANALYSIS; THERMAL EFFICIENCY; PLANT; ENERGY; COGENERATION; VHTR; ELECTROLYSIS; FLOWSHEET; EXERGY; DESIGN;
D O I
10.1016/j.ijhydene.2024.06.323
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The fourth-generation Very High Temperature Reactor (VHTR) holds great promise as a reactor type for largescale clean hydrogen (H2) production in conjunction with the Sulfur-Iodine (SI) thermochemical process. However, limited research exists on the design and economic analysis of coupled VHTR and SI process nuclear hydrogen production systems, particularly when the combined cycle is incorporated as a power cycle within the system. To address this issue, we have developed and examined an advanced VHTR-driven hydrogen-electricity co-production system that adopts the SI process and combined cycle. The system has been modeled from both thermodynamic and economic perspectives, and its thermo-economic performance has been assessed under various operating conditions. Several parametric studies have been conducted to elucidate factors influencing the unit H2 production cost. The simulation results demonstrate that the thermal efficiency of the proposed SI process is in the range of approximately 27.95%-35.28%, and under the baseline operating condition, the whole system can concurrently produce hydrogen at a rate of about 290 mol/s while generating around 103 MW of net electric power, with thermal efficiency, exergy efficiency, and unit H2 production cost of about 37%, 36%, and 4.32 $/kg, respectively. The unit H2 production cost of the proposed system is predicted to range between approximately $1.5/kg and $7/kg. Finally, it has been determined that increasing the reactor thermal power, extending the system lifetime, improving the cost capacity factor and unit electricity price, as well as decreasing the mass flow ratio and interest rate, all contribute to a reduction in the unit H2 production cost.
引用
收藏
页码:688 / 702
页数:15
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    Xiong, Wei
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    Macian-Juan, Rafael
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    Yang, Bo
    Li, Ru
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    ENERGY, 2024, 308