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    Method and system for regulation of cooling capacity of a cooling system based on a gas expansion process
    3.
    发明授权
    Method and system for regulation of cooling capacity of a cooling system based on a gas expansion process 有权
    基于气体膨胀过程调节冷却系统的冷却能力的方法和系统

    公开(公告)号：US09528758B2

    公开(公告)日：2016-12-27

    申请号：US12734937

    申请日：2008-12-05

    Applicant: Inge L. Nilsen

    Inventor： Inge L. Nilsen

    IPC: F25J3/06 ,  F25J1/02 ,  F25B9/02 ,  F25J1/00

    CPC classification number: F25J1/0236 ,  F25B9/02 ,  F25B2400/23 ,  F25J1/0022 ,  F25J1/005 ,  F25J1/0052 ,  F25J1/0072 ,  F25J1/0082 ,  F25J1/0204 ,  F25J1/0212 ,  F25J1/0245 ,  F25J1/0249 ,  F25J1/0278 ,  F25J1/0288 ,  F25J1/0294 ,  F25J1/0298 ,  F25J2220/64 ,  F25J2240/60 ,  F25J2270/16 ,  F25J2280/02 ,  F25J2290/62

    Abstract: A method and associated system for regulation of the cooling capacity of a cooling system that uses a gas expansion cooling circuit where the cooling principle is expansion of one or more gaseous cooling medium streams from a higher pressure to a lower pressure are described, characterised by the following steps: —reducing the amount of cooling medium which is circulated in the cooling circuit (100) temporarily in that a fraction of gaseous cooling medium is pre-cooled at a higher pressure and is extracted from the cooling circuit (100), —expanding the fraction of cooled gaseous cooling medium across an expansion device (102) to a lower pressure so that at least one part of liquid cooling medium separates, —separating the liquid from the non-condensed gas for temporary storage in a storage unit (104) so that the liquid is temporarily not circulated in the otherwise closed cooling circuit (100), —thereafter to return temporarily stored gaseous cooling medium from the storage unit (104) to the cooling circuit (100) according to need, and—returning non-condensed gas and evaporated cooling medium from the storage unit (104) to a suitable location in the cooling circuit (100). A system to reduce the cooling capacity of a cooling installation based on gas expansion cooling, is also described.

    Abstract translation: 描述了一种用于调节使用气体膨胀冷却回路的冷却系统的冷却能力的方法和相关系统，其中冷却原理是将一种或多种气态冷却介质流从较高压力膨胀到较低压力，其特征在于， 以下步骤： - 减少在冷却回路（100）中循环的冷却介质的量，其中一部分气态冷却介质在较高压力下被预冷却并从冷却回路（100）中提取出来 将冷却的气态冷却介质穿过膨胀装置（102）的分数降低到低压，使得至少一部分液体冷却介质将液体与未冷凝气体分离，以便临时存储在存储单元（104）中， 使得液体暂时不在另外封闭的冷却回路（100）中循环，然后从存储单元返回临时存储的气态冷却介质 （104）到冷却回路（100），并且将非冷凝气体和蒸发的冷却介质从储存单元（104）返回到冷却回路（100）中的适当位置。 还描述了一种降低基于气体膨胀冷却的冷却装置的冷却能力的系统。

    METHOD FOR DRYING NATURAL GAS BY THE JOINT COOLING OF SOLVENT AND NATURAL GAS
    5.
    发明申请
    METHOD FOR DRYING NATURAL GAS BY THE JOINT COOLING OF SOLVENT AND NATURAL GAS 审中-公开
    通过联合冷却溶剂和天然气来干燥天然气的方法

    公开(公告)号：US20120272824A1

    公开(公告)日：2012-11-01

    申请号：US13496146

    申请日：2010-09-13

    Applicant: Johannes Menzel

    Inventor： Johannes Menzel

    IPC: B01D53/26

    CPC classification number: C10L3/10 ,  B01D53/1406 ,  B01D53/263 ,  B01D53/265 ,  B01D2252/2023 ,  B01D2252/2026 ,  B01D2252/20405 ,  B01D2252/20436 ,  F25J1/0022 ,  F25J1/0236 ,  F25J2220/68

    Abstract: A process for the drying of gases which are routed through two or more gas coolers connected in series. The coolers being supplied with a solvent stream absorbing water from the gas entering the respective cooler, with a mixed stream consisting of gas and solvent entering each of these gas coolers, then being routed through the respective cooler and, after joint cooling in the respective cooler, being separated by a gas/liquid separator in the outlet of the respective cooler into a gas stream of reduced water content and a solvent stream laden with water. The water content of the gas is successively reduced from the first cooler to the last cooler and the solvent stream separated and laden with water being either used as feed stream for the upstream cooler or directly returned to the solvent regeneration unit where the water-enriched solvent is again freed from water.

    Abstract translation: 用于干燥气体的方法，其通过串联连接的两个或更多个气体冷却器。 冷却器被提供有从进入各冷却器的气体中吸收水的溶剂流，并且由气体和溶剂组成的混合流进入每个这些气体冷却器，然后通过相应的冷却器被引导，并且在相应冷却器中联合冷却之后 ，由相应冷却器的出口中的气/液分离器分离成具有降低的水含量的气流和含水的溶剂流。 气体的含水量从第一冷却器逐渐降低到最后一个冷却器，分离并充满水的溶剂流被用作上游冷却器的进料流，或直接返回到溶剂再生单元，其中富含水的溶剂 再次摆脱了水。

    Process for the liquefaction of gases
    6.
    发明授权
    Process for the liquefaction of gases 失效
    气体液化过程

    公开(公告)号：US5144806A

    公开(公告)日：1992-09-08

    申请号：US707873

    申请日：1991-05-31

    Applicant: Jochen Frenzel ,  Josef Weber ,  Horst Gutowski, deceased

    Inventor： Jochen Frenzel ,  Josef Weber ,  Horst Gutowski, deceased

    IPC: F25J1/00 ,  F25J1/02 ,  F25J3/08

    CPC classification number: F25J1/0007 ,  F25J1/001 ,  F25J1/0037 ,  F25J1/004 ,  F25J1/0202 ,  F25J1/0224 ,  F25J1/0236 ,  F25J1/0276 ,  F25J2205/20 ,  F25J2205/66 ,  F25J2210/42 ,  F25J2220/02 ,  F25J2245/90 ,  F25J2270/06 ,  F25J2270/912 ,  F25J2280/30 ,  F25J2280/40 ,  F25J2290/60

    Abstract: Gases, e.g., helium, are treated to freeze out impurities in the form of liquid and solids, and resultant gases are liquefied in a refrigerating unit. For automatic control of the freeze purification system, control of this process is responsive to two performance figures, namely, the liquefaction performance of refrigerating unit and the degree of impurities in the available crude gas. The purification process comprises an alternating sequence of purification phases A and regeneration phases B. The amount of gas used in regeneration phase B for liquefaction is additionally produced in purification phase A and intermediately stored in a medium-pressure buffer vessel. The sequence of purification phases A and regeneration phases B is continued up to a pressure P.sub.Mmax in the buffer vessel. Once this pressure is reached, the freeze purification system is regenerated; then, in an idle phase C, the pressure in the buffer vessel is reduced to P.sub.Mmin by liquefaction of the gas. Then the sequence of purification phases A and regeneration phases B starts again.

    Abstract translation: 处理气体（例如氦气）以冷冻液体和固体形式的杂质，并将所得气体在制冷单元中液化。 对于冷冻净化系统的自动控制，该过程的控制响应于两个性能图，即制冷单元的液化性能和可用粗气中的杂质含量。 净化过程包括纯化阶段A和再生阶段B的交替序列。用于液化的再生相B中使用的气体量在净化阶段A中另外产生，并且中间储存在中压缓冲容器中。 纯化阶段A和再生阶段B的顺序持续到缓冲容器中的压力PMmax。 一旦达到这个压力，再生冷冻净化系统; 那么在空闲阶段C中，缓冲容器中的压力通过气化液化而降低到PMmin。 然后再次开始纯化阶段A和再生阶段B的顺序。

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