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    • 5. 发明公开
    • Air separation
    • Lufttrennung。
    • EP0259070A2
    • 1988-03-09
    • EP87307389.4
    • 1987-08-21
    • The BOC Group plc
    • Atkinson, Timothy David
    • F25J3/04
    • F25J3/0466F25J3/04284F25J3/04309F25J3/04351F25J3/0446F25J3/04533F25J3/04575F25J3/04581F25J2200/02F25J2200/50F25J2205/02F25J2235/50F25J2235/52F25J2235/58F25J2240/80Y10S62/924
    • Purified air typically at its dew point is passed into distillation column 10 through inlet 2. Oxygen-rich liquid is withdrawn through outlet 6 and is passed to the top of a mixing column 20. Nitrogen-rich vapour passes from the top of the distillation column 10 to the bottom of the mixing column 20. In the mixing column, there is a downward flow of liquid that becomes progressively richer in nitrogen and an upward flow of vapour that becomes progressively richer in oxygen. Liquid nitrogen is withdrawn from the mixing column 20 through outlet 16 and is returned to the distillation column 10 to provide reflux for the distillation column 10. In addition a mixed stream 28 comprising oxygen and nitrogen is withdrawn from the column 20 as product or waste. The mixing column 20 is provided with a first condenser 30 at its top and a second condenser 40 which takes a vapour stream from intermediate the outlet 28 and the top of the column 20 and returns liquid to the column 20. The second condensation is effected by heat exchange with boiling liquid taken from and returned to the column 10. An argon-enriched oxygen stream is withdrawn (in 4) from the column 10 and is separated in a second distillation column 50 to yield an argon product.
    • 通常在其露点的纯化空气通过入口2进入蒸馏塔10.富氧液体通过出口6排出并通过混合塔20的顶部。富氮蒸气从蒸馏塔顶部通过 10在混合塔20的底部。在混合塔中,存在下降的液体流,其逐渐变得富含氮气,并且蒸气的向上流动变得越来越富氧。 液氮通过出口16从混合塔20中排出并返回到蒸馏塔10中,为蒸馏塔10提供回流。此外,包含氧和氮的混合物流28作为产物或废物从塔20中排出。 混合塔20在其顶部设置有第一冷凝器30和第二冷凝器40,第二冷凝器40从出口28的中部和塔20的顶部获取蒸气流并将液体返回到塔20中。第二冷凝通过 与沸腾的液体进行热交换并从塔10回收。从塔10中取出富含氩的氧气流(在4中),并在第二蒸馏塔50中分离出氩气产物。
    • 7. 发明公开
    • Air separation method and apparatus
    • Verfahren und Vorrichtungfürdie Lufttrennung。
    • EP0202843A2
    • 1986-11-26
    • EP86303609.1
    • 1986-05-12
    • The BOC Group plc
    • Atkinson, Timothy DavidLavin, John Terence
    • F25J3/04
    • F25J3/0446F25J3/0466F25J2200/02F25J2200/50F25J2205/90
    • Cooled and purified air is admitted to a single distillation column 2 through an inlet 4. The air is separated in the column 2 into oxygen and nitrogen fraction. A gaseous nitrogen stream is passed from the top of the column 2 through column 24 into a mixing chamber 26 where it is mixed with a liquid oxygen stream withdrawn from the bottom of the column 2 through a conduit 22. The resulting mixture is expanded through expansion valve 30 and is then used to condense nitrogen vapour, taken from the top of the column 2, in heat exchanger 32. The resulting nitrogen condensate is returned to the top of the column 2 through conduit 36 and adds to the reflux produced for the column by a condenser 8. The column 2 is provided with a side column 12 that produces an argon product.
    • 冷却和纯化的空气通过入口4进入单个蒸馏塔2.空气在塔2中分离成氧和氮馏分。 气态氮气流从塔2的顶部通过塔24进入混合室26,在该混合室26中与通过管道22从塔2的底部排出的液氧流混合。所得混合物通过膨胀膨胀 阀30,然后用于冷凝在热交换器32中从塔2的顶部取出的氮蒸气。所得到的氮冷凝物通过导管36返回到塔2的顶部,并加入到塔中产生的回流 通过冷凝器8.柱2设置有产生氩产物的侧柱12。