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26 条记录 (耗时 0.088 秒)

    Process for the production of a gas by adsorption
    2.
    发明授权
    Process for the production of a gas by adsorption 失效
    通过吸附生产气体的方法

    公开(公告)号：US5549733A

    公开(公告)日：1996-08-27

    申请号：US410310

    申请日：1995-03-24

    申请人： Christine Marot ,  Pierre Petit ,  Xavier Vigor

    发明人： Christine Marot ,  Pierre Petit ,  Xavier Vigor

    IPC分类号： B01D53/04 ,  B01D53/047 ,  C01B13/02

    CPC分类号： B01D53/0476 ,  C01B13/02 ,  B01D2256/12 ,  B01D2259/4003 ,  B01D2259/40067 ,  B01D2259/40081 ,  B01D2259/403 ,  B01D2259/41

    摘要： In a "vacuum" type cycle, the depressurization of a first adsorber at the high pressure of the cycle is effected by placing it in communication with the outlet of a second adsorber at the low pressure of the cycle. This communication takes place simultaneously with countercurrent pumping in a first stage for the second adsorber and in a second stage for the first adsorber, the recompression to the high pressure of the cycle being effected by production gas. Used for the production of oxygen from air.

    摘要翻译： 在“真空”型循环中，通过使第一吸附器在循环的低压下与第二吸附器的出口连通，来实现第一吸附器在该循环的高压下的减压。 该通信与第一吸附器的第一阶段中的逆流泵送和第一吸附器的第二阶段同时进行，通过生产气体对循环的高压进行再压缩。 用于从空气中生产氧气。

    Rotatable device for the separation by adsorption of at least one constituent of a gaseous mixture
    3.
    发明授权
    Rotatable device for the separation by adsorption of at least one constituent of a gaseous mixture 失效
    用于通过吸附气态混合物的至少一种成分进行分离的可旋转装置

    公开(公告)号：US5441559A

    公开(公告)日：1995-08-15

    申请号：US162029

    申请日：1993-12-01

    申请人： Pierre Petit ,  Michel Poteau ,  Jean-Marc Scudier ,  Xavier Vigor

    发明人： Pierre Petit ,  Michel Poteau ,  Jean-Marc Scudier ,  Xavier Vigor

    IPC分类号： B01D53/04 ,  B01D53/06 ,  C01B13/02

    CPC分类号： B01D53/0431 ,  B01D53/0476 ,  B01D53/06 ,  C01B13/0259 ,  B01D2257/102 ,  B01D2259/40005 ,  B01D2259/4068 ,  C01B2210/0046

    摘要： A rotary device including a plurality of vertical prismatic sectors mounted on a first annular plate comprising two arrays of gas passages which communicate with the outer and inner collectors of respective sectors, and interacting with a second plane annular plate on a housing defining a set of inner chambers. The second plate comprises two concentric arrays of apertures which communicate with corresponding chambers in the set of chambers, and are spread out along the path of the two gas passage arrays of the first plate. The device is particularly useful for producing oxygen.

    摘要翻译： PCT No.PCT / FR93 / 00288 Sec。 371日期：1993年12月1日 102（e）日期1993年12月1日PCT 1993年3月23日PCT公布。 出版物WO93 / 20925 日期：1993年10月28日。一种旋转装置，包括安装在第一环形板上的多个垂直棱镜扇区，该第一环形板包括两个气体通道阵列，其与相应扇区的外部和内部收集器连通，并与第二平面环形板相互作用 限定一组内室的壳体。 第二板包括与该组腔室中的相应腔室连通的两个同心孔的阵列，并且沿着第一板的两个气体通道阵列的路径展开。 该装置对于生产氧气特别有用。

    Method for cooling a gaseous mixture to a low temperature
    6.
    再颁专利
    Method for cooling a gaseous mixture to a low temperature 失效

    公开(公告)号：USRE30140E

    公开(公告)日：1979-11-06

    申请号：US501246

    申请日：1974-08-28

    申请人： Maurice Grenier ,  Pierre Petit

    发明人： Maurice Grenier ,  Pierre Petit

    IPC分类号： C07C7/09 ,  C08G77/00 ,  C10G5/06 ,  F25J1/00 ,  F25J3/02

    CPC分类号： F25J3/0257 ,  C07C7/09 ,  C08G77/00 ,  C10G5/06 ,  F25J1/0022 ,  F25J1/004 ,  F25J1/0045 ,  F25J1/0055 ,  F25J1/0202 ,  F25J1/0212 ,  F25J1/0231 ,  F25J1/0237 ,  F25J1/0249 ,  F25J1/025 ,  F25J3/0209 ,  F25J3/0233 ,  F25J3/0242 ,  F25J3/0247 ,  F25J2200/02 ,  F25J2200/50 ,  F25J2200/70 ,  F25J2200/74 ,  F25J2200/76 ,  F25J2200/80 ,  F25J2205/04 ,  F25J2215/04 ,  F25J2215/64 ,  F25J2215/66 ,  F25J2270/12 ,  F25J2290/34

    摘要： .Iadd. .Iadd.8. A method for cooling a second gaseous mixture to low temperature and producing at least one constituent of said mixture in liquid phase, comprising:a. cooling and subjecting first gaseous mixture containing at least one component of said secong gaseous mixture, to a fractionate condensation under a first pressure,b. expanding at least two condensed fractions obtained during the fractionate condensation of said first gaseous mixture, reuniting the expanded condensed fractions with said first gaseous mixture under a second pressure lower than said first pressure, vaporizing and reheating the reunited fractions with said first gaseous mixture under said second pressure, by heat exchange with said second gaseous mixture undergoing cooling, and with said first gaseous mixture undergoing fractionate condensation, and recompressing said first gaseous mixture to said first pressure,c. reuniting under said first pressure said second gaseous mixture undergoing cooling with said first gaseous mixture undergoing fractionate condensation, when said gaseous mixture is in conditions of temperature and pressure such that a major portion of said constituent to be produced in liquid phase is condensed within said second gaseous mixture, and after the first condensed fraction of said first gaseous mixture has been withdrawn for expansion and vaporization, continuing the fractionate condensation of the mixture so obtained under said first pressure until there is obtained a last condensed fraction containing a major part of said constituent to be produced in liquid phase,d. expanding to said second pressure the last condensed fraction, and separating the last expanded fraction into a liquid portion expanded to a pressure lower than said second pressure and a residual gaseous portion for recompression with said first gaseous mixture, and withdrawing said last expanded liquid portion as a product stream, ande. prior to reuniting said first gaseous mixture and said second gaseous mixture, condensing at least partially said second gaseous mixture under a third pressure which is higher than said first pressure, and expanding said second gaseous mixture at least partially condensed to said first pressure. .Iaddend.