石油炼制与化工 ›› 2025, Vol. 56 ›› Issue (7): 24-31.

• 加工工艺 • 上一篇    下一篇

影响制氢装置长周期平稳运行的问题分析及对策

史家亮   

  1. 中国石化北京燕山分公司
  • 收稿日期:2024-12-27 修回日期:2025-03-24 出版日期:2025-07-12 发布日期:2025-07-01
  • 通讯作者: 史家亮 E-mail:shijl286.yssh@sinopec.com

ANALYSIS AND COUNTERMEASURES OF LONG TERM OPERATION PROBLEMS IN A HYDROGEN PRODUCTION UNIT

  • Received:2024-12-27 Revised:2025-03-24 Online:2025-07-12 Published:2025-07-01

摘要: 针对国内某天然气制氢装置运行过程中出现的转化炉炉管花斑、余热锅炉换热效率快速降低、中温变换反应器床层超温等问题进行了详细的原因分析,并提出了相应的解决措施。结果表明:转化炉炉管出现花斑的主要原因包括①原料气硫、氯杂质含量偏高,②装置加工负荷低、装置处理量频繁调整,③催化剂装填不当,产生“架桥”现象,④催化剂积炭,⑤转化炉火嘴调节不当,⑥反复开停工过程中升/降温速度过快对转化催化剂强度的影响等;余热锅炉换热效率快速降低的原因在于催化剂中的抗积炭助剂K2O被带走形成了结垢,导致传热速率下降;而余热锅炉换热效率快速降低是中温变换反应器床层超温的主要原因。为解决这些问题,提出严格控制负荷调整频次和速率,控制原料气流量变化速率和升/降温速率、优化转化炉燃烧状态、中压蒸汽热运循环、中温变换反应器入口注水等措施。综合实施上述措施,可保障制氢装置连续平稳运行。

关键词: 蒸汽重整, 制氢, 花斑, 余热锅炉, 中温变换反应器

Abstract: A detailed analysis was conducted on the causes of problems such as flower spots on the conversion furnace tubes, rapid decrease in heat transfer efficiency of the waste heat boiler, and overheating of the medium temperature shift reactor bed in a domestic natural gas hydrogen production unit, and corresponding solutions were proposed. The results showed that the main reasons for the occurrence of flower spots in the converter tube include:①high sulfur and chlorine impurity content in the feed gas, ②low processing load of the device and frequent adjustment of the device processing capacity, ③improper catalyst loading, resulting in "bridging" phenomenon, ④catalyst coking, ⑤improper adjustment of the converter furnace nozzle, ⑥the impact of rapid heating/cooling speed on the strength of the conversion catalyst during repeated start-up and shutdown processes. The reason for the rapid decrease in heat transfer efficiency of the waste heat boiler is that the anti-coking additive K2O in the catalyst is taken away to form scaling, resulting in a decrease in heat transfer rate.The rapid decrease in heat exchange efficiency of the waste heat boiler is the main reason for the bed overheating of the medium temperature shift reactor. To address these issues, measures such as strictly controlling the frequency and rate of load adjustment, controlling the rate of change in feed gas flow rate and temperature rise/fall rate, optimizing the combustion state of the converter, implementing medium pressure steam thermal circulation, and injecting water into the inlet of the medium temperature shift reactor are proposed. The comprehensive implementation of the above measures can ensure the continuous and stable operation of the hydrogen production unit.

Key words: steam reforming, hytrogen production, flower spot, waste heat boiler, medium temperature shift reactor