石油炼制与化工 ›› 2025, Vol. 56 ›› Issue (6): 82-89.

• 加工工艺 • 上一篇    下一篇

烷基化装置引气分碳五至水洗系统措施与效果分析

牛东会,杨跃进,向杰,曹太吉,许楠   

  1. 中国石化河南炼化公司
  • 收稿日期:2024-12-10 修回日期:2024-12-11 出版日期:2025-06-12 发布日期:2025-05-30
  • 通讯作者: 牛东会 E-mail:1920152722@qq.com

MEASURES AND EFFECTS ANALYSIS OF THE ALKYLATION UNIT INTRODUCING C5 COMPONENTS FROM GAS FRACTIONATOR TO THE WATER WASHING SYSTEM


  • Received:2024-12-10 Revised:2024-12-11 Online:2025-06-12 Published:2025-05-30

摘要: 中国石化河南炼化公司为了提高200 kt/a烷基化装置烷基化油收率,解决夏季汽油蒸气压高的问题,采取了掺炼一定量气分碳五至烷基化装置的办法,实现了烷基化油收率的提高。但在掺炼过程中,装置相关管线及设备出现堵塞情况,造成装置无法顺利掺炼气分碳五。针对该情况,通过对堵塞原因进行分析,可知气分碳五携带的N-甲基二乙醇胺杂质是引起管线及设备堵塞的主要原因。通过引气分碳五至烷基化装置水洗系统,脱除气分碳五中的杂质,气分碳五水洗罐中水洗水及中和池总排口水样氮质量浓度分别稳定控制在126.1 mg/L和47.4 mg/L左右,中和池总排口水样pH稳定在6~7范围,达到排放指标要求。水洗气分碳五引进烷基化反应系统后,装置原有易堵塞管线及设备压差稳定可控,原料烷烯摩尔比、反应温度、酸质量分数、酸耗及异丁烷体积分数等关键参数可分别稳定控制在1.3,3 ℃,92%,83.79 kg/t,88.8%左右。得到研究法辛烷值为94.6、雷德饱和蒸气压为47.91 kPa、终馏点为191.1 ℃、密度(20℃)为695.5 kg/m3及铜片腐蚀为1a级的优质烷基化油,并成功实现烷基化油收率提高3.48百分点的目标,为炼油厂汽油质量提升以及经济效益增加提供了有力的保障与支撑。

关键词: 硫酸烷基化, 烷基化油, 气分碳五, 水洗措施

Abstract: SINOPEC Henan Refining & Chemical Co.,Ltd. in order to improve the 200 kt/a alkylation unitalkylated oil yieldand solve the problem of high gasoline vapor pressure in the summer, mixing a certain amount of C5 components from gas fractionator (C5) to the alkylation unit, and the yield of alkylated oil was improved successfully, but during the blending of C5, the relevant pipelines and equipments of the device were prone to clogging, resulting in the C5 could not be blended successfully.In response to the situation, through the analysis of the clogging situation and causes, it was found that the N-methyldiethanolamines impurity carried by C5 were the main cause of clogging of the pipelines and equipments. Then, the impurities in the C5 were successfully removed by leading the C5 to the water washing system of the alkylation unit, which made the mass concentration of nitrogen of the washing water in the water washing tank of the C5 and the water samples in the total discharge of the neutralization pool be controlled stably at about 126.1mg/L and 47.4mg/L respectively, and the pH of the total discharge water sample of the neutralization pool was stabilized at the range of 6—7, which was in line with the requirements of the back-channel emission indexes. And after the water-washed C5 was introduced into the alkylation reaction system, the differential pressure of the original easily clogged pipeline and equipment of the device was stable and controllable, and the key production parameters such as feedstock alkene ratio, reaction temperature, mass fraction of acid, acid consumption, and volume fraction of isobutane could be stably controlled at about 1.3, 3℃, 92%, 83.79kg/t, and 88.8% respectively. While ensuring the smooth operation of the plant, the high quality alkylated oil products with octane number of 94.6, Reid's saturated vapor pressure of 47.91 kPa, final distillation point of 191.1℃, density(20℃) of 695.5kg/m3 and copper flake corrosion grade of 1a were obtained, and the target of alkylated oil yield increase of 3.48 percentage points was achieved successfully, which provided strong guarantee and support for the improvement of the quality of gasoline in the refinery as well as the increase of the efficiency of the refinery.

Key words: alkylation catalyzed by sulfuric acid, alkylated oil, Ccomponents from gas fractionator, water washing measures