石油炼制与化工 ›› 2026, Vol. 57 ›› Issue (10): 152-160.

• 节能减排 • 上一篇    

成本约束下炼油厂绿氢替代灰氢的协同增效路径

廖忠陶1,王尊博1,2,王万真1,白锦川3,王瑞娥1   

  1. 1. 中国石油玉门油田分公司炼油化工总厂
    2. 浙江大学能源高效清洁利用国家重点实验室
    3. 甘肃省酒泉职业技术大学化工学院
  • 收稿日期:2026-04-02 修回日期:2026-06-26 出版日期:2026-10-12 发布日期:2026-09-20
  • 通讯作者: 廖忠陶 E-mail:liaozt@petrochina.com.cn
  • 基金资助:
    中国石油天然气股份有限公司科技项目

RESEARCH ON SYNERGISTIC BENEFIT PATHWAYS FOR GREEN HYDROGEN REPLACING GREY HYDROGEN IN REFINERY UNDER COST CONSTRAINTS


  • Received:2026-04-02 Revised:2026-06-26 Online:2026-10-12 Published:2026-09-20

摘要: 为了实现炼油厂绿氢替代灰氢并应对其成本增加,构建了绿氢替代+系统集成优化的协同增效路径。首先,通过建立氢气生产/消纳系统物料平衡模型,量化分析了“绿氢替代灰氢”对炼油厂氢源结构、燃料气系统及资源利用效率的影响。结果表明,以4600 m3/h绿氢替代炼油厂干气制氢装置生产的灰氢后,导致企业生产成本增加。因而提出并验证了两项成本优化策略:其一,利用停运干气制氢装置的PSA单元将重整氢气纯度(φ)从85%提升至99%以上,从而减少下游加氢装置新氢消耗约300 m3/h;其二,采用液相吸收法回收全厂高C3+ 含量燃料气中的液态烃13 kt/a。经济性核算结果表明:系统集成优化后,新建C3+回收装置和绿氢替代灰氢导致全厂成本增加3381万元/a,而回收高C3+液态烃和完全加工费节省共计3494万元/a,项目实施后企业效益提升113万元/a;此外,项目实施后全厂CO2减排约23 kt/a,考虑增加碳汇收益(碳价按100元/t计)约231万元。因此,实施绿氢替代灰氢可成为炼油厂资源重构与系统优化的重要契机,可在实现深度碳减排的同时保持经济效益的可持续性。

关键词: 绿氢, 灰氢, 重整氢, 绿氢炼化, 轻烃回收

Abstract: To achieve the green hydrogen replacing gray hydrogen initiative in refineries and address the associated cost increase, a synergistic efficiency enhancement pathway of green hydrogen substitution + system integration optimization is constructed. First, by establishing a material balance model for the hydrogen production/consumption system, the impacts of green hydrogen replacing gray hydrogen on the refinery's hydrogen source structure, fuel gas system, and resource utilization efficiency are quantitatively analyzed. The results show that replacing the gray hydrogen produced by the refinery's dry gas hydrogen production unit with 4600 m3/h of green hydrogen leads to an increase in the enterprise's production cost. Therefore, two cost optimization strategies are proposed and verified: Using the PSA unit of the decommissioned dry gas hydrogen production unit to raise the purity (φ) of reformed hydrogen from 85% to over 99%, thereby reducing the fresh hydrogen consumption of downstream hydrogenation units by approximately 300 m3/h.Adopting the liquid-phase absorption method to recover 13 kt/a of liquid hydrocarbons from the high C3+ content fuel gas across the entire plant. The economic accounting results indicate that after system integration optimization, the new C3+ recovery unit and the "green hydrogen replacing gray hydrogen" initiative cause the total plant cost to increase by 33.81 million yuan per year. Meanwhile, the recovery of high C3+ liquid hydrocarbons and the total savings from full processing fee reduction amount to 34.94 million yuan per year, boosting the enterprise's annual benefit by 1.13 million yuan after the project implementation. In addition, the total plant CO2 emission reduction reaches approximately 23 kt/a, and the increased carbon sink benefit (calculated at a carbon price of 100 yuan/t) is about 2.31 million yuan. Thus, implementing green hydrogen replacing gray hydrogen can serve as a critical opportunity for refineries to restructure resources and optimize systems, enabling deep carbon emission reduction while maintaining the sustainability of economic benefits.

Key words: green hydrogen, grey hydrogen, reforming hydrogen, green hydrogen refining, light hydrocarbon recovery