CRYOGENIC COOLING DEVICE
    1.
    发明申请

    公开(公告)号:US20240377107A1

    公开(公告)日:2024-11-14

    申请号:US18780370

    申请日:2024-07-22

    Abstract: A cryogenic cooling device includes: a cooling system including a cryocooler that includes a precooling stage configured to cool a refrigerant, a cooling stage that is disposed to be separated from the precooling stage, and a refrigerant circulation circuit configured to cool the cooling stage with the refrigerant; a fixation portion that is fixed with respect to the precooling stage, is thermally coupled to the precooling stage, and is cooled by the precooling stage; and a cooling stage support member that connects the cooling stage to the fixation portion such that displacement of the cooling stage with respect to the fixation portion is allowed.

    Heating, ventilation, and air-conditioning systems and methods

    公开(公告)号:US11841179B2

    公开(公告)日:2023-12-12

    申请号:US16742351

    申请日:2020-01-14

    Inventor: Michael F Taras

    CPC classification number: F25B9/04 F24F5/0096 F25B9/06 F25B30/02 F25B49/02

    Abstract: A heating, ventilation, and air-conditioning (“HVAC”) system for use with a refrigerant. The HVAC system includes a compressor, a condenser, an expansion device, an evaporator, and a separator. The compressor is operable to compress the refrigerant. The condenser is positioned downstream of the compressor and operable to condense the refrigerant. The expansion device is positioned downstream of the condenser and operable to reduce a pressure of the refrigerant flowing therethrough. The evaporator is positioned downstream of the expansion device and operable to vaporize the refrigerant from the expansion device. The separator is positioned downstream of the expansion device and operable to separate the refrigerant into liquid refrigerant and gaseous refrigerant. The gaseous refrigerant from the separator and the liquid refrigerant from the separator are combined prior to being compressed by the compressor.

    Electronic cooling systems
    5.
    发明授权

    公开(公告)号:US11533828B2

    公开(公告)日:2022-12-20

    申请号:US15930611

    申请日:2020-05-13

    Abstract: Disclosed herein are cooling systems, methods of making cooling systems, and methods of cooling using cooling systems. A cooling system includes a compression container with a coolant that includes a fluid. A valve is arranged on the compression container through which the coolant is released from the compression container. The cooling system further includes a component positioned to receive droplets of the coolant. The component has a surface with a three-dimensional topography that includes a plurality of pillars and a plurality of trenches. The component is an electronic component or a photoelectronic component.

    Bernoulli heat pump having laminar flow of refrigerant

    公开(公告)号:US20220260286A1

    公开(公告)日:2022-08-18

    申请号:US17624854

    申请日:2020-07-09

    Applicant: VENTVIA LTD.

    Inventor: Itzhak MERKSAMER

    Abstract: An improved Bernoulli heat pump, wherein the intake section of a Venturi tube is structured so that when the refrigerant flows from the intake section into and through most of the middle (narrow) section, its flow is essentially laminar. Additionally, a second, bi-phase, component is added to the flowing gaseous refrigerant. Part of the bi-phase component evaporates, reaching super saturation, which state is maintained in the middle section, owing to the laminar flow, increasing heat absorption.

    Systems and methods for providing continuous cooling at cryogenic temperatures

    公开(公告)号:US10724768B2

    公开(公告)日:2020-07-28

    申请号:US15605701

    申请日:2017-05-25

    Abstract: Systems and methods of continuous cooling at cryogenic temperatures. One exemplary aspect involves a refrigeration system that includes: a chamber adapted to hold liquid and gaseous coolant received from a cooling pot; a first adsorption pump having an inlet end in fluid communication with the chamber, the first adsorption pump configured to capture gas from the liquid and gaseous coolant when the first adsorption pump is enabled; a second adsorption pump having an inlet end in fluid communication with the chamber, the second adsorption pump configured to capture gas from the liquid and gaseous coolant when the second adsorption pump is enabled; a first heater or heat switch for desorbing the gas captured by the first adsorption pump; and a second heater or heat switch for desorbing the gas captured by the second adsorption pump.

    Refrigerator and control method thereof

    公开(公告)号:US10422563B2

    公开(公告)日:2019-09-24

    申请号:US15971606

    申请日:2018-05-04

    Abstract: A control method includes initially operating a compressor at the same RPM as an operating RPM of the compressor during a previous cycle, adjusting the RPM in consideration of an operation rate of the previous cycle such that the RPM is increased when the operation rate is greater than a first set value, reduced when the operation rate is less than a second set value, and maintained when the operation rate is within a range between the first set value and the second set value, and operating the compressor at the adjusted RPM, the first set value being greater than the second set value.

    Industrial and hydrocarbon gas liquefaction

    公开(公告)号:US10415878B2

    公开(公告)日:2019-09-17

    申请号:US15078585

    申请日:2016-03-23

    Inventor: Colin Nikiforuk

    Abstract: A method for liquefaction of industrial gases or gas mixtures (hydrocarbon and/or non-hydrocarbon) uses a modified aqua-ammonia absorption refrigeration system (ARP) that is used to chill the gas or gas mixture during the liquefaction process. The gas may be compressed to above its critical point, and the heat of compression energy may be recovered to provide some or all of the thermal energy required to drive the ARP. The method utilizes a Joule Thomson (JT) adiabatic expansion process which results in no requirement for specialty cryogenic rotating equipment. The aqua-ammonia absorption refrigeration system includes a vapor absorber tower (VAT) which permits the recovery of some or all of the heat of solution and heat of condensation energy in the system when anhydrous ammonia vapor is absorbed into a subcooled lean aqua-ammonia solution. The modified ARP with VAT may achieve operating pressures as low as 10 kPa which results in ammonia gas chiller operating temperatures as low as −71 C.

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