甲醇装置脱硫槽压差升高的原因分析及应对措施

乙烯工业 ›› 2024, Vol. 36 ›› Issue (2): 22-24.

甲醇装置脱硫槽压差升高的原因分析及应对措施

王哲，丁玉奎，张磊磊，罗春青，李宏

中国石油天然气股份有限公司独山子石化分公司，新疆独山子 833699

收稿日期:2023-04-06 修回日期:2023-11-12 出版日期:2024-06-25 发布日期:2024-06-26
作者简介:王哲，男，2004年毕业于新疆大学化学工程与工艺专业，工学学士，现从事甲醇生产运行管理工作，工程师。

Cause Analysis and Countermeasures for Pressure Difference Increase in Desulfurization Tank of Methanol Plant

Wang Zhe, Ding Yukui, Zhang Leilei, Luo Chunqing, Li Hong

PetroChina Dushanzi Petrochemical Company, Dushanzi, Xinjiang, P.C.833699

Received:2023-04-06 Revised:2023-11-12 Online:2024-06-25 Published:2024-06-26

摘要/Abstract

摘要：

甲醇装置采用乙烯装置裂解单元的低压甲烷为原料，原料中烯烃含量偏高的情况时有发生，影响甲醇装置的安全平稳运行。甲醇装置在脱硫槽更换了具有加氢能力的B脱硫剂后，出现了压差逐渐升高的情况，通过现场验证和实操摸索，并采用低温加氢工艺技措，有效解决了脱硫槽压差升高的瓶颈问题。

关键词: 甲醇装置 , 脱硫槽 , 烯烃析碳 , 压差升高解决措施

Abstract:

Methanol plant uses low pressure methane from the cracking unit of ethylene plant as the raw material. There have been times when the olefin content of the raw material was high, affecting the safe and stable operation of the methanol plant. After replacing the desulfurizer in the desulfurization tank of methanol plant by desulfurizer B with hydrogenation capacity, the pressure difference gradually increased. Through field verification and practical operation, low temperature hydrogenation technology was used to effectively solve the bottleneck problem of pressure difference increase in the desulfurization tank.

Key words: methanol plant, desulfurization tank, olefin precarburization, pressure difference increase, countermeasure

王哲, 丁玉奎, 张磊磊, 罗春青, 李宏. 甲醇装置脱硫槽压差升高的原因分析及应对措施[J]. 乙烯工业, 2024, 36(2): 22-24.

Wang Zhe, Ding Yukui, Zhang Leilei, Luo Chunqing, Li Hong. Cause Analysis and Countermeasures for Pressure Difference Increase in Desulfurization Tank of Methanol Plant[J]. Ethylene Industry, 2024, 36(2): 22-24.