石油化工设备技术 ›› 2026, Vol. 47 ›› Issue (4): 30-35.doi: 10.3969/j.issn.1006-8805.2026.04.006

• 动设备 • 上一篇    下一篇

循环螺杆压缩机故障停机对C4全加氢装置的影响分析

耿强,吕静,马立国   

  1. 中国石化工程建设有限公司,北京 100101
  • 收稿日期:2026-02-06 修回日期:2026-06-05 接受日期:2026-06-28 出版日期:2026-07-17 发布日期:2026-07-17
  • 作者简介:耿强,男, 2014年毕业于中国石油大学(华东)化学工程与技术专业,工学硕士,从事石油化工工程设计工作,高级工程师,已发表SCI论文5篇。

Analysis on the Impacts of Circulating Compressor Failure on C4 Full Hydrogenation Unit

Geng Qiang, Lyu Jing, Ma Liguo   

  1. SINOPEC Engineering Incorporation, Beijing, 100101
  • Received:2026-02-06 Revised:2026-06-05 Accepted:2026-06-28 Online:2026-07-17 Published:2026-07-17

摘要: C4全加氢装置循环螺杆压缩机对装置的可靠运行具有重要作用,能够有效提高物料利用效率,降低驰放气中C4和氢气的损失。该压缩机可能由于油路系统、液喷系统、仪表系统或密封系统存在故障而导致停机。文章对其停机原因进行了分析,提出了应对方案,并深入探讨了停机后不同切换工况对物料损失和产品质量的影响,得出如下结论:循环压缩机中断补氢和中断补氢回收一段驰放气方案均会显著增加氢气消耗和驰放气损失;通过牺牲操作压力来回收一段加氢驰放气虽可在一定程度上降低物耗,但效果有限,改善作用不够明显。上述方案均可维持装置稳定运行。设计时应考虑切换时间控制在0.5 h内的操作要求,以确保二段全加氢系统能够维持正常循环,同时保证产品质量不受影响。

关键词: C4全加氢, 螺杆压缩机, 压缩机故障, 驰放气, 氢耗

Abstract: The circulating screw compressor in the C4 full hydrogenation unit plays a vital role in the reliable operation of the unit. It can effectively improve the material utilization efficiency and reduce the losses of C4 components and hydrogen in the purge gas. The compressor may shut down due to faults existing in the oil circuit system, liquid injection system, instrument system or sealing system. This paper analyzes the causes of the compressor failure, puts forward corresponding countermeasures, and thoroughly investigates the impacts of different switching conditions on material loss and product quality after shutdown. The conclusions are drawn as follows: both the scheme of interrupting hydrogen make-up by the circulating compressor and the scheme of interrupting hydrogen make-up while halting the recovery of the first-stage purge gas will markedly raise hydrogen consumption and purge gas loss. Although recovering the first-stage hydrogenation purge gas by lowering operating pressure can reduce material consumption to a certain extent, the mitigation effect is limited and the improvement is insignificant. All the above schemes can maintain the stable operation of the unit. During design, the operational requirement of controlling the switching time within 0.5 hours should be considered to ensure that the second-stage full hydrogenation system can maintain normal circulation while ensuring product quality unaffected.

Key words: C4 full hydrogenation, screw compressor, compressor failure, purge gas, hydrogen consumption