石油炼制与化工 ›› 2026, Vol. 58 ›› Issue (7): 145-150.

• 节能减排 • 上一篇    下一篇

钠法脱硫提取亚硫酸钠工艺在催化裂化装置的应用

余伟   

  1. 中韩(武汉)石油化工有限公司
  • 收稿日期:2026-01-29 修回日期:2026-01-13 出版日期:2026-07-12 发布日期:2026-06-29
  • 通讯作者: 余伟 E-mail:yuwei.zhsh@sinopec.com

APPLICATION OF SODIUM-BASED DESULFURIZATION PROCESS FOR SODIUM SULFITE EXTRACTION IN FCC UNIT

  • Received:2026-01-29 Revised:2026-01-13 Online:2026-07-12 Published:2026-06-29

摘要: 国内某炼化企业2.8 Mt/a催化裂化装置烟气脱硫单元成功投运钠法脱硫提取亚硫酸钠绿色循环工艺示范项目。对此工艺进行了简单介绍,并结合现场实际运行情况对常见问题进行了分析并给出了有效解决措施。该创新工艺通过双塔系统实现了SO2高效脱除与资源化利用,在满足烟气超低排放标准(SO2质量浓度不大于25 mg/m3,粉尘质量浓度不大于10 mg/m3)的同时,将脱硫产物转化为工业级无水亚硫酸钠产品。装置采用浓缩塔-吸收塔协同运行模式,配合盐析结晶技术,实现了含盐废水近零排放和副产物商品化的双重环保目标。经一年连续运行验证,系统排放指标稳定达到设计值,后处理单元产品纯度(w)维持在80%以上,整体运行压降控制在1 200~1 500 Pa范围内,验证了该工艺在催化裂化烟气治理领域的技术先进性和工程可行性。

关键词: 催化裂化, 烟气脱硫, 亚硫酸钠, 废水近零排放

Abstract: The flue gas desulfurization unit of a 2.8 Mt/a catalytic cracking unit in a domestic refining and chemical enterprise has successfully put into operation the "sodium-based desulfurization extracting sodium bisulfite" green circular process demonstration project. This article briefly introduces this process, analyzes common problems based on actual on-site operation conditions, and provides effective solutions.This innovative process achieves efficient removal and resource utilization of SO2 through a dual-tower system. While meeting the ultra-low emission standards for flue gas (the mass concentration of SO2 is not grater than 25 mg/m3, the mass concentration of dust is not grater than 10 mg/m3), it converts the desulfurization products into industrial-grade anhydrous sodium bisulfite products. The unit adopts a "concentration tower-absorption tower" collaborative operation mode, combined with salting-out crystallization technology, achieving the dual environmental protection goals of near zero discharge of salt-containing wastewater and commercialization of by-products. After one year of continuous operation verification, the system emission indicators have stably reached the design values, the purity of the post-treatment unit products has been maintained at over 80%, and the overall operating pressure drop has been controlled within the range of 1200—1500Pa, verifying the technological progressiveness and engineering feasibility of this process in the field of catalytic cracking flue gas treatment.

Key words: catalytic cracking, flue gas desulfurization, sodium sulfite, near zero wastewater discharge