电解
聚合物电解质膜电解
高温电解
堆栈(抽象数据类型)
碱性水电解
工艺工程
高压电解
计算机科学
制氢
工作(物理)
灵活性(工程)
氢
化学
机械工程
工程类
数学
统计
物理化学
电解质
有机化学
程序设计语言
电极
作者
Mónica Sánchez,Ernesto Amores,David Romero Abad,Lourdes Rodrı́guez,Carmen Clemente-Jul
标识
DOI:10.1016/j.ijhydene.2019.12.027
摘要
A model of an alkaline electrolysis plant is proposed in this paper, including both stack and balance of plant, with the objective of analyzing the performance of a complete electrolysis system. For this purpose, Aspen Plus has been used in this work due to its great potential and flexibility. Since this software does not include codes for modelling the electrolysis cells, a custom model for the stack has been integrated as a subroutine, using a tool called Aspen Custom Modeler. This stack model is based on semi-empirical equations which describe the voltage cell, Faraday efficiency and gas purity as a function of the current. The rest of the components in the electrolysis plant have been modelled with standard operation units included in Aspen Plus. Simulations have been carried out in order to evaluate and optimize the balance of the plant of an alkaline electrolysis system for hydrogen production. Also, a parametric study has been conducted. The results show that increasing the operation temperature and reducing the pressure can improve the overall performance of the system. The proposed model in this work for the alkaline electrolyzer can be used in the future to develop a useful tool to carry out techno-economic studies of alkaline electrolysis systems integrated with other process.
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