Combined service main air/product compressor
    5.
    发明授权
    Combined service main air/product compressor 失效
    组合服务主要空气/产品压缩机

    公开(公告)号:US06393865B1

    公开(公告)日:2002-05-28

    申请号:US09671073

    申请日:2000-09-27

    IPC分类号: F25J300

    摘要: A combined main air/O2 enriched product compressor for use with an air separation unit that produces O2 enriched product is provided that includes a prime mover that drives a bull gear. The bull gear drives at least two pinion gears, and the pinion gears drive several compression stages where at least one compression stage compresses feed air for the air separation unit and at least one compressor stage compresses O2 enriched product from the air separation unit. The combined main air/O2 enriched product compressor satisfies all air separation unit feed air requirements and at least some compression for the oxygen product from the air separation unit. A method is also provided.

    摘要翻译: 提供了与产生富O2产品的空气分离单元一起使用的组合的主要空气/ O2富集产品压缩机,其包括驱动大齿轮的原动机。 大齿轮驱动至少两个小齿轮,并且小齿轮驱动几个压缩级,其中至少一个压缩级压缩用于空气分离单元的进料空气,并且至少一个压缩机级将空气分离单元的富氧产物压缩。 组合的主要空气/ O 2浓缩产品压缩机满足所有空气分离单元进料空气要求和至少一些来自空气分离单元的氧气产品的压缩。 还提供了一种方法。

    Low energy consumption method for separating gaseous mixtures and in
particular for medium purity oxygen production
    8.
    发明授权
    Low energy consumption method for separating gaseous mixtures and in particular for medium purity oxygen production 失效
    用于分离气体混合物的低能量消耗方法,特别是用于中等纯度的氧气生产

    公开(公告)号:US4732597A

    公开(公告)日:1988-03-22

    申请号:US854600

    申请日:1986-04-22

    IPC分类号: F25J3/04 F25J3/02

    摘要: A method for the separation of gaseous mixtures such as air and for producing medium purity oxygen, comprising compressing the gaseous mixture in a first compressor to about 3.9-4.1 atmospheres pressure, passing said compressed gaseous mixture in heat exchange relationship with sub-ambient temperature gaseous nitrogen, dividing the cooled, pressurized gaseous mixture into first and second streams, introducing the first stream into the high pressure chamber of a double rectification column, separating the gaseous mixture in the rectification column into a liquid oxygen-enriched stream and a gaseous nitrogen stream and supplying the gaseous nitrogen stream for cooling the compressed gaseous mixture, removing the liquid oxygen-enriched stream from the low pressure chamber of the rectification column and pumping the liquid, oxygen-enriched steam to a predetermined pressure, cooling the second stream, condensing the cooled second stream and evaporating the oxygen-enriched stream in an evaporator-condenser, delivering the condensed second stream to the high pressure chamber of the rectification column, and heating the oxygen-enriched stream and blending the oxygen-enriched stream with a compressed blend-air stream to the desired oxygen concentration.

    摘要翻译: 一种分离气体混合物如空气和用于产生中等纯度氧气的方法,包括将第一压缩机中的气体混合物压缩至约3.9-4.1大气压,使所述压缩气体混合物与亚环境温度气体 将冷却的加压气体混合物分成第一和第二流,将第一流引入双精馏塔的高压室中,将精馏塔中的气体混合物分离成富氧气流和气态氮气流 并且供应用于冷却压缩气体混合物的气态氮气流,从精馏塔的低压室除去富氧液流,并将液体富氧蒸汽泵送至预定压力,冷却第二流,冷凝第 冷却的第二流并蒸发富氧流 将冷凝的第二流输送到精馏塔的高压室,并加热富氧流并将富氧流与压缩的混合空气流混合至所需的氧浓度。

    METHOD FOR OPERATING AN AIR SEPARATION PLANT

    公开(公告)号:US20180003437A1

    公开(公告)日:2018-01-04

    申请号:US15382910

    申请日:2016-12-19

    IPC分类号: F25J3/04

    摘要: A method for the production of air gases with variable liquid production by the cryogenic separation of air can include the steps of sending a purified and compressed air stream to a cold box under conditions effective for cryogenically separating the air stream into an oxygen product and nitrogen using a system of columns, wherein the purified and compressed air stream is at a feed pressure when entering the system of columns; withdrawing the oxygen product at a product pressure; delivering the oxygen product at a delivery pressure to an oxygen pipeline, wherein the oxygen pipeline has a pipeline pressure; wherein during the second mode of operation, the method can include monitoring the pipeline pressure; reducing the difference between the pipeline pressure and the delivery pressure; and adjusting liquid production from the cold box. By operating the method in a dynamic fashion, additional liquid production can be realized in instances in which the pipeline pressure deviates from its highest value.