Oxygen enrichment process
    2.
    发明授权
    Oxygen enrichment process 失效
    氧气浓缩过程

    公开(公告)号:US6004378A

    公开(公告)日:1999-12-21

    申请号:US840357

    申请日:1992-02-24

    Abstract: In an adsorptive alternating pressure process for the enrichment of air with oxygen using a molecular sieve zeolite in an adsorber, wherein adsorbed components are desorbed under a pressure below the pressure at which air separation and N.sub.2 adsorption is effected and, after desorption, the molecular sieve adsorber is at least partly returned to the air separation pressure with oxygen gas produced in countercurrent to the air separation gas flow, the improvement which comprises cooling product gas and covering the molecular sieve adsorber with the cooled product gas.

    Abstract translation: 在用吸附剂中的分子筛沸石富集空气的吸附交替压力方法中,吸附组分在低于空气分离和N 2吸附作用的压力的压力下解吸,并且在解吸后,分子筛 吸附器至少部分地与空气分离气体流逆流产生的氧气返回到空气分离压力,其改进包括冷却产物气体并用冷却的产物气覆盖分子筛吸附器。

    Adsorptive oxygen enrichment of air with mixtures of molecular sieve
zeolites
    4.
    发明授权
    Adsorptive oxygen enrichment of air with mixtures of molecular sieve zeolites 失效
    吸附氧富集空气与分子筛沸石混合物

    公开(公告)号:US5656066A

    公开(公告)日:1997-08-12

    申请号:US648524

    申请日:1996-05-13

    Abstract: An improved process for the oxygen enrichment of air by vacuum swing adsorption, pressure swing adsorption or a combination thereof, wherein the improvement comprises providing at least one packing at each of the air inlet to and air outlet from the adsorber, the packing at the air inlet side of the adsorber comprising Na-Ca zeolite X with an SiO.sub.2 /Al.sub.2 O.sub.3 ratio of 2.0 to 2.5 and with a CaO/Al.sub.2 O.sub.3 ratio of 0.4 to 0.75, the ratio being dependent upon the air inlet temperature, at an air inlet temperature of 20.degree. to 30.degree. C., the CaO/Al.sub.2 O.sub.3 ratio of the Na-Ca zeolite X at the inlet zone being 0.4 to 0.6, at an air inlet temperature of 30.degree. to 40.degree. C., the CaO/Al.sub.2 O.sub.3 ratio of the Ca zeolite X at the inlet zone being 0.55 to 0.65 and at an air inlet temperature of 40.degree. to 50.degree. C., the CaO/Al.sub.2 O.sub.3 ratio of the Na-Ca zeolite X at the inlet zone being 0.6 to 0.75, the packing at the air outlet side of the adsorber comprising Na-Ca zeolite A with a CaO/Al.sub.2 O.sub.3 ratio of 0.5 to 1.0 or Na-Ca zeolite X with CaO/Al.sub.2 O.sub.3 ratio of 0.4 to 1.0, above the CaO/Al.sub.2 O.sub.3 ratio of the Na-Ca zeolite X at the inlet side.

    Abstract translation: 通过真空变压吸附,变压吸附或其组合来改善空气富氧的方法,其中改进包括在吸附器的空气入口和空气出口的每个处提供至少一个填料,空气中的填料 吸附器的入口侧包含SiO 2 / Al 2 O 3比为2.0至2.5且CaO / Al 2 O 3比为0.4至0.75的Na-Ca沸石X,该比率取决于空气入口温度,入口温度为20℃ 在30〜40℃,进口温度为30〜40℃的Na-Ca沸石X的CaO / Al 2 O 3比为0〜30℃,CaO / Al 2 O 3比例为 入口处的沸石X为0.55〜0.65,入口温度为40〜50℃,入口区Na-Ca沸石X的CaO / Al2O3比为0.6〜0.75, 包含CaO / Al 2 O 3比例为0.5〜1.0的Na-Ca沸石A的吸附器的出气侧或Na-Ca zeo CaO / Al2O3比为0.4〜1.0,高于入口侧的Na-Ca沸石X的CaO / Al 2 O 3比例。

    Separation process
    7.
    发明授权
    Separation process 失效
    分离过程

    公开(公告)号:US4254062A

    公开(公告)日:1981-03-03

    申请号:US2501

    申请日:1979-01-10

    CPC classification number: C07C17/389

    Abstract: A process for the separation of isomeric dichlorotoluenes is described wherein an isomeric mixture of dichlorotoluenes is passed over a zeolite of the X or Y type, non-adsorbed dichlorotoluene is separated off and the adsorbed dichlorotoluene is eluted from the zeolite by contacting the same with an eluant.

    Abstract translation: 描述了分离异构二氯甲苯的方法,其中将二氯甲苯的异构体混合物通过X或Y型沸石,分离出未吸附的二氯甲苯,并将吸附的二氯甲苯通过与沸石接触而从沸石中洗脱出来 洗脱液

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