Kong Rui, Chen Lingen, Xia Shaojun, Li Penglei, Ge Yanlin
College of Power Engineering, Naval University of Engineering, Wuhan 430033, China.
Institute of Thermal Science and Power Engineering, Wuhan Institute of Technology, Wuhan 430205, China.
Entropy (Basel). 2021 Jan 8;23(1):82. doi: 10.3390/e23010082.
The thermochemical sulfur-iodine cycle is a potential method for hydrogen production, and the hydrogen iodide (HI) decomposition is the key step to determine the efficiency of hydrogen production in the cycle. To further reduce the irreversibility of various transmission processes in the HI decomposition reaction, a one-dimensional plug flow model of HI decomposition tubular reactor is established, and performance optimization with entropy generate rate minimization (EGRM) in the decomposition reaction system as an optimization goal based on finite-time thermodynamics is carried out. The reference reactor is heated counter-currently by high-temperature helium gas, the optimal reactor and the modified reactor are designed based on the reference reactor design parameters. With the EGRM as the optimization goal, the optimal control method is used to solve the optimal configuration of the reactor under the condition that both the reactant inlet state and hydrogen production rate are fixed, and the optimal value of total EGR in the reactor is reduced by 13.3% compared with the reference value. The reference reactor is improved on the basis of the total EGR in the optimal reactor, two modified reactors with increased length are designed under the condition of changing the helium inlet state. The total EGR of the two modified reactors are the same as that of the optimal reactor, which are realized by decreasing the helium inlet temperature and helium inlet flow rate, respectively. The results show that the EGR of heat transfer accounts for a large proportion, and the decrease of total EGR is mainly caused by reducing heat transfer irreversibility. The local total EGR of the optimal reactor distribution is more uniform, which approximately confirms the principle of equipartition of entropy production. The EGR distributions of the modified reactors are similar to that of the reference reactor, but the reactor length increases significantly, bringing a relatively large pressure drop. The research results have certain guiding significance to the optimum design of HI decomposition reactors.
热化学硫碘循环是一种潜在的制氢方法,而碘化氢(HI)分解是决定该循环制氢效率的关键步骤。为进一步降低HI分解反应中各类传递过程的不可逆性,建立了HI分解管式反应器的一维活塞流模型,并基于有限时间热力学,以分解反应系统中的熵产率最小化(EGRM)为优化目标进行性能优化。参考反应器由高温氦气进行逆流加热,基于参考反应器的设计参数设计了最优反应器和改进反应器。以EGRM为优化目标,采用最优控制方法求解在反应物入口状态和产氢率均固定的条件下反应器的最优构型,与参考值相比,反应器中总EGR的最优值降低了13.3%。在最优反应器总EGR的基础上对参考反应器进行改进,在改变氦气入口状态的条件下设计了两种长度增加的改进反应器。两种改进反应器的总EGR与最优反应器相同,分别通过降低氦气入口温度和氦气入口流量来实现。结果表明,传热EGR占比很大,总EGR的降低主要是通过减少传热不可逆性实现的。最优反应器分布的局部总EGR更为均匀,这大致印证了熵产均分原理。改进反应器的EGR分布与参考反应器相似,但反应器长度显著增加,带来了较大的压降。研究结果对HI分解反应器的优化设计具有一定的指导意义。