石油化工设备技术 ›› 2026, Vol. 47 ›› Issue (5): 45-49,39.doi: 10.3969/j.issn.1006-8805.2026.05.008

• 腐蚀与防护 • 上一篇    

丁二烯装置再沸器腐蚀原因分析及优化措施

姚首领,张瑞丽,杜 斌,王立锋   

  1. 浙江石油化工有限公司,浙江 舟山 316000
  • 收稿日期:2026-03-30 修回日期:2026-08-18 接受日期:2026-08-31 出版日期:2026-09-15 发布日期:2026-09-16
  • 作者简介:姚首领,男,2021年毕业于中国石油大学(北京)化学工程与工艺专业,学士,主要从事丁二烯装置生产研究工作,工程师。
  • 基金资助:
    浙江石油化工有限公司(批准号:ZSH-RD-25-036)资助的课题

Corrosion Cause Analysis and Optimization Measures for Reboilers in Acetonitrile Based Butadiene Extraction Units

Yao Shouling, Zhang Ruili, Du Bin, Wang Lifeng   

  1. Zhejiang Petrochemical Co., Ltd., Zhoushan, Zhejiang, 316000
  • Received:2026-03-30 Revised:2026-08-18 Accepted:2026-08-31 Online:2026-09-15 Published:2026-09-16

摘要: 某20万t/a乙腈法丁二烯抽提装置运行过程中,萃取系统再沸器频繁出现管束腐蚀、泄漏问题,严重威胁装置安全生产。经分析发现,其腐蚀机理为含水乙腈在高温工况下分步水解生成乙酰胺、乙酸与氨气,其中的乙酸会引发碳钢设备发生均匀腐蚀与点蚀。同时,腐蚀产生的铁离子具有强催化活性,使丁二烯、炔烃加速聚合,生成胶质与垢层。垢层附着导致再沸器换热效率下降,塔釜温度被动升高,进一步加剧乙腈水解,形成水解-腐蚀-聚合-再加剧水解的恶性循环。由于原乙腈回收塔设计再生能力不足,造成循环溶剂纯度偏低、水含量超标,杂质、水分、催化介质在循环溶剂中不断累积,构成了乙腈水解的有利环境,是诱发腐蚀问题的根本原因。为此,对乙腈回收塔塔盘、冷源及配套仪表阀门进行了改造,将溶剂再生量由1 t/h 提升至3 t/h,并配套落实控温、控水、脱氧、钝化等工艺管控措施。改造后,循环乙腈品质显著提升,设备腐蚀与聚合物生成得到有效遏制,同时乙腈损耗与蒸汽消耗大幅降低,年经济效益显著增加。该案例可为同类乙腈法丁二烯装置防腐与溶剂系统优化提供工程参考。

关键词: 乙腈水解, 有机酸腐蚀, 铁离子催化, 溶剂再生, 工艺改造

Abstract: During the operation of a 200 kt/a acetonitrile-based butadiene extraction unit, the reboilers in the extraction system frequently experienced tube bundle corrosion and leakage, which has seriously threatened the safe production of the unit. It was found through analysis that the corrosion mechanism involved the stepwise hydrolysis of hydrated acetonitrile under high-temperature conditions, generating acetamide, acetic acid and ammonia gas. The generated acetic acid may cause uniform corrosion and pitting on carbon steel equipment. Meanwhile, iron ions generated by corrosion possessed strong catalytic activity, accelerating the polymerization of butadiene and alkynes to form gums and deposits. The adhesion of deposits reduced the heat-transfer efficiency of the reboilers and caused a passive rise in the column bottom temperature, which further aggravated acetonitrile hydrolysis. Consequently, a vicious cycle of hydrolysis-corrosion-polymerization-enhanced hydrolysis was formed. The insufficient regeneration capacity of the original acetonitrile recovery column design resulted in low purity and excessive water content in the circulating solvent. Continuous accumulation of impurities, moisture and catalytic media in the circulating solvent created favorable conditions for acetonitrile hydrolysis, which constituted the root cause of the corrosion. Accordingly, modifications were carried out on the trays, cold source and supporting instrument valves of the acetonitrile recovery column. The solvent regeneration rate was increased from 1 t/h to 3 t/h, and supporting process control measures including temperature control, water content control, deoxygenation and passivation were implemented. After modification, the quality of circulating acetonitrile was significantly improved. Equipment corrosion and polymer formation were effectively restrained. Meanwhile, acetonitrile loss and steam consumption were greatly reduced, bringing remarkable annual economic benefits. This case can provide engineering references for anti-corrosion and solvent-system optimization of similar acetonitrile-based butadiene extraction units.

Key words: acetonitrile hydrolysislorganic acid corrosionliron ion catalysislsolvent regenerationlprocess modification