解吸气,变压吸附,优化改造,吸附容量 ," /> 解吸气,变压吸附,优化改造,吸附容量 ,"/> desorption gas, pressure swing adsorption, optimization and renovation, adsorption capacity ,"/> <p class="MsoNoSpacing" align="left" style="text-align:left;"> <b>某炼化企业<span>PSA</span>解吸气回收<span>H2</span>技术经济性分析<span></span></b>

石油化工设计 ›› 2026, Vol. 43 ›› Issue (3): 18-24.doi: 10.3969/j.issn.1005-8168.2026.03.004

• 设计技术 • 上一篇    下一篇

某炼化企业PSA解吸气回收H2技术经济性分析

戴鹏程1,汤 帅1,张怀森1,张志军1,曹 勃2   

  1. (1.山东裕龙石化有限公司,山东 烟台 265700;

    2.中国石化工程建设有限公司,北京 100101)

  • 收稿日期:2025-10-10 出版日期:2026-08-25 发布日期:2026-09-07
  • 作者简介:戴鹏程,男,2009年毕业于长江大学化学工程与工艺专业,工程学士,工程师,主要从事炼油工艺技术管理工作

Techno-Economic Analysis of Hydrogen Recovery from PSA Desorptioni Gas in a Refining and Petrochemical Enterprise

Dai Pengcheng1, Tang Shuai1, Zhang Huaisen1, Zhang Zhijun1, Cao Bo2   

  1. (1. Shandong Yulong Petrochemical Co., Ltd., Yantai, Shandong, 

    265700; 2. SINOPEC Engineering Incorporation, Beijing, 100101)

  • Received:2025-10-10 Online:2026-08-25 Published:2026-09-07

摘要:

氢气是石化生产不可或缺的重要原料。为有效回收含CO杂质解吸气中的氢气,提高全厂氢气综合利用率,拟对现有脱除CH4杂质的变压吸附装置工艺流程开展优化升级。基于变压吸附基本理论和装置现有的开车数据,核算装置对CO的吸附容量,推导出改造后装置吸附时间理的论计算公式,从技术层面验证了该装置具备处理含CO气源的能力。项目实施后,经测算改造新增成本和经济效益,结果显示,项目落地后每年可回收氢气1.79×107 kg,为企业创造直接经济效益4091.47万元。本次工艺改造在技术性和经济性上均具可行性,能够为炼化企业投产初期实现氢气资源高效利用提供可靠优化路径,有利于企业朝绿色低碳发展。

关键词: 解吸气')">

解吸气, 变压吸附, 优化改造, 吸附容量

Abstract:

Hydrogen is an indispensable feedstock for petrochemical production. To recover hydrogen from CO-containing desorption gas and enhance the plant-wide hydrogen utilization efficiency, the process flow of the existing pressure swing adsorption (PSA) unit for CH4 impurity removal was to be optimized. Based on the fundamental PSA theory and the current operational data, the unit's CO adsorption capacity was calculated, and the theoretical calculation formula for the adsorption time of the modified unit was derived. The results technically demonstrated the unit's capability to process CO-containing gas sources. An analysis of the additional costs and economic benefits after the modification shows that the modified unit could recover 17.9 million kg of hydrogen annually, generating a direct economic benefit of 40.9147 million yuan for the enterprise. The results demonstrate that this modification scheme is technically and economically feasible. It provides a reliable optimization approach for refining and petrochemical enterprises to maximize hydrogen resource utilization during initial operation stages, which is conducive to the green and low-carbon development of enterprises.

Key words: desorption gas')">

desorption gas, pressure swing adsorption, optimization and renovation, adsorption capacity