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作 者:盛斌[1] 曾强[1] 吴遥 唐忠渝 Sheng Bin;Zeng Qiang;Wu Yao;Tang Zhongyu(Zhongxian Branch of Chongqing Natural Gas Purification Plant General,PetroChina Southwest Oil & Gasfield Company,Chongqing,China;Yinjin Branch of Chongqing Natural Gas PurificationPlant General,PetroChina Southwest Oil & Gasfield Company,Chongqing,China)
机构地区:[1]中国石油西南油气田公司重庆天然气净化总厂忠县分厂 [2]中国石油西南油气田公司重庆天然气净化总厂引进分厂
出 处:《石油与天然气化工》2019年第3期34-38,共5页Chemical engineering of oil & gas
摘 要:通过对脱硫和硫磺回收装置进行分析可知,影响烟气中SO2排放的主要工艺因素是原料气气质、气量的波动、酸气组成、脱硫溶液性能及催化剂性能。为了降低硫磺回收装置的SO2排放,使其达到国家环保要求,主要采取了以下技术措施:①通过控制脱硫溶液质量分数及入塔温度,并适当降低溶液循环量,提高MDEA溶液的选择性;②及时更换失活催化剂;③在常规克劳斯段三级反应器添加SO2选择性加氢催化剂,减少进入超级克劳斯段的SO2含量;④优化停产除硫方案,缩短除硫时间。结果表明,采取上述措施后,天然气净化装置的硫回收率稳定较高,排放烟气中SO2质量浓度达到标准要求。Through the analysis on the desulfurization and sulfur recovery unit, it was concluded that the main process influence factors of SO 2 emission in flue gas were the fluctuation of feed gas composition and volume flow, the acid gas composition, the performance of desulfurization solution and catalyst. In order to reduce the SO 2 emission of the sulfur recovery unit and meet the national environmental protection requirements, the following technical measures were taken:(1) Improve the selectivity of MDEA solution by controlling the mass fraction of desulfurization solution and the solution temperature entering the absorption tower, and appropriately reduce the solution circulation.(2) Replace the deactivated catalyst in time.(3) Add SO 2 selective hydrogenation catalyst to the third-stage reactor of the conventional Claus section to reduce the SO 2 content entering the super Claus section.(4) Optimize the sulfur removal scheme, and shorten the sulfur removal time during plant production and shutdown. The results showed that after adopting the above measures, the sulfur recovery rate of the natural gas purification unit was stable high and the SO 2 mass concentration in the flue gas met the standard requirements.
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