首页> 外国专利> APPARATUS FOR LOW-TEMPERATURE SEPARATION WITH DEPHLEGMATION OF LTSD FOR EXTRACTION OF HYDROCARBONS C2+ FROM NATURAL GAS (VERSIONS)

APPARATUS FOR LOW-TEMPERATURE SEPARATION WITH DEPHLEGMATION OF LTSD FOR EXTRACTION OF HYDROCARBONS C2+ FROM NATURAL GAS (VERSIONS)

机译:低温分离低温脱硫分离天然气中C 2 + 的装置

摘要

FIELD: technological processes.;SUBSTANCE: invention relates to low-temperature separation plants and can be used in gas industry for extraction of hydrocarbons C2+ from natural gas. Installation in version 1 includes drying unit, external cooling circuit in composition of evaporator, compressor, condenser and reducing device, two recuperative heat exchangers, reducing devices, dephlegmator, demethanizer and low-temperature separator. Version 2 includes compressor, refrigerator and additional reducing device. In operation of version 1, high-pressure gas is dried, cooled in a first recuperative heat exchanger, an evaporator and a second recuperative heat exchanger, then, reduced and directed to dephlegmator cooled by low-temperature separation gas, which is then heated in the first recuperative heat exchanger and discharged. During circulation, the external circuit coolant after heating in the evaporator is compressed by a compressor driven by at least one of the expanders, cooled in a condenser and reduced. Dephlegmation gas is reduced and mixed with the methane-containing gas and separated into a gas and a condensate in a low-temperature separator. Reflux is reduced, mixed with condensate and, through a second recovery heat exchanger, into demethanizer, from which methane-containing gas and hydrocarbons C2+ are removed. Operation of version 2 differs by the fact that part of high pressure gas is compressed by compressor actuated by means of at least one of expanders, cooled in refrigerator, second recovery heat exchanger and reduced.;EFFECT: invention increases output of hydrocarbons C2+.;2 cl, 2 dwg
机译:低温分离装置技术领域本发明涉及低温分离装置,可用于天然气工业中从天然气中提取碳氢化合物C 2 + 。版本1中的安装包括干燥单元,由蒸发器,压缩机,冷凝器和还原装置组成的外部冷却回路,两个换热热交换器,还原装置,分馏器,脱甲烷塔和低温分离器。版本2包括压缩机,冰箱和附加的减速装置。在版本1的操作中,将高压气体干燥,在第一同流换热器,蒸发器和第二同流换热器中冷却,然后还原并引导至由低温分离气冷却的除湿器,然后将其加热到第一换热热交换器并排出。在循环期间,在蒸发器中加热后的外部回路冷却剂被由至少一个膨胀器驱动的压缩机压缩,在冷凝器中冷却并减少。脱气气体被还原并与含甲烷的气体混合,并在低温分离器中分离成气体和冷凝物。减少回流,与冷凝物混合,并通过第二个回收热交换器进入脱甲烷塔,从中除去含甲烷气体和碳氢化合物C 2 + 。版本2的操作不同之处在于,高压气体的一部分被压缩机压缩,该压缩机由至少一个膨胀器驱动,在冰箱中冷却,在第二个回收热交换器中冷却,并被还原。效果:本发明增加了碳氢化合物的输出> 2 + .; 2 cl,2 dwg

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