石油化工设计 ›› 2019, Vol. 36 ›› Issue (3): 48-.doi: 10.3969/j.issn.1005-8168.2019.03.013

• 工程应用 • 上一篇    下一篇

硫转移剂在催化裂化装置中的应用

 许步建1,王佳琨1,谢灵丹2,张延芳3   

  1. 1.中石油华东设计院有限公司,山东 青岛 266071 2.中国石油四川石化有限责任公司,四川 彭州 611930 3.中国石油化工股份有限公司胜利油田分公司,山东 东营 257000
  • 出版日期:2019-08-25 发布日期:2019-11-05
  • 作者简介:许步建,男,2013年毕业于天津大学化学工程专业,硕士,主要从事炼油设计工作,工程师。 E-mail:xubujian@cnpccei.cn,电话:0532-80950778

 Application of Sulfur Transfer Agent in FCC Unit

 Xu Bujian1, Wang Jiakun1, Xie Lingdan2, Zhang Yanfang3   

  1. 1. CNPC EastChina Design Institute Co., Ltd., Qingdao, Shandong, 266071; 2. PetroChina Sichuan Petrochemical Co., Ltd., Pengzhou, Sichuan, 611930;  3. SINOPEC Shengli Oilfield Company, Dongying, Shandong, 257000)
  • Online:2019-08-25 Published:2019-11-05

摘要:  

介绍了催化裂化装置硫转移剂注入系统加料流程及对装置产品的影响。注入硫转移剂后,烟气中SO2脱除率达到50.1%,烟气硫占原料硫的比例从加注前的2.81%w)降至2.27%w)。同时,工业试验的标定结果表明:加入硫转移剂后,干气、液化气硫含量明显增多,但对液化气、汽油、轻柴油产品性质无不良影响。另外,硫转移剂对装置催化剂的粒径分布、活性、选择性均无明显负面影响。然而,采用硫转移剂导致硫磺回收装置过程气发生变化,使得酸性气中潜硫量为正常值的107.5%,因此在设计硫磺回收装置时要考虑较大的操作弹性。另外,当烟气中SOx含量很高时,采用硫转移剂与湿法脱硫组合工艺,可将NaOH消耗量从1 217 kg/h降低至486.8 kg/h,同时含盐污水量从19.06 t/h降低到17.1 t/h,且含盐量降至4.87%,可直接排放,无需设置硫酸盐结晶设施,降低了装置费用。

关键词: 硫转移剂, 催化裂化, 硫磺回收

Abstract:  This paper introduces the feeding process of sulfur transfer agent injection system in FCC unit and its effect on the products. After the injection of sulfur transfer agent, the removal rate of SO2 in flue gas reaches 50.1%, and the proportion of flue gas sulfur in feed sulfur decreases from 2.81 wt% to 2.27 wt%. Meanwhile, the test run results of industrial tests show that the sulfur contents of dry gas and LPG increase significantly after adding sulfur transfer agent, and no adverse effects are found on the properties of LPG, gasoline and light diesel products. In addition, sulfur transfer agent has no significant negative effects on the particle size distribution, activity or selectivity of the catalysts in FCC unit. However, the use of sulfur transfer agent leads to changes in the process gas of sulfur recovery unit, and the latent sulfur in acidic gas reaches 107.5% of the normal value, so the sulfur recovery unit should be designed to have higher operating flexibility. When the SOx concentration in flue gas is high, the combination process of sulfur transfer agent and wet desulfurization can be adopted. The NaOH consumption can be reduced from 1217 kg/h to 486.8 kg/h, the saline sewage can be reduced from 19.06 t/h to 17.1 t/h, and the salt content can be reduced to 4.87%, so it can be discharged directly without installing sulfate crystallization facilities, thus reducing the unit cost.

Key words: sulfur transfer agent, fluid catalytic cracking/FCC, sulfur recovery