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    Air separation method and apparatus
    81.
    发明授权
    Air separation method and apparatus 有权
    空气分离方法和装置

    公开(公告)号：US09222725B2

    公开(公告)日：2015-12-29

    申请号：US11818636

    申请日：2007-06-15

    申请人： Neil Mark Prosser ,  Richard John Jibb

    发明人： Neil Mark Prosser ,  Richard John Jibb

    IPC分类号： F25J3/04 ,  F25J5/00

    CPC分类号： F25J3/04187 ,  F25J3/04084 ,  F25J3/0409 ,  F25J3/04218 ,  F25J3/0423 ,  F25J3/04236 ,  F25J3/04303 ,  F25J3/04387 ,  F25J3/04412 ,  F25J3/04678 ,  F25J5/00 ,  F25J2240/10 ,  F25J2290/12 ,  F25J2290/32 ,  F25J2290/44

    摘要： A compressed air stream is cooled to a temperature suitable for its rectification within a lower pressure heat exchanger and a boosted pressure air stream is liquefied or converted to a dense phase fluid within a higher pressure heat exchanger in order to vaporize pumped liquid products. Thermal balancing within the plant is effectuated with the use of waste nitrogen streams that are introduced into the higher and lower pressure heat exchangers. The heat exchangers are configured such that the flow area for the subsidiary waste nitrogen stream within the higher pressure heat exchanger is less than that would otherwise be required so that the subsidiary waste nitrogen streams were subjected to equal pressure drops in the higher and lower pressure heat exchangers. This allows the higher pressure heat exchanger be fabricated with a reduced height and therefore a decrease in fabrication costs.

    摘要翻译： 将压缩空气流冷却到适合于在低压热交换器内进行精馏的温度，并且在高压热交换器中将增压空气流液化或转化成致密相流体，以便蒸发泵送的液体产物。 使用引入高压和低压热交换器的废氮气流来实现设备内的热平衡。 热交换器被构造成使得在高压热交换器内的辅助废氮流的流动面积小于另外需要的流动面积，使得辅助废氮气流在较高和较低的压力热中受到相等的压降 交换器。 这允许以较低的高度制造高压热交换器，因此制造成本降低。

    Refrigeration Method and Installation
    82.
    发明申请
    Refrigeration Method and Installation 审中-公开
    制冷方法和安装

    公开(公告)号：US20140238074A1

    公开(公告)日：2014-08-28

    申请号：US14346601

    申请日：2012-08-14

    申请人： Jean-Marc Bernhardt ,  Cindy Deschildre ,  Eric Fauve ,  David Grillot

    发明人： Jean-Marc Bernhardt ,  Cindy Deschildre ,  Eric Fauve ,  David Grillot

    IPC分类号： F25B9/00

    CPC分类号： F25B5/02 ,  F25B1/10 ,  F25B9/002 ,  F25B43/02 ,  F25J1/0065 ,  F25J1/0201 ,  F25J1/0265 ,  F25J1/027 ,  F25J1/0271 ,  F25J1/0272 ,  F25J1/0279 ,  F25J1/0294 ,  F25J5/00 ,  F25J2230/20 ,  F25J2230/24 ,  F25J2270/912

    摘要： Method and installation for refrigerating the same application by means of several refrigerators/liquefiers disposed in parallel, the refrigerators/liquefiers in parallel using a working gas of the same nature having a low molar mass, that is to say having a mean total molar mass of less than 10 g/mol such as pure gaseous helium, each refrigerator/liquefier comprising a station for compressing the working gas, a cold box intended to cool the working gas at the output from the compression station, the working gas cooled by each of the respective cold boxes of the refrigerators/liquefiers being put in thermal exchange with the application with a view to supplying cold to the latter, in which a single compression station compresses the working gas for each of the respective separate cold boxes of the refrigerators/liquefiers disposed in parallel, the single compression station comprising only compression machines of the lubricated-screw type and systems for removing oil from the working fluid output from the compression machines, so that the compression machines and the oil-removal systems are shared by the refrigerators/liquefiers disposed in parallel.

    摘要翻译： 通过并联设置的几台冰箱/液化器对同一应用进行制冷的方法和装置，使用具有低摩尔质量的相同性质的工作气体平行地使用冰箱/液化器，也就是说具有平均总摩尔质量 小于10g / mol，例如纯气态氦，每个冰箱/液化器包括用于压缩工作气体的站，用于冷却来自压缩站输出的工作气体的冷箱， 各冷藏箱/液化器的冷箱与应用程序进行热交换，以向后者供应冷气，其中单个压缩站压缩设置的冰箱/液化器的各个分开的冷箱中的工作气体 并联地，单个压缩站仅包括润滑螺杆式压缩机和用于从工作f中除去油的系统 通过压缩机输出，从而压缩机和除油系统由平行设置的冰箱/液化器共享。

    Process for separation of gas mixture
    83.
    发明授权
    Process for separation of gas mixture 失效
    气体混合物分离方法

    公开(公告)号：US4474590A

    公开(公告)日：1984-10-02

    申请号：US500726

    申请日：1983-06-03

    申请人： Bernard A. Bucchianeri

    发明人： Bernard A. Bucchianeri

    IPC分类号： C10K1/20 ,  F25J5/00 ,  F25J3/02

    CPC分类号： C10K1/20 ,  F25J5/00

    摘要： A process for the purification of the low-boiling constituents of a compresed gas mixture, such as a mixture comprising a carbonaceous gas, by cooling to low temperatures in cyclical alternated regenerators to condense high-boiling constituents of the gas mixture comprising (1) passing the gas mixture through a first regenerator from the warm end to the cold end of the same to cool the gas mixture and to condense the high-boiling constituents of the mixture thereby producing a purified gas stream; (2) passing a scavenging gas which is at a lower pressure than said gas mixture in the first regenerator through a second regenerator from the cold end to the warm end of the same to clean this second regenerator and to re-evaporate the high-boiling constituents, (3) passing at least part of the purified gas stream through a third regenerator from the cold end to the warm end of the same to re-cool this third regenerator, preferably to the temperature of the first regenerator, and (4) compressing and recycling at least part of the scavenging gas which has passed through the second regenerator through the first regenerator from the warm end to the cold end and repeating the process as defined above.

    摘要翻译： 一种用于纯化混合气体混合物的低沸点组分的方法，所述混合物包括含碳气体，通过在循环交替的再生器中冷却至低温以冷凝气体混合物的高沸点组分，其包括（1）通过 气体混合物通过第一再生器从其温热端到冷端，冷却气体混合物并使混合物的高沸点组分冷凝，从而产生纯化的气流; （2）将来自第一再生器的压力低于所述第一再生器中的气体混合物的清扫气体从第二再生器通过冷端至其温端，以清洁该第二再生器并重新蒸发高沸点 （3）将至少部分净化气流通过第三再生器从冷端传递至其温端，以再次冷却该第三再生器，优选至第一再生器的温度，以及（4） 将已经通过第二再生器的至少部分清除气体从第一再生器从热端压缩并再循环到冷端并重复如上所述的过程。

    Temperature control method for reversing type heat exchanger group of air separation system
    84.
    发明授权
    Temperature control method for reversing type heat exchanger group of air separation system 失效
    空气分离系统换向换热器组的温度控制方法

    公开(公告)号：US4459143A

    公开(公告)日：1984-07-10

    申请号：US451960

    申请日：1982-12-21

    申请人： Makoto Nawata ,  Norio Nakazato ,  Sachihiro Yoshimatsu ,  Youichi Itou ,  Kengo Sugiyama ,  Yasuo Tasaka

    发明人： Makoto Nawata ,  Norio Nakazato ,  Sachihiro Yoshimatsu ,  Youichi Itou ,  Kengo Sugiyama ,  Yasuo Tasaka

    IPC分类号： F28F27/02 ,  F25J3/04 ,  F25J5/00 ,  F28F27/00

    CPC分类号： F25J5/00 ,  F28F27/00 ,  F25J2210/40 ,  F25J2280/02

    摘要： A temperature control method for a reversing type heat exchanger group wherein an outlet temperature of reheating gas of an arbitrarily selected reversing type heat exchanger which serves as a reference in the reversing heat exchanger group is rendered equal in value to a reference control temperature set beforehand in such a manner so as to satisfy the sweeping temperature difference. The outlet temperatures of the reheating gas in the other reversing type heat exchangers of the reversing type heat exchanger group are rendered equal in value to the outlet temperature of the reheating gas in the reversing type heat exchanger serving as the reference. Thus, the temperature of the cold end of all of the reversing type heat exchangers of the reversing type heat exchanger group are caused to be balanced equally whereby ice and dry ice deposited on the feed water channels can be effectively removed by a sweeping action.

    摘要翻译： 用于反转型热交换器组的温度控制方法，其中在换向换热器组中作为基准的任意选择的换向换热器的再加热气体的出口温度与预先设定的参考控制温度相等 以满足扫描温度差的方式。 反转型热交换器组的其他换向型热交换器中的再加热气体的出口温度与作为基准的换向型热交换器中的再加热气体的出口温度相等。 因此，使逆变型热交换器组的所有反向型热交换器的冷端的温度平衡地平衡，从而可以通过扫掠动作有效地去除沉积在给水通道上的冰和干冰。

    Process and apparatus for the separation of a hydrogen-containing gaseous mixture
    85.
    发明授权
    Process and apparatus for the separation of a hydrogen-containing gaseous mixture 失效
    用于分离含氢气体混合物的方法和装置

    公开(公告)号：US3654769A

    公开(公告)日：1972-04-11

    申请号：US3654769D

    申请日：1968-10-31

    申请人： LINDE AG ZENTRALE PATENTABLEIL

    发明人： LINDE HERMANN

    IPC分类号： F25J5/00 ,  F25J3/00 ,  F25J3/08

    CPC分类号： F25J5/00 ,  Y10S62/934

    摘要： A process and apparatus is provided for separation of a hydrogen-containing gaseous mixture, wherein the gaseous mixture is separated into a condensate fraction and a crude hydrogen fraction containing the hydrogen in addition to other residual components. Separation is accomplished by refrigeration under pressure in at least two reversible regenerators which are charged alternately with crude gas and scavenging gas. The crude hydrogen, after further cooling by partial condensation or by a washing step with liquid nitrogen, is freed of the residues of other components. The purified hydrogen product, which can optionally contain nitrogen, is engine-expanded for the purpose of producing refrigeration and then conducted through heat exchange coils in at least one of the regenerators.

    摘要翻译： 提供了一种用于分离含氢气体混合物的方法和装置，其中除了其它残余组分之外，将气体混合物分离成冷凝物部分和含有氢的粗制氢馏分。 分离是通过在至少两个可逆的再生器中在压力下冷冻来完成的，这些可再生的再生器与粗气体和清除气体交替地进行充电。 粗氢气在通过部分冷凝进一步冷却或用液氮洗涤步骤后，不含其它成分的残留物。 可以任选地含有氮气的纯化的氢产物是发动机膨胀的，用于产生制冷，然后通过至少一个再生器中的热交换盘管进行。