FIELD: compressor-building engineering, particularly provision of explosion-proof operation during gas, gas-condensate and oil well repair and development. SUBSTANCE: method involves compressing atmospheric air free from mechanical admixtures into initial compressor stages up to pressure of 8 - 12 kg/sq.sm; cooling compressed air; removing water and oil drops from compressed air into cooler and water-and-oil trap; cleaning air from water and oil vapor into air fine filter; separating air in gas-separator into inert nitrogenbased gas mixture with oxygen content of 10% and oxygen enriched air; extracting oxygen from air into gas-separator and compressing oxygen up to pressure of 100 - 150 kg/sq.cm; removing admixtures from oxygen into water-and-oil trap; cooling oxygen up to temperature below 40 C into cooler; feeding inert gas mixture through multi-stage booster unit into vessel, wherein inert gas mixture feeding into vessel is performed by all booster unit cylinders during the initial period to increase vessel pressure up to the first step pressure; feeding inert gas mixture from the first step into the second compression step along with pumping gas mixture simultaneously by the second step and the third step cylinders to obtain vessel pressure equal to that of the second step; operating booster unit by successive cycle, namely the first-the second-the third steps pumping into vessel along with inert gas mixture cooling up to temperature 40 C into coolers and cleaning into water-and-oil traps or heating into heater (or vortex tube) up to temperature of 150 - 300 C and supplying to consumers under pressure of 25 - 250 kg/sq.sm. EFFECT: increased extraction factor of inert gas mixture, decreased oxygen content into inert gas mixture, increased use factor of compressed air components, extended range of obtained air components by temperature, pressure and efficiency. 7 cl, 1 dwg
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机译:领域:压缩机制造工程,尤其是在天然气,凝析油和油井的修理和开发过程中提供防爆操作。实质:该方法涉及将不含机械混合物的大气压缩到初始压缩机阶段,压力达到8-12 kg / sq.sm;冷却压缩空气;将压缩空气中的水滴和油去除到冷却器和水油分离器中;将水和油蒸气中的空气清洗到空气细滤器中;将气体分离器中的空气分离成氧含量为10%的惰性氮基气体混合物和富氧空气;从空气中提取氧气到气体分离器中,并将氧气压缩至100-150 kg / sq.cm的压力;将氧气中的混合物去除到水和油的陷阱中;将氧气冷却至低于40摄氏度的温度并进入冷却器;通过多级增压器将惰性气体混合物进料到容器中,其中在初始期间,所有增压器气缸将惰性气体混合物进料到容器中,以将容器压力增加到第一步压力。将惰性气体混合物从第一步骤送入第二压缩步骤,同时通过第二和第三气缸将气体混合物泵入,以获得与第二步骤相同的容器压力;通过连续的循环操作增压器单元,即将第一,第二,第三步骤与惰性气体混合物一起泵入容器,冷却至40°C的温度进入冷却器,清洗成水油收集器或加热到加热器(或涡流管) ),温度可达150-300 C,并在25-250 kg / sq.sm的压力下供应给消费者。效果:增加惰性气体混合物的提取系数,减少惰性气体混合物中的氧气含量,增加压缩空气成分的使用系数,获得的空气成分的温度,压力和效率范围扩大。 7厘升,1载重吨
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