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Process for separating vinyl esters from a gas stream comprising ethylene and vinyl esters

机译:从包含乙烯和乙烯基酯的气流中分离乙烯基酯的方法

摘要

Process for separating esters of vinyl alcohol from a gas stream comprising from 70 to 99.5% by weight of ethylene and from 0.5 to 30% by weight of esters of vinyl alcohol being at a pressure in the range of from 0.5 MPa to 10 MPa and a temperature in the range of from 5°C to 50°C comprising the steps ofa) cooling the gas stream in a first heat exchanger by means of a cooling medium to a temperature of from -5°C to 40°C;b) withdrawing the not condensed part of the gas stream from the first heat exchanger and transferring it to a second heat exchanger;c) cooling the gas stream in the second heat exchanger to a temperature of from -20°C to 5°C;d) withdrawing the not condensed part of the gas stream from the second heat exchanger, reducing the pressure of the gas stream to from 0.5 MPa to 3 MPa and transferring it to a separation vessel;e) withdrawing the not condensed part of the gas stream from the separation vessel and transferring it as cooling medium to the second heat exchanger; andf) withdrawing the cooling medium as ethylene gas stream with a reduced content of esters of vinyl alcohol from the second heat exchanger,and process for copolymerizing ethylene and esters of vinyl alcohol in the presence of free-radical polymerization initiators at pressures in the range of from 110 MPa to 500 MPa and temperatures in the range of from 100°C to 350°C in a continuously operated polymerization apparatus comprising such a process for separating esters of vinyl alcohol from a gas stream comprising from 70 to 99.5% by weight of ethylene and from 0.5 to 30% by weight of esters of vinyl alcohol.
机译:在压力为0.5MPa至10MPa,压力为0.5MPa至10MPa的条件下从包含70至99.5重量%的乙烯和0.5至30重量%的乙烯醇的酯的气流中分离乙烯醇的酯的方法。温度范围为5°C至50°C,包括以下步骤:a)在第一热交换器中借助于冷却介质将气流冷却至-5℃至40℃的温度;b)从第一热交换器中取出未冷凝的气流部分,并将其转移到第二热交换器中;c)将第二热交换器中的气流冷却至-20°C至5°C;d)从第二热交换器中取出未冷凝的气流部分,将气流的压力从0.5MPa降低到3MPa,并将其转移到分离容器中;e)从分离容器中抽出未冷凝的部分气流,并将其作为冷却介质转移到第二热交换器;和f)从第二换热器中抽出冷却介质,将其作为乙烯气流,减少乙烯醇的酯含量,连续操作的聚合反应中,在自由基聚合引发剂的存在下,在110 MPa至500 MPa的压力和100℃至350℃的温度下使乙烯和乙烯醇的酯共聚的方法和方法包括这样一种用于从气流中分离出乙烯醇的酯的方法的装置,该气流包含70至99.5重量%的乙烯和0.5至30重量%的乙烯醇的酯。

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