高含硫天然气净化厂Cansolv尾气处理工艺优化OA
Optimization of Cansolv tail gas treatment process in high-sulfur natural gas purification plant
目的 解决某高含硫天然气净化厂 Cansolv尾气处理装置 DS贫液中热稳定盐和S2O2-3 含量升高、DS贫液 pH 升高及高 COD废水处理量大等问题.方法 通过调整尾气燃烧炉反应段燃烧温度、优化工艺流程和关键运行参数,解决了 DS溶液品质变差、胺液净化单元(amine purification unit,APU)启运频率高、溶剂消耗量大的问题,确保排放烟气中 SO2 质量浓度平均值长期保持在 50 mg/m3 以下,远低于 GB 39728—2020《陆上石油天然气开采工业大气污染物排放标准》规定的排放限值(当硫磺回收装置总规模<200 t/d时,排放烟气中 SO2 质量浓度限值为 800 mg/m3).结果 优化关键运行参数后,装置工艺性能如下:①尾气燃烧炉燃烧段温度由 800℃调整为在 710~740℃范围内运行,燃烧后过程气中 O2 体积分数控制在1.5%~2.5%的范围内,热稳定盐与 DS溶剂中有机胺物质的量比从 1.5∶1~1.7∶1降至 1.1∶1~1.6∶1,APU启运频率由设计时的 6 次/d降至 1~2 次/d;②文丘里组合塔出口温度由 50℃降至在 30~35℃范围内运行,维持系统水平衡,DS溶液消耗量约减少 0.4 t/a,高 COD 废水处理量约减少 180 m3/a.结论 参数调整及工艺流程优化可弥补该装置的设计缺陷,使 DS贫液pH恢复至正常运行范围,降低其发生歧化反应的风险,从而使DS溶剂的性能得到改善.
Objective This study aims to solve issues in the Cansolv tail gas treatment unit of the high-sulfur natural gas purification plant:high levels of heat-stable salts and thiosulfate in the DS lean solution,an increased pH of the DS lean solution,and a large volume of high-COD wastewater.Method Problems such as the deterioration of DS solution quality,high startup frequency of the amine purification unit(APU),and excessive solvent consumption were solved by adjusting the combustion temperature in the reaction section of the tail gas combustion furnace and optimizing the process flow and key operating parameters.As a result,the average mass concentration of SO2 in the flue gas remained below 50 mg/m3 over the long term,being far below the limit of the GB 39728—2020 Emission standard of air pollutants for onshore oil and gas exploitation and production industry(800 mg/m3 for a sulfur recovery unit with capacity<200 t/d).Result After optimizing the key operating parameters,the process performance of the unit was as follows:First,the combustion section temperature of the tail gas combustion furnace was adjusted from 800℃to 710-740℃,and the volume fraction of oxygen in the process gas after combustion was controlled within 1.5%-2.5%.The molar ratio of heat-stable salts to organic amine in the DS solvent decreased from 1.5:1-1.7:1 to 1.1:1-1.6:1,and the APU startup frequency dropped from the design value of 6 times per day to 1-2 times per day.Second,the outlet temperature of the Venturi combination tower was reduced from 50℃to 30-35℃,maintaining the system water balance.The consumption of DS solution was reduced by about 0.4 t/a,and the volume of high-COD wastewater requiring treatment was reduced by about 180 m3/a.Conclusion Parameter adjustment and process flow optimization can compensate for the design defects of the unit,restore the pH of the DS lean solution to the normal operating range,and reduce the risk of disproportionation reactions,thereby improving the performance of the DS solvent.
陈光军;罗元;鲁大勇;赵西;伍虹桥;瞿忠华;李珊;杨星毅
中国石油西南油气田公司川西北气矿中国石油西南油气田公司川西北气矿中国石油西南油气田公司川西北气矿中国石油西南油气田公司天然气研究院中国石油西南油气田公司川西北气矿中国石油西南油气田公司川西北气矿中国石油西南油气田公司川西北气矿中国石油西南油气田公司川西北气矿
高含硫天然气Cansolv尾气处理氧化吸收热稳定盐GB 39728—2020
high-sulfur natural gasCansolvtail gas treatmentoxidation absorptionheat-stable saltsGB 39728—2020
《石油与天然气化工》 2026 (4)
8-14,7
中国石油西南油气田公司川西北气矿科技计划项目"高含硫原料天然气有机硫直接催化水解侧线试验"(2025-10sy)
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