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煤制油尾气脱碳装置运行问题分析及对策
引用本文:马军,蔡卫,张武,张治国,杨如意.煤制油尾气脱碳装置运行问题分析及对策[J].石化技术与应用,2022,0(2):132-134.
作者姓名:马军  蔡卫  张武  张治国  杨如意
作者单位:国家能源集团宁夏煤业有限责任公司 煤制油分公司,宁夏 银川 750409
摘    要:针对宁夏煤业有限责任公司400万t/a煤制油尾气脱碳装置,分析了脱碳塔压差高、系统接气受阻、系统中Fe3+质量浓度超标、V2O5消耗高等问题,并提出工艺优化对策。结果表明:更换或清洗堵塞严重的规整填料,可防止塔压差升高;增加溶液过滤量可除去系统中的机械杂质、烃类物质、Fe3+等,可防止塔压差升高,但会增加V2O5消耗量;降低水洗塔液位、稳定洗剂水量、提高合成尾气和贫液温度,可防止系统接气受阻;保证系统中V5+质量浓度在5.5 g/L以上,可缓解设备腐蚀,同时保证反应的高效性。

关 键 词:煤制油  尾气脱碳  费托合成  吸收剂  V2O5  K2CO3  钝化

Operating problems analysis and countermeasures of coal-to-oil tail gas decarbonization unit
MA Jun,CAI Wei,ZHANG Wu,ZHANG Zhi-guo,YANG Ru-yi.Operating problems analysis and countermeasures of coal-to-oil tail gas decarbonization unit[J].Petrochemical Technology & Application,2022,0(2):132-134.
Authors:MA Jun  CAI Wei  ZHANG Wu  ZHANG Zhi-guo  YANG Ru-yi
Affiliation:Coal To Liquid Branch Company of Ningxia Coal Industry Co Ltd,CHN Energy Group ,Yinchuan 750409,China
Abstract:Based on the decarbonization unit of 4 Mt/a coal-to-oil tail gas in Ningxia Coal Industry Co Ltd, the problems such as high pressure difference of decarbonizing tower, obstruction of system gas, excessive concentration of Fe3+ in the system and high consumption of V2O5 were analyzed and the countermeasures of process optimization were put forward. The results showed that by replacing or cleaning the regular packing with serious blockage could prevent the abnormal increase of pressure difference of the column; the mechanical impurities, hydrocarbon substances and Fe3+ in the system could be removed by increasing the amount of solution filtration, which could prevent the increase of column pressure difference, but it would increase the consumption of V2O5. It could from prevent obstructing when accepting gas from the system by reducing the liquid level of the washing tower, stabilizing the water quantity of the washing agent and raising the temperature of the synthetic tail gas and temperature of the lean liquid. It could alleviate the corrosion of equipment and the high efficiency of reaction when the mass concentration of V5+ in the system was above 5.5 g/L.
Keywords:coal to oil  tail gas decarbonization  Fischer-Tropsch synthesis  absorbent  V2O5  K2CO3  passivation
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