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    • 82. 发明授权
    • Method for storing a subcooled liquid
    • 储存液体液体的方法
    • US3812683A
    • 1974-05-28
    • US25311072
    • 1972-05-15
    • CHICAGO BRIDGE & IRON CO
    • LAVERMAN R
    • F17C9/00F17C5/02
    • F17C9/00F17C2201/0109F17C2201/0119F17C2201/054F17C2203/03F17C2203/0629F17C2205/018F17C2223/0161
    • An enclosed cryogenic storage tank having an insulated bottom, a vertical insulated wall projecting upwardly from the bottom, an insulated roof projecting to the wall and completely covering the space surrounded by the wall, and an insulated deck inside and extending across the tank at a fixed location between the tank bottom and tank roof. A process of removing a subcooled liquefied gas from the space beneath an insulated deck in an insulated cryogenic storage tank, feeding the removed subcooled liquefied gas in heat exchange with a stream of warm liquefied gas of the same composition as the subcooled liquefied gas to cool the warm stream, returning the subcooled liquefied gas to the tank below the deck, and feeding the cooled stream of liquefied gas to the tank above the deck. Alternatively, a stream of the subcooled liquefied gas can be mixed with the steam of warm liquefied gas and the combined stream then fed to the tank above the insulated deck.
    • 封闭的低温储罐,具有绝缘底部,从底部向上突出的垂直绝缘壁,一个绝缘屋顶,突出到墙壁上,完全覆盖由墙壁围绕的空间,以及一个绝缘甲板,内部并以固定的方式延伸穿过水箱 罐底与罐顶之间的位置。
    • 83. 发明授权
    • Life support system and method
    • 生命支持系统和方法
    • US3807396A
    • 1974-04-30
    • US62361667
    • 1967-03-16
    • E & M LABOR
    • FISCHEL H
    • A61M16/10A62B7/06B63C11/24F17C9/00F17C9/02F25J3/04F25J3/08
    • A62B7/06A61M16/10A61M16/1045A61M16/22A61M2202/0208A61M2202/03B63C11/24F17C9/00F17C9/02F17C2265/025F17C2270/02F25J3/04981F25J2210/42F25J2215/02F25J2215/40F25J2270/904A61M2202/0007
    • Life support is provided by a cryogenic closed circuit system for either hyperbaric, isobaric or hypobaric respiratory environments. Oxygen content in a gas mixture is maintained in a selected partial pressure range by establishing thermodynamic equilibrium between a liquid oxygen supply, which is maintained at an appropriate temperature, and a gas mixture within an enclosed volume communicating with the liquid oxygen. Incoming gases are passed into the gas-containing volume and adjusted to an appropriate partial pressure of oxygen solely by virtue of saturation equilibrium, and independently of ambient pressure and gas mixture variations. The useful life of a given oxygen supply volume is greatly extended because of the high compaction ratio of liquid oxygen with respect to oxygen gas at standard temperature and pressure, and because of full physiological use of the oxygen. The temperature of the liquid oxygen may be controlled through the use of a cryogenic reservoir, a cryogenic refrigerator or other means. A heat exchanger may be deployed in the closed circuit system to cool incoming contaminated gases to cryogenic levels and to heat outgoing breathable gases to acceptable levels, and to provide more efficient use of the cryogen. The closed circuit system may further include means for compensating for ambient pressure variations by the injection of an inert gas or gases and for cleansing of incoming gases by removal of water vapor and carbon dioxide.
    • 生命支持由低温闭合回路系统提供,用于高压,等压或低压呼吸环境。 气体混合物中的氧含量通过建立保持在适当温度的液氧供应与与液氧连通的封闭容积内的气体混合物之间的热力学平衡而保持在选择的分压范围内。 进入的气体进入含气体积并仅通过饱和平衡调节到适当的氧气分压,并且独立于环境压力和气体混合物变化。 由于在标准温度和压力下液氧对于氧气的压实比高,并且由于氧气的完全生理使用,所以给定供氧体积的使用寿命大大延长。 可以通过使用低温储存器,低温冰箱或其他方式来控制液氧的温度。 热交换器可以部署在闭路系统中以将进入的污染气体冷却到低温水平,并将输出的可呼吸气体加热到可接受的水平,并提供更有效地使用冷冻剂。 闭路系统还可以包括用于通过注入惰性气体或气体来补偿环境压力变化的装置,以及通过去除水蒸汽和二氧化碳来清洁进入的气体。
    • 84. 发明授权
    • Transfer device for cryogenic fluids
    • 低温流体转移装置
    • US3648018A
    • 1972-03-07
    • US3648018D
    • 1970-02-05
    • DOW CHEMICAL CO
    • CHENG CHIN HUANLEONARD DONALD E
    • F17C9/00F22B1/28
    • F17C9/00F17C2221/011F17C2221/014F17C2221/017F17C2223/0161F17C2223/047F17C2225/047Y10T137/6606
    • Disclosed is a device for transferring a cryogenic fluid from its storage vessel to cryostat or other vessel. The device is an open ended tube of sufficient length to permit its lower extremity to project below the surface of the fluid when it is inserted into an opening in the vessel. The tube is fitted with a collar which forms a substantially airtight seal between the tube and the opening. A heater capable of producing sufficient heat to vaporize part of the fluid is attached to the tube. The vaporization creates an internal pressure which forces the fluid up through the tube. By insulating the heater from the tube so that the fluid forced into the tube is not vaporized, a steady flow of cryogenic fluid is delivered to a desired location, e.g., a cryostat.
    • 公开了一种用于将低温流体从其存储容器转移到低温恒温器或其他容器的装置。 该装置是足够长度的开口管,当其插入容器中的开口中时,允许其下端在流体表面下方突出。 管装配有一个在管和开口之间形成基本气密密封的套环。 能够产生足够的热量以蒸发部分流体的加热器附接到管。 蒸发产生内部压力,迫使流体向上通过管。 通过将加热器与管隔离,使得强制进入管的流体不被蒸发,将低温流体的稳定流量输送到期望的位置,例如低温恒温器。
    • 87. 发明授权
    • Means for removal of liquefied gas
    • US3123983A
    • 1964-03-10
    • US3123983D
    • B63B27/24F04D13/12F17C9/00
    • B63B27/24F04D13/12F17C9/00F17C2205/0338F17C2221/033F17C2223/0161F17C2223/033F17C2227/0135F17C2227/0157F17C2227/0178F17C2227/0185F17C2227/0192F17C2260/032
    • 959,493. Pumping systems for liquefied gases. CONCH INTERNATIONAL METHANE Ltd. Dec. 1, 1961 [Jan. 16, 1961], No. 43101/61. Headings F1C, F1G, F1R and F1T. [Also in Division B8] A pumping system for liquids such as liquefied natural gases comprises a turbine 16 driving a pump 10 near the bottom of the liquid container and the working fluid has a solidification temperature below the temperature of the liquid 18 in the container 14. The turbine 16 may be driven by a combination of liquid and gas in which case the turbine exhaust fluid passes through a condenser 40 below the liquid level. After passing through the pump, the pressurised liquid is vaporised in a heat exchanger 50 and led to the turbine in an insulated pipe. If the turbine working fluid has a liquefaction temperature below the temperature of the liquid 18 then the pressurised working fluid passes through a pressure regulator fitted externally of the tank. The working fluid may be the vapour from the liquid in which case it is drawn off from the interior of the container (Fig. 4). Vapour from the container may pass into a separator (Fig. 3 not shown) or directly to the turbine 16 via a compressor 68. The exhaust from the turbine may pass into the line 22 and assist the flow of the effluent from the pump 10 in which case the vapour and liquid pass into the separator, the vapour passing to the compressor or back to the container and the liquid passing to a delivery line. In the event of a pump failure, or to assist the pump, compressed vapour may be passed through the delivery line. This pumping system ensures that vapour is returned to the container to counteract any pressure drop as the liquid level falls. In a modified form of this embodiment, (Fig. 4), the turbine exhaust is led directly to an accumulator 82, which also serves as a separator, and the line 70 has a by-pass 82 leading directly to the delivery line 22 the liquid being pumped direct to a separator 102. When the turbine 16 and pump 10 are inoperative the valve 78 and valves 84, 88 may be opened and liquid is pumped by vapour pressure into the accumulator 82, which has a relief valve 98. The liquid drains through lines 90, 92, 106 to a delivery reservoir.