Automation and control of an experimental protonic membrane steam methane reforming system

IF 3 Q2 ENGINEERING, CHEMICAL
Dominic Peters , Xiaodong Cui , Yifei Wang , Christopher G. Donahue , Jake Stanley , Carlos G. Morales-Guio , Panagiotis D. Christofides
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引用次数: 0

Abstract

Nickel dispersion on doped barium-zirconate ceramics is a state-of-the-art material formulation used to fabricate proton conducting membranes that can reform methane at lower operational temperatures (600 to 800 °C). Although steady-state operational data have been reported for these ion-conducting ceramic reformers, transient datasets are uncommon and not readily available. Moreover, the automation of protonic membrane reformers is a major technical challenge for the commercialization of modular thermo-electrochemical hydrogen generators with highly nonlinear process dynamics. Here, a multi-input multi-output feedback control scheme has been designed from a relative gain array analysis of three process variables for an experimental 500 W (thermal and electrochemical power consumption) protonic membrane reforming system. Specifically, the proposed control architecture automatically calculates hydrogen separation rate setpoints while safely and effectively reaching hydrogen production rate setpoints and desired steam-to-carbon ratios. The control architecture also drives the system to 99.6% methane conversion at a current density of 0.564 ± 0.0125 Acm−2 at 788 °C. Internal temperature fluctuations are mostly constrained to ± 6.00 °C min−1, which improves catalyst longevity when operating at hydrogen recovery rates exceeding 50%. Chief among these findings is an experimental demonstration of a control scenario that alters the hydrogen production rate setpoint every 150 min without sacrificing system-wide controllability. Integrator windup scenarios and counterproductive control actions are also avoided through rational controller design and proper controller tuning exercises. Industrial-scale applications of protonic membrane reformers may therefore be automated to control up to three process variables and have up to three additional control degrees of freedom for process intensification and optimization, making for well-governed, autonomous hydrogen generation units.
实验质子膜蒸汽甲烷重整系统的自动化与控制
掺杂锆酸钡陶瓷上的镍分散体是一种最先进的材料配方,用于制造质子导电膜,可以在较低的操作温度(600至800°C)下重组甲烷。虽然已经报道了这些离子传导陶瓷转化炉的稳态运行数据,但瞬态数据集并不常见,也不容易获得。此外,质子膜重整器的自动化是具有高度非线性过程动力学的模块化热电化学氢发生器商业化的主要技术挑战。本文基于三个过程变量的相对增益阵列分析,设计了一种多输入多输出反馈控制方案,用于500w质子膜重整实验系统(热和电化学功耗)。具体来说,所提出的控制架构自动计算氢分离率设定值,同时安全有效地达到产氢率设定值和所需的蒸汽碳比。在788℃下,当电流密度为0.564±0.0125 a·cm−2时,该控制架构还可使系统的甲烷转化率达到99.6%。内部温度波动大多被限制在±6.00°C⋅min - 1,当氢回收率超过50%时,提高了催化剂的寿命。这些发现中最主要的是一个控制方案的实验演示,该方案每150分钟改变一次产氢率设定值,而不会牺牲系统范围的可控性。通过合理的控制器设计和适当的控制器调优练习,还可以避免积分器上发条场景和适得其反的控制动作。因此,质子膜重整器的工业规模应用可以自动化控制多达三个过程变量,并具有多达三个额外的控制自由度,以进行过程强化和优化,从而形成良好的管理,自主制氢装置。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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CiteScore
3.10
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