石油炼制与化工 ›› 2026, Vol. 57 ›› Issue (8): 123-130.

• 节能减排 • 上一篇    下一篇

电解水制氢与煤化工产业链的耦合研究

孔德升1,肖长宇2,慕冰涵2,肖丹丹1   

  1. 1. 恒力石化(大连)新材料科技有限公司
    2. 宁波中金石化有限公司
  • 收稿日期:2026-01-20 修回日期:2026-05-08 出版日期:2026-08-12 发布日期:2026-07-23
  • 通讯作者: 孔德升 E-mail:ds519520@163.com

RESEARCH ON COUPLING UTILIZATION OF HYDROGEN PRODUCTION VIA WATER ELECTROLYSIS AND COAL CHEMICAL INDUSTRY CHAIN


  • Received:2026-01-20 Revised:2026-05-08 Online:2026-08-12 Published:2026-07-23

摘要: 针对煤化工产业链高能耗、高碳排放和电解水制氢成本高的问题,对电解水制氢与煤化工产业链进行耦合,设计出无变换制氢耦合工艺。通过制氢系统、热能系统和O2系统的耦合设计,不仅在碳减排方面成效显著,同时可降低产业链生产成本,对新能源消纳模式创新、促进能源绿色低碳转型具有重要意义。研究结果表明:以生产3.0×105 m3/h H2、700 kt/a甲醇、350 kt/a醋酸和1.0×105 m3/h CH4的煤化工产业链为例,采用无变换制氢耦合工艺,使煤化工产业链的净化气需求量由9.4×105 m3/h降低至2.4×105 m3/h,可取消变换装置和变压吸附(PSA)装置,使空气分离装置、气化装置和低温甲醇洗装置规模缩小80%,减少气化用煤4 080 kt/a,减少CO2排放9 147.20 ktCO2e/a,但工艺装置投资需增加5.6%;配合6.5×105 m3/h电解水制氢装置,每小时可消纳绿电3.25 GW.h,CO2排放量降低102.44%,实现煤化工产业链CO2的“净零”排放;热能系统耦合后,驱动蒸汽产量增加130 t/h,产率提升36.5%;当绿电价格为0.2元/(kW.h)时,对电解水制氢副产的O2进行分级利用后,制氢成本可降至1.01元/m3,与煤制氢成本相当。

关键词: 电解水制氢, 煤化工, 耦合工艺, 热能, 氧气, 碳减排

Abstract: Addressing the constraints of high energy consumption, high carbon emissions, and high costs in hydrogen production through water electrolysis within the coal chemical industry chain, a study was conducted on the coupling design of hydrogen production through water electrolysis and the coal chemical industry chain. Through the coupling design of the hydrogen production system, thermal energy system, and oxygen system, not only were significant achievements made in carbon emission reduction, but also the production costs of the industry chain were reduced. This is of great significance for innovating new energy consumption models and promoting the green and low-carbon transformation of energy. The research shows that, taking the coal chemical industry chain producing 3.0×105 m3/h of hydrogen, 700 kt/a of methanol, 350 kt/a of acetic acid, and 1.0×105 m3/h of methane gas as an example, by adopting the coupling process of hydrogen production without conversion, the demand for purified gas in the coal chemical industry chain is reduced from 9.4×105 m3/h to 2.4×105 m3/h. The conversion unit and PSA unit are eliminated, and the scale of the air separation unit, gasification unit, and rectisol unit is reduced by 80%. Investment in process equipment increased by 5.6%, coal consumption for gasification is reduced by 4 080 kt/a, and CO2 emissions are reduced by 9 147.20 kt/a. Equipped with a 6.5×105 m3/h hydrogen production device through water electrolysis, it can consume 3.25 GW.h of green electricity per hour, the CO2 emissions have been reduced by 102.44%, achieving "net zero" CO2 emissions in the coal chemical industry chain. After coupling with the thermal energy system,the output of driving steam increases by 130 t/h, and the yield rate is improved by 36.5%. When the price of green electricity is 0.2 yuan/(kW.h), after the by-product oxygen from hydrogen production through water electrolysis is utilized in a graded manner, the cost of hydrogen production can be reduced to 1.01 yuan/m3, which is comparable to the cost of gray hydrogen.

Key words: hydrogen production through water electrolysis, coal chemical industry, coupling process, thermal energy, oxygen, carbon emission reduction