OPTIMAL DESIGN OF RESOURCE-SAVING ADSORPTION UNITS FOR HYDROGEN RECOVERY ON BLOCK ADSORBENTS

Oleg O. Golubyatnikov, Evgeny I. Akulinin
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Abstract

The paper presents a new approach to the design of resource-saving pressure swing adsorption (PSA) installations for hydrogen recovery, which ensures a safe flow rate in the frontal layer of the block adsorbent using optimal programs for multi-stage smooth opening of the valves of the installation. The safe flow rate of 0.3 m/s was determined experimentally, which practically eliminates the abrasion of the adsorbent during the PSA process. An iterative algorithm was proposed to reduce the problem of optimal installation design to the problem of nonlinear programming. A number of optimization problems of design of the installation with a capacity of 100-4000 l/min STP and a hydrogen purity of 99.99%+ were solved using the example of a hydrogen 4-bed 4-step vacuum PSA. The optimal combinations of mode and design parameters of the PSA installation and the trends of their changes depending on capacity were determined. An exhaustive comparative analysis of PSA installations designed according to a new and traditional approach was carried out. It was found that installations designed according to the new approach secure a greater profit from hydrogen production by an average of 28.3% due to lower energy consumption for hydrogen production and weight and size characteristics (the length of the adsorbent layer and the inner diameter of the adsorber) compared to installations that are designed according to the traditional approach
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块状吸附剂资源型氢回收吸附装置的优化设计
本文提出了一种资源节能型变压吸附(PSA)装置的设计新方法,通过优化装置阀的多级平滑开启方案,保证了块式吸附剂前层的安全流量。实验确定的安全流速为0.3 m/s,基本消除了吸附过程中吸附剂的磨损。提出了一种迭代算法,将最优安装设计问题简化为非线性规划问题。以氢气4床4步真空PSA装置为例,解决了STP容量100- 4000l /min、氢气纯度99.99%以上的装置设计优化问题。确定了PSA装置模式和设计参数的最优组合及其随容量的变化趋势。根据新的和传统的方法设计的PSA装置进行了详尽的比较分析。研究发现,根据新方法设计的装置与根据传统方法设计的装置相比,由于氢气生产的能耗更低,重量和尺寸特性(吸附剂层的长度和吸附剂的内径)更低,因此可以从氢气生产中获得平均28.3%的更高利润
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