炼油技术与工程 ›› 2024, Vol. 54 ›› Issue (6): 57-60.

• 催化剂和助剂 • 上一篇    下一篇

TUD-DNS3型烟气脱硝助剂在重油催化裂化装置的工业应用

孙坤滨, 刘丽强, 程相民   

  1. 中国石化海南炼油化工有限公司
  • 收稿日期:2024-01-11 出版日期:2024-06-16 发布日期:2024-06-27
  • 作者简介:孙坤滨,技术员,2012年毕业于常州大学,现从事工艺技术管理工作。联系电话:0898-28820602,18789500793,E-mail:sunkb.hnlh@sinopec.com。;

Summary of industrial application of TUD-DNS3 flue gas denitrification additive in heavy oil catalytic cracking unit

Sun Kunbin, Liu Liqiang, Cheng Xiangmin   

  1. SINOPEC Hainan Refining & Chemical Co.,Ltd.
  • Received:2024-01-11 Online:2024-06-16 Published:2024-06-27

摘要:

自2023年6月1日起,海南省洋浦经济开发区催化裂化催化剂再生烟气NOx排放浓度限值由200 mg/m3降至100 mg/m3。某企业为避免烟气NOx排放超标,进行了TUD-DNS3型脱硝助剂工业应用试验。加注该脱硝助剂后,烟气NOx质量浓度稳步降低,在助剂累计量达到系统催化剂总藏量约2.5%时,综合塔出口NOx质量浓度由135 mg/m3降至92 mg/m3,脱除率达30%以上。TUD-DNS3磨损指数为1.78%,新鲜催化剂磨损指数为2.10%,二者相差不大,表现为助剂加注前后油浆固含量基本不变。在外排烟气SO2质量浓度基本不变的情况下,脱硫脱硝耗碱量约下降2 t/d,气体产品中硫化氢含量上升,说明TUD-DNS3具有一定硫转移效果。TUD-DNS3加注后再生烟气中CO/CO2体积比由0.367降至0.238,再生侧取热负荷增加,外取热器产汽量增加约17 t/h,在余热锅炉炉膛温度维持稳定的情况下,余热锅炉消耗燃料气量有所上升。

关键词: TUD-DNS3, 重油催化裂化, 烟气, NOx, 加注方案, SOx, 硫转移, 脱硝助剂

Abstract:

Starting from June 1, 2023, the NOx emission limit of catalytic cracking catalyst regeneration flue gas in Yangpu Economic Development Zone has been reduced from 200 mg/m3 to 100 mg/m3. A certain enterprise conducted industrial application tests of TUD-DNS3 denitration additive to avoid excessive NOx emissions from flue gas. After adding the denitration agent, the mass concentration of NOx in the flue gas steadily decreased. When the cumulative amount of the agent reached about 2.5% of the total catalyst storage in the system, the mass concentration of NOx at the outlet of the comprehensive tower decreased from 135 mg/m3 to 92 mg/m3, and the removal rate reached over 30%. The wear index of TUD-DNS3 was 1.78%, and the wear index of fresh catalyst was 2.1%. The difference in wear index between the two was not significant, as the concentration of smoke dust and solid content of oil slurry remained basically unchanged before and after the addition of additives. When the mass concentration of SO2 in the discharged flue gas remains basically unchanged, the alkali consumption for desulfurization and denitrification decreased by about 2 t/d, and the hydrogen sulfide content in the gas product increased, indicating that TUD-DNS3 had a certain sulfur transfer effect. After the addition of TUD-DNS3, the CO/CO2 ratio in the regenerated flue gas decreased from 0.367 to 0.238. The heat load on the regeneration side increased, and the steam generation of the external heat exchanger increased by about 17 t/h. While the furnace temperature of the waste heat boiler remained stable, the fuel gas consumption of the waste heat boiler increased.

Key words: TUD-DNS3, heavy oil catalytic cracking, flue gas, NOx, refueling plan, SOx, sulfur transfer, denitrification additives