Efficiency of the sulfur-iodine thermochemical water splitting process for hydrogen production based on ADS (accelerator driven system)

被引:12
作者
Garcia, Lazaro [1 ]
Gonzalez, Daniel [1 ]
Garcia, Carlos [1 ]
Garcia, Laura [1 ]
Brayner, Carlos [2 ]
机构
[1] Higher Inst Technol & Appl Sci, Dept Nucl Engn, Havana, Cuba
[2] Univ Fed Pernambuco, Dept Nucl Energy, Recife, PE, Brazil
关键词
Thermochemical water splitting cycles; Thermal efficiency; ADS; Sulfur-iodine cycle; Chemical process simulation; TRANSMUTATION ADVANCED DEVICE; PEBBLE-BED ADS; NUCLEAR-ENERGY; CYCLE; POWER;
D O I
10.1016/j.energy.2013.05.042
中图分类号
O414.1 [热力学];
学科分类号
摘要
The current hydrogen production is based on fossil fuels; they have a huge contribution to the atmosphere's pollution. Thermochemical water splitting cycles don't present this issue because the required process heat is obtained from nuclear energy and therefore, the environmental impact is smaller than using conventional fuels. Although, solar hydrogen production could be also used for practical applications because it's lower environmental impact. One of the promising approaches to produce large quantities of hydrogen in an efficient way using nuclear energy is the sulfur-iodine (S-I) thermochemical water splitting cycle. The nuclear source proposed in this paper is a pebble bed gas cooled transmutation facility. Pebble bed very high temperature advanced systems have great perspectives to assume the future nuclear energy. Softwares based on CPS (chemical process simulation) can be used to simulate the thermochemical water splitting sulfur-iodine cycle for hydrogen production. In this paper, a model for analyzing the sulfur-iodine process sensibility respect to the thermodynamics parameters: temperature, pressure and mass flow is developed. Efficiency is also calculated and the influence of different parameters on this value. The behavior of the proposed model for different values of initial reactant's flow, is analyzed. (c) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:469 / 477
页数:9
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