Exergy study of hydrogen cogeneration and seawater desalination coupled to the HTR-PM nuclear reactor

被引:9
作者
Rodriguez, Daniel Gonzalez [1 ]
Lira, Carlos Alberto Brayner de Oliveira [1 ]
Lima, Fernando Roberto de Andrade [1 ]
Hernandez, Carlos Garcia [2 ]
机构
[1] CRCN NE, Ctr Reg Ciencias Nucl Nordeste, BR-28610974 Recife, PE, Brazil
[2] Univ La Habana, Inst Super Tecnolo & Ciencias Aplicadas, InSTEC, Ave Salvador Allende Esq Luaces, Havana 10400, Cuba
关键词
Nuclear hydrogen production; Sulfur-iodine; HTR-PM nuclear Reactor; CPS; Efficiency; Exergy; SULFUR-IODINE CYCLE; BUNSEN REACTION; THERMOCHEMICAL CYCLE; LIQUID-EQUILIBRIA; HIGH-TEMPERATURE; DECOMPOSITION; ENERGY; EFFICIENCY; FLOWSHEET; ELECTROLYSIS;
D O I
10.1016/j.ijhydene.2022.10.162
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
This work presents a novel integration system of the high-temperature gas-cooled reactor-pebble bed module project to a hydrogen production process using the iodine-sulfur cycle in cogeneration with seawater desalination. The current approach includes a Rankine cycle, a sulfur-iodine thermochemical cycle for hydrogen production and a multi-stage flash desalination process. The use of a catalyst that allows the H2SO4 decomposition re-action to being carried out at temperatures compatible with the nuclear reactor project is considered. The residual heat from the acid decomposition reactions is used to desalinate seawater through the multi-stage flash process. A chemical process simulator is used to create a computational model that allows estimates of global and local efficiencies of the proposed flow diagram. Some operating parameters were sized, and their influence on the efficiency is also reported. The proposed model for the sulfur-iodine cycle can produce 0.41 kg/s of hydrogen with partial energy and exergetic efficiency of 37.35% and 38.64%. The desalination process can process 40.70 kg/s with energy and exergy efficiencies of 58.78% and 82.66%, respectively. The higher exergy destruction share is obtained in the heat ex-changers (36.55%), chemical reactors (16.56%) and separators (12.80%). The global system showed efficiencies of 40.13% and 52.04%, respectively.(c) 2022 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:2483 / 2509
页数:27
相关论文
共 57 条
[21]   Effects of operating parameters on the pressurized Bunsen reaction for the integrated operation of sulfur iodine hydrogen production process [J].
Kim, Hyo Sub ;
Park, Hyun Kyu ;
Kim, Young Ho ;
Park, Chu Sik ;
Bae, Ki Kwang .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (34) :15133-15140
[22]  
Kugeler K., 2019, Modular High-Temperature Gas-cooled Reactor Power Plant, DOI [10.1007/978-3-662-57712-7, DOI 10.1007/978-3-662-57712-7]
[23]   Experimental study of the vapour-liquid equilibria of HI-I2-H2O ternary mixtures, Part 2: Experimental results at high temperature and pressure [J].
Larousse, B. ;
Lovera, P. ;
Borgard, J. M. ;
Roehrich, G. ;
Mokrani, N. ;
Maillault, C. ;
Doizi, D. ;
Dauvois, V. ;
Roujou, J. L. ;
Lorin, V. ;
Fauvet, P. ;
Carles, P. ;
Hartmann, J. M. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (08) :3258-3266
[24]   Development of a flowsheet for iodine-sulfur thermo-chemical cycle based on optimized Bunsen reaction [J].
Lee, Byung Jin ;
No, Hee Cheon ;
Yoon, Ho Joon ;
Jin, Hyunq Gon ;
Kim, Young Soo ;
Lee, Jeong Ik .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (05) :2133-2143
[25]   Challenges for renewable hydrogen production from biomass [J].
Levin, David B. ;
Chahine, Richard .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (10) :4962-4969
[26]   Energy and economic assessment of an industrial plant for the hydrogen production by water-splitting through the sulfur-iodine thermochemical cycle powered by concentrated solar energy [J].
Liberatore, Raffaele ;
Lanchi, Michela ;
Giaconia, Alberto ;
Tarquini, Pietro .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (12) :9550-9565
[27]   EQUATION-OF-STATE MIXING RULES FOR MULTICOMPONENT MIXTURES - THE PROBLEM OF INVARIANCE [J].
MATHIAS, PM ;
KLOTZ, HC ;
PRAUSNITZ, JM .
FLUID PHASE EQUILIBRIA, 1991, 67 :31-44
[28]   Conceptual design and evaluation of an innovative hydrogen purification process applying diffusion-absorption refrigeration cycle (Exergoeconomic and exergy analyses) [J].
Mehrpooya, Mehdi ;
Mousavi, Seyed Ali ;
Asadnia, Majid ;
Zaitsev, Andrew ;
Sanavbarov, Romin .
JOURNAL OF CLEANER PRODUCTION, 2021, 316
[29]   A review on hydrogen production thermochemical water-splitting cycles [J].
Mehrpooya, Mehdi ;
Habibi, Roghayeh .
JOURNAL OF CLEANER PRODUCTION, 2020, 275
[30]  
Oh CH, 2006, HYDROGEN PRODUCTION