| Class / Patent application number | Description | Number of patent applications / Date published |
|---|
| 062480100 | With vapor discharged from storage receptacle | 67 |
| 20080209916 | Apparatus and method for flowing compressed fluids into and out of containment - Methods for loading a compressed fluid, such as natural gas, into and discharging the compressed fluid out of containment are provided. The compressed fluid is injected into a bottom portion of a container system for storage and/or transport until a target pressure is reached after which gas is withdrawn from an upper portion of the container system at a rate to maintain the target pressure while the compressed fluid is injected in the bottom portion. The compressed fluid is cooled through an expansion valve and by refrigerated chillers or by injecting a cold liquid of the same chemical composition as the compressed fluid, such as liquid natural gas, into the compressed fluid prior to injection into the container system. Withdrawal or discharge from the container system to a receiving facility begins with blow down from the bottom portion of the container system without a displacement fluid and continues until pressure falls below an acceptable differential pressure. The discharge stream is passed through a separator and a light gas from the separator is pressurized and injected into an upper portion of the container system to drive the compressed fluid out the bottom. The light gas is pressurized using either a compressor or a heated tank system, where two vessels operate in parallel, trapping and heating the light gas and then discharging to the container system from one while filling the other and alternating the operation between the two. | 09-04-2008 |
| 20080256959 | Vessel - A water-going liquefied carbon dioxide (LCD) transport vessel comprising a pressurised and refrigerated LCD container, a cargo discharge pump within said container for pumping LCD out of said container along a conduit, a booster pump for pumping LCD along the conduit to a platform, a first backflow line downstream of the cargo pump to the container, a second backflow line from downstream of the booster pump to the container, and optionally a heater arranged to heat LCD flowing from said vessel along the conduit. | 10-23-2008 |
| 20080264072 | LIQUEFIED GAS SUPPLY DEVICE AND METHOD - To provide a liquefied gas supply device and supply method that has good operability and a compact structure, and enables stable supply of large flow rates of liquefied gas while managing the consumption amount of liquefied gas promptly in real time. A liquefied gas supply device characterized by having container | 10-30-2008 |
| 20080282709 | LIQUIFIED GAS SUPPLY SYSTEM AND METHOD THEREOF - A liquefied gas supply system and method can supply the liquefied gas in a plurality of liquefied gas containers uniformly to supply huge amount of gas constantly. A liquefied gas supply system comprises a plurality of liquefied gas containers | 11-20-2008 |
| 20090090112 | SYSTEM AND METHOD FOR CRYOGENIC ENHANCEMENT TO MECHANICAL FREEZERS - A cryogenic enhanced mechanical freezer system and method are provided. The disclosed system includes a mechanical freezer compartment adapted for freezing food products on a conveyor, a cryogen injection system adapted to directly inject cryogen into a shrouded zone proximate the conveyor in the mechanical freezer compartment, an exhaust system adapted to rapidly evacuate cryogen vapors from the freezer compartment; and a freezer control system adapted to operatively control the exhaust system and cryogen injection system in response to selected inputs so as to not adversely affect the mechanical refrigeration capacity associated with the mechanical freezer. The selected inputs may include user inputs as well as inputs received from one or more temperature sensors disposed in the freezer compartment and a gas analyzer adapted to monitor concentrations of selected gases within the freezer compartment. Access to the freezer compartment is prevented using a door interlock arrangement during any cryogen injection operations and when the atmosphere in the freezer compartment is not safe as determined by the gas analyzer. | 04-09-2009 |
| 20090113899 | Systems and Methods for Ultra Low Temperature Storage - Systems and methods are disclosed to provide an ultra low temperature (ULT) cryogenic processor apparatus. The apparatus includes an external housing with flat sides; an inner housing coupled to the external housing to define a vacuum region there between; material disposed in the vacuum region to provide redundant insulation and structural support; and a cryogenic heat exchanger contained in the inner housing. | 05-07-2009 |
| 20090266086 | FLOATING MARINE STRUCTURE HAVING LNG CIRCULATING DEVICE - Disclosed is an apparatus for containing LNG. The apparatus includes an LNG tank containing liquid phase LNG and boil-off gas of LNG, and an circulating device. The circulating device includes an intake port and a discharge port. The circulating device further includes an flowing pathway from the intake port to the discharge port that does not include a forced LNG liquefying device. The intake port is located in an upper portion of the LNG tank, and the discharge port is located in a lower portion of the LNG tank substantially lower than the intake port. The circulating device is configured to suction, through the intake port, boil-off gas from the upper portion of the LNG tank and to discharge boil-off gas, through the discharge port, to the lower portion of the LNG tank. | 10-29-2009 |
| 20090314009 | VACUUM ACTUATED VALVE FOR HIGH CAPACITY STORAGE AND DELIVERY SYSTEMS - The invention relates to a re-configured valve design to accommodate a high volume of product in the delivery system and the dispensation of product upon the application of a predetermined vacuum condition on the downstream side of the valve. | 12-24-2009 |
| 20100089071 | Apparatus For Recovery Of Volatile Organic Compound Vapor - A self-contained unit which is automated for safety and efficiency recovers emissions present as a result of loading volatile organic compositions at marine or land based vessels or terminals. The unit is enclosed for protection of its components from wind, weather and the saltwater marine environment, while including venting for protection against possible vapor build-up. The unit also includes required support services and materials, and also includes structure for protection against transfer of explosion back into the cargo vessel or terminal. | 04-15-2010 |
| 20100236259 | Operating Method for a Cryo-Compressed Tank - An operating method is provided for a cryo-compressed tank for supplying cryogenic hydrogen to a consumer of a motor vehicle under supercritical pressure at 13 bar or more. In order to compensate for pressure loss resulting from hydrogen removal, the removed hydrogen that has been heated in a heat exchanger is conveyed to a heat exchanger, provided in the cryo-compressed tank, by way of a tank pressure regulating valve and a branch line, which branches off of a supply line leading to the consumer. After flowing through the heat exchanger, it is introduced into the supply line downstream of the branching off of the branch line. Over a period of time that significantly exceeds the cycle times of a conventional frequency valve, either the removed amount of hydrogen is guided without limitation into the heat exchanger, provided in the cryo-compressed tank, the tank pressure regulating valve being completely open, or no return of the heated hydrogen into the heat exchanger occurs at all. Downstream of the branching off of the branch line, the supply line has a pressure regulating unit, which ensures that irrespective of the changes in the pressure in the supply line caused upstream of the pressure regulating unit by switching the tank pressure regulating valve, a sufficient and continuous supply of hydrogen to the consumer at the pressure required is guaranteed. | 09-23-2010 |
| 20110192174 | METHOD FOR REGASIFYING LIQUEFIED NATURAL GAS WITH PREVIOUSLY DEHUMIDIFIED AMBIENT AIR - The method of vaporizing LNG consists in using previously dehumidified ambient air as a direct heat exchange fluid in a first air heat exchanger ( | 08-11-2011 |
| 20110225984 | FREEZER WITH LIQUID CRYOGEN REFRIGERANT AND METHOD - A freezer that uses liquid cryogen as a refrigerant includes an inner vessel defining a storage chamber and an outer jacket generally surrounding the inner vessel so that an insulation space is defined there between. A heat exchanger is positioned in a top portion of the storage chamber and has an inlet in communication with a supply of the liquid cryogen refrigerant so that the liquid cryogen refrigerant selectively flows through the heat exchanger to cool the storage chamber while being vaporized. A purge line is in communication with the outlet of the heat exchanger and includes a purge outlet positioned over the exterior of the heat exchanger. A purge valve is positioned within the purge line so that the vaporized liquid cryogen from the heat exchanger is selectively directed to the exterior of the heat exchanger to reduce ice formation on the heat exchanger. | 09-22-2011 |
| 20110314838 | GAS SUPPLY DEVICE - The present invention relates to a gas supply device having a compact configuration that enables prevention of vaporized gas by requisite minimum heating means from being liquefied again and an installation area to be considerably reduced. The gas supply device is provided with: a tank configured to retain material liquid; and a mass flow controller that is connected to an inside of the tank through a first valve unit, and controls a flow rate of gas resulting from vaporizing the material liquid, in which inside an outer wall of the tank, an internal flow path is formed, and the internal flow path is provided with a generated gas lead-out line provided with: a first valve flow-in flow path connecting the inside of the tank and a first inlet port; and a first valve flow-out flow path connecting a first outlet port and an introduction port of the mass flow controller . | 12-29-2011 |
| 20120011859 | GAS-FLOW CRYOSTAT FOR DYNAMIC TEMPERATURE REGULATION USING A FLUID LEVEL SENSOR - A gas-flow cryostat adapted for dynamic temperature regulation using a fluid level sensor; the cryostat further including one or more heaters coupled to various components of the cryostat. As fluid evaporates from a liquid coolant evaporation reservoir within the cryostat, the fluid level sensor and a feedback control unit are adapted to monitor and dynamically control the level of evaporating coolant by regulating the heaters. Accordingly, the cryostat is adapted to dynamically control temperature about a specimen region within the cryostat. The cryostat can be used in various applications, including analytical laboratory equipment for measuring various physical properties of samples. Temperature sensors are further incorporated for added control and optimization of the cryostat. | 01-19-2012 |
| 20120060517 | METHOD FOR SUPPLYING REFINED LIQUEFIED GAS - A method for supplying a refined liquefied gas, in which prior to the supply of a liquefied gas stored in a container, the liquefied gas is refined by (1) determining the concentrations of impurities in the gas phase, then estimating the concentration of each impurity in the liquid phase from the ratio between the liquid-phase concentration and the gas-phase concentration of the impurity (gas-liquid equilibrium constant (K | 03-15-2012 |
| 20120090334 | Storage Tank For A Cryogenic Fluid With A Partitioned Cryogen Space - A cryogenic storage tank comprises a partition that divides a cryogen space into a main storage space and an auxiliary space. A valve disposed inside the cryogen space is associated with a first fluid passage through the partition. The valve comprises a valve member that is actuatable by fluid forces within the cryogen space. A second fluid passage through the partition comprises a restricted flow area that is dimensioned to have a cross-sectional flow area that is smaller than that of a fill conduit such that there is a detectable increase in back-pressure when the main storage space is filled with liquefied gas. | 04-19-2012 |
| 20120096873 | Cryogenic system with rapid thermal cycling - A fluid control assembly is connected between a cold gas container intended to be operated at deep cryogenic temperatures (e.g., 4K) and a gas reservoir for controlling the flow of fluid between the container and the reservoir. The fluid control assembly may be a passive valve assembly or an electrically controlled valve assembly which controls fluid flow between the reservoir and the container as a function of temperature and/or pressure differentials. The fluid control assembly enables the container to be rapidly cooled by restricting the amount of fluid flow from the reservoir into the container when the container is subjected to thermal cycling within a limited temperature range (e.g., 4K to 11K). The fluid control assembly together with the gas reservoir and the container form a thermal damper which is suited for use in a cryocooling system for producing the cryogenic temperatures (e.g., 4K) to operate superconducting devices which may need to be thermally cycled to remove trapped flux. | 04-26-2012 |
| 20120222430 | PLANT FOR REGASIFICATION OF LNG - A plant for regasification of LNG includes at least one pump boosting LNG pressure; an LNG/coolant heat exchanger producing NG from LNG being flowed from the boosting pumps; a closed coolant loop extending through the LNG/coolant heat exchanger and including at least one heat exchanger, a coolant from the respective heat exchanger being passed through the LNG heat exchanger as a gas and leaving in a condensed state as to produce NG by thermal exchange; and a heating medium being used within the respective heat exchanger as to provide coolant in a gaseous state. An NG/coolant heat exchanger is arranged in connection with the LNG/coolant heat exchanger and is connected to the closed coolant loop, whereby LNG is preheated within the LNG/coolant heat exchanger and NG is trim heated within the NG/coolant heat exchanger using liquid coolant from at least one heat exchanger. | 09-06-2012 |
| 20120234024 | HYBRID PUMPER - A process and apparatus that includes a cryogenic source for providing a cryogenic fluid for vaporization, a cryogenic pump in fluid flow communication with the cryogenic source for increasing the pressure of the cryogenic fluid, an unfired vaporizer coolant circuit | 09-20-2012 |
| 20120260674 | FLOATING MARINE STRUCTURE HAVING LNG CIRCULATING DEVICE - Disclosed is an apparatus for containing LNG. The apparatus includes an LNG tank containing liquid phase LNG and boil-off gas of LNG, and an circulating device. The circulating device includes an intake port and a discharge port. The circulating device further includes an flowing pathway from the intake port to the discharge port that does not include a forced LNG liquefying device. The intake port is located in an upper portion of the LNG tank, and the discharge port is located in a lower portion of the LNG tank substantially lower than the intake port. The circulating device is configured to suction, through the intake port, boil-off gas from the upper portion of the LNG tank and to discharge boil-off gas, through the discharge port, to the lower portion of the LNG tank. | 10-18-2012 |
| 20130008185 | CRYOGEN CYLINDER - A cryogen cylinder includes a tank having a side wall defining a chamber for containing a cryogenic substance in the tank; and a plate assembly mounted in the chamber, the plate assembly constructed and arranged to provide a passageway for vapor from the cryogenic substance to be introduced into the passageway. | 01-10-2013 |
| 20130008186 | CRYOGEN HEAT PLATE HEAT EXCHANGER - A heat exchanger includes a first housing disposed in a first atmosphere and having an upstream end, a downstream end and an internal space for a cryogenic substance; and a heat plate assembly mounted to the first housing and being exposed to the first atmosphere for providing heat transfer at an interface of the first atmosphere and the heat plate assembly. | 01-10-2013 |
| 20130091870 | Cold gas supply device and NMR installation comprising such a device - A device for supplying cold gases to an NMR installation or analytical apparatus equipped with a measuring probe, with cold gases ensuring the cooling of the sample contained in the probe, but also its lift and rotation, the device including an insulated tank containing liquid gas at boiling point and in which are arranged exchangers through which gas streams to be cooled pass, these exchangers being connected to transfer lines channeling the cooled gases to the probe. The device also includes at least one additional exchanger that ensures a pre-cooling of the gas stream before it is channeled to the corresponding exchanger, with the or each additional exchanger coming in the form of a double-flow exchanger that is supplied either by the gaseous vapor produced by the boiling of the liquid gas in the tank or by the cold gas that is evacuated or that escapes at the probe. | 04-18-2013 |
| 20130205804 | HANDLER AND PART INSPECTING APPARATUS - A handler includes a storage tank which stores liquid nitrogen, supply channels which supply refrigerant from the storage tank to inner passages of a first shuttle, a valve which opens and closes the supply channel, and a heat exchanger which has vaporization chambers with larger flow path cross-sectional areas than those of the supply channels to vaporize liquid nitrogen within the vaporization chambers. According to this structure, the respective vaporization chambers are filled with nitrogen gas produced by preceding vaporization. Thus, pressure fluctuations produced by successive vaporization of liquid nitrogen can be reduced. Moreover, nitrogen gas is supplied to the respective inner passages. Accordingly, excessive cooling for part housing pockets can be prevented. | 08-15-2013 |
| 20130232997 | ECONOMIZER BIASING VALVE FOR CRYOGENIC FLUIDS - Described herein are systems and methods for cryogenic fluid delivery. The systems may include a pressure vessel containing a cryogenic fluid formed of liquid and vapor that is connected to a use device via a withdrawal line. The withdrawal line connects to the cryogenic fluid in the pressure vessel via two routes, a liquid tube and a vapor line. The vapor line may include a back-pressure regulator that opens the vapor line depending on pressure in the system. The withdrawal line may include a pressure relief valve that exerts pressure on the liquid tube. A bypass line may connect the withdrawal line to the liquid tube. The bypass line has a check valve that permits free flow of cryogen from the withdrawal line to the liquid tube via the bypass line while prohibiting cryogen flow from the pressure vessel through the bypass line. The methods employ the systems described herein. | 09-12-2013 |
| 20130291567 | Regasification Plant - Methods and systems for regasifiing LNG are provided. A method for regasifying liquefied natural gas (LNG) includes providing heat to a LNG regasification process from a power plant. If the heat is not sufficient, additional heat can be provided to the LNG regasification process from a cooling tower operated in a warming tower configuration. | 11-07-2013 |
| 20130305745 | BULK CRYOGENIC LIQUID PRESSURIZED DISPENSING SYSTEM AND METHOD - A system for dispensing cryogenic liquid to a use point includes a bulk tank containing a supply of cryogenic liquid and a pressure builder that is in communication with the tank via a pressure building valve. The pressure builder uses heat exchangers to vaporize a portion of the cryogenic liquid as needed to pressurize the bulk tank. The pressurized cryogenic liquid is dispensed through a dispensing line running from the bottom of the tank. A vent valve also vents vapor from the tank to control pressure. Operation of the vent and pressure building valves is automated by a controller that receives data from sensors. The controller determines the required saturation pressure for the tank and varies the tank pressure to match and provide a generally constant outlet pressure depending on conditions of the cryogenic liquid. | 11-21-2013 |
| 20130312430 | GAS TANK REFUELING SYSTEM - A method of expansive-cooling an amount of a natural gas during transfer from a first storage container to a second storage container is provided. In addition, a system including two storage containers connected by an expander for the expansion of natural gas during the transfer from the first storage container to the second storage container is provided. | 11-28-2013 |
| 20130333396 | CRYOGENIC COOLING APPARATUS FOR TRANSPORT OF PERISHABLE GOODS - A portable cryogenic cooling apparatus includes a platform; a tank for storing a cryogen and mounted to the platform; a heat exchanger operatively associated with the platform and in fluid communication with the cryogen; at least one air circulation device operatively associated with the heat exchanger for moving atmosphere therethrough; a first exhaust pipe in communication with the heat exchanger for removing gaseous cryogen from the heat exchanger to a location external to the atmosphere; a power source mounted to the platform and connected to the at least one air circulation device for powering said device; a control valve operatively associated with the tank and the heat exchanger to adjust an amount of the cryogen provided to the heat exchanger; and a controller in communication with the heat exchanger and the control valve for generating a signal to the control valve for operation thereof. | 12-19-2013 |
| 20140033738 | METHODS AND SYSTEMS FOR A RAIL VEHICLE INCLUDING A SOURCE OF GASEOUS NATURAL GAS - Various methods and systems are provided for supplying gaseous natural gas to a rail vehicle. In one embodiment, a method of receiving fuel for use by a first vehicle comprises sending a request from the first vehicle to a remote liquid fuel container to convert a portion of the fuel in the liquid fuel container that is in a first, liquid phase from the first, liquid phase to a second, gaseous phase. | 02-06-2014 |
| 20140069118 | METHOD AND SYSTEM FOR SUPPLYING FUEL TO HIGH-PRESSURE NATURAL GAS INJECTION ENGINE - Provided is a fuel supply system for a marine structure using a high-pressure natural gas injection engine. The fuel supply system includes: a boil-off gas (BOG) compression unit configured to receive and compress BOG generated in a storage tank storing a liquefied gas; a reliquefaction apparatus configured to receive and liquefy the BOG compressed by the BOG compression unit; a buffer tank configured to receive the liquefied BOG from the reliquefaction apparatus and separate the reliquefied BOG into a gaseous component and a liquid component; a high-pressure pump configured to receive the liquid component from the buffer tank and compress the liquid component; and a high-pressure gasifier configured to gasify the liquid component compressed by the high-pressure pump and supply the gasified liquid component to the high-pressure natural gas injection engine. | 03-13-2014 |
| 20140130522 | Liquefied Gas Supply Conditioning System and Method - A conditioning system for a liquefied gas includes a source of liquefied gas, the liquefied gas provided from the source at a first temperature. A first heater is disposed to heat a flow of the liquefied gas to a second temperature. An accumulator is disposed to collect and store a quantity of the liquefied gas at the second temperature. A second heater is disposed to receive a flow of gas from the accumulator and the first heater, the second heater operating to heat the gas to a third temperature and provide the heated gas at the third temperature to a gas outlet. | 05-15-2014 |
| 20140137572 | Natural Gas Vehicle Vented Gas Capture System - A natural gas fuel system is provided. The system includes a vent gas recapture tank, a liquid natural gas (LNG) storage tank operably connected to the vent gas recapture tank, and a pressure control regulator operably connected to the vent gas recapture tank and the LNG storage tank. Vent gas is released from at least one point on the fuel system and stored in the vent gas recapture tank when certain conditions are met. | 05-22-2014 |
| 20140174104 | CRYOGENIC STORAGE TANK SYSTEM AND AUTO FLOW PATH SELECTOR VALVE THEREFOR - A cryogenic storage tank system and an automatic flow path selector valve for the same, in which maintenance is more convenient, the length of pipes is minimized, and the pressure of liquefied gas in a gaseous phase inside a cryogenic storage tank is automatically adjusted. | 06-26-2014 |
| 20140196474 | COLD HEAT RECOVERY APPARATUS USING AN LNG FUEL, AND LIQUEFIED GAS CARRIER INCLUDING SAME - Provided are a cold heat recovery apparatus using an LNG fuel and a liquefied gas carrier, in which costs involved in the installation and operation of a reliquefying facility can be reduced by recovering and utilizing cold heat of the LNG fuel when boil-off gas of liquefied gas as a cargo is reliquefied, and energy saving and reduction of environmental pollutants can be achieved because additional energy is not consumed in a reliquefaction process. A cold heat recovery apparatus for processing boil-off gas generated in a liquefied gas tank by using cold heat of an LNG fuel includes cold heat usage means using cold heat of an LNG supplied from an LNG fuel tank storing an LNG as a fuel to an engine, so as to processing the boil-off gas generated in the liquefied gas tank. | 07-17-2014 |
| 20140202176 | CONTROLLED ENVIRONMENT EXPANDER - Systems and methods are disclosed that expand environmental support for an HVAC system with an HVAC fluid circulating throughout by vaporizing a cryogen; and sparging the vaporized cryogen to dispense sparge bubbles to the HVAC fluid to cool the HVAC fluid. | 07-24-2014 |
| 20140216065 | METHOD FOR THE RECOVERY OF VENT GASES FROM STORAGE VESSELS - A method for removing gas from a storage vessel and returning it along with a liquid feed to the vessel. The gas such as natural gas is withdrawn from the storage vessel and fed to a venturi device where it is combined with a feed of liquid to the venturi device. The gas will combine with the liquid feed in the venturi device while the pressure in the storage vessel will be decreased thereby reducing the need for venting and increasing efficiency of the storage vessel. | 08-07-2014 |
| 20140352330 | LIQUEFIED GAS TREATMENT SYSTEM - A liquefied gas treatment system according to an embodiment of the present invention includes a boil-off gas heat exchanger exchanging heat between boil-off gas, pressurized by a boil-off gas compressor and recovered along a boil-off gas supply line branching off upstream of a liquefied gas-consuming unit, and the boil-off gas supplied from a liquefied gas storage tank, wherein the boil-off gas heat exchanger cools the boil-off gas, recovered along the boil-off gas supply line, with the boil-off gas, supplied from the liquefied gas storage tank, or flash gas, supplied through a vapor recovery line. | 12-04-2014 |
| 20140352331 | LIQUEFIED GAS TREATMENT SYSTEM - A liquefied gas treatment system according to an embodiment of the present invention includes a boil-off gas heat exchanger exchanging heat between boil-off gas, pressurized by a boil-off gas compressor and recovered along a boil-off gas supply line branching off upstream of a liquefied gas-consuming unit, and the boil-off gas, supplied from a liquefied gas storage tank, wherein the boil-off gas heat exchanger exchanges heat between the boil-off gas, pressurized by the boil-off gas compressor and recovered along the boil-off gas supply line, and flash gas, supplied through a vapor recovery line. | 12-04-2014 |
| 20140352332 | LIQUID METHANE STORAGE SYSTEM AND METHOD - Systems and methods for controlling the temperature and pressure of a cryogenic liquid methane storage unit are provided. The disclosed systems and methods generate methane gas from a reservoir of liquid methane stored within the methane storage unit, vent the methane gas through one or more outlet valves connected to the methane storage unit, and generate electric power using the vented methane gas. The generated electric power can then be used to initiating a cooling cycle, which reduces the temperature of said reservoir of liquid methane and reduces the pressure in said methane storage unit. Micro anaerobic digesters and methane storage units may be configured in a networked environment with a central controller that monitors remote units. | 12-04-2014 |
| 20150007584 | Operating Method for a Cryopressure Tank - An operating method is provided for a cryopressure tank in which cryogenic hydrogen for supplying a motor vehicle fuel cell can be stored under supercritical pressure at 13 bar or more. In order to compensate the pressure drop resulting from removal of hydrogen from the cryopressure tank, either a heat transfer medium is supplied to a heat exchanger provided in the cryopressure tank via a control valve over a period of time which significantly exceeds the cycle times of a conventional cycle valve or the heat transfer medium is not supplied to the heat exchanger. Depending on the fill level of the cryopressure tank, the control valve is actuated with respect o a desired temperature or a desired pressure of the hydrogen in the cryopressure tank. As long as there is a risk of liquefaction of the residual hydrogen in the cryopressure tank, as is the case when the temperature falls below the critical temperature of 33 K if the pressure drops below the critical pressure of approximately 13 bar, during the removal of cryogenic hydrogen from the cryopressure tank, the temperature is adjusted such that it does not drop below the critical temperature of 33 Kelvin. If the fill state in the cryopressure tank drops further, the pressure in the cryopressure tank is adjusted when there is no longer a risk of liquefaction such that the pressure does not drop below a minimum pressure value which the hydrogen that is removed from the cryopressure tank must have in order to be usable in the consumer without restricting the function thereof. | 01-08-2015 |
| 20150013350 | Cryogenic Fluid Cylinder - A cryogenic fluid cylinder includes an inner vessel for holding cryogenic fluid, a cylindrically shaped outer vessel having a vertical longitudinal axis surrounds the inner vessel and forms an insulating space there between, and operating controls located on a top of the outer vessel. Customer or end user operating controls include a liquid-use valve for selectively dispensing liquid cryogen, a pressure-building valve for selectively controlling a pressure building circuit, and a gas-use valve for selectively dispensing cryogen gas. Supplier or maintenance personnel operating controls include an economizer regulator for selectively setting at least one desired pressure of the inner vessel, a vent valve for selectively venting cryogen fluid, and a vacuum pressure port for indicating vacuum pressure between the vessels. The end user controls are located on a front side of the outer vessel while the supplier controls are located on a rear side of the outer vessel. | 01-15-2015 |
| 20150121903 | DEVICE FOR SUPPLYING GAS - Device for supplying evaporated gas from a storage tank for refrigerated liquefied gas with regulated pressure to a consumer, the requirements of which for pressure and mass flow of the gas vary widely, the device having: a motor operated high-pressure pump for the liquefied gas, the driving rotational speed of which determines the mass flow of the pumped liquefied gas; downstream of the high-pressure pump an evaporator for the liquefied gas; downstream of the evaporator a pressure-regulating valve for the evaporated gas, the outlet of which is connected to the consumer; a first regulator, the measured variable of which is the pressure of the evaporated gas downstream of the pressure regulating valve and the manipulated variable of which acts on the pressure-regulating valve; a second regulator, the measured variable of which is the pressure of the gas between the high-pressure pump and the pressure-regulating valve and the manipulated variable of which acts on a rotational speed controller for the high-pressure pump; and means for combining the manipulated variables of the two regulators in such a manner that the manipulated variable of the first regulator additionally acts on the rotational speed controller. | 05-07-2015 |
| 20150330575 | METHOD FOR MANAGING LNG BOIL-OFF AND LNG BOIL-OFF MANAGEMENT ASSEMBLY - A method for managing boil-off from an LNG tank located on board of an aircraft. The method, including removing the boil-off from the aircraft and disposing of the removed boil-off from the aircraft and an equipment assembly for use with an aircraft having an on-board LNG tank with a vent system having an outlet coupling, including a removal system configured to remove boil-off from the aircraft and a disposal system configured to dispose of the boil-off. | 11-19-2015 |
| 20150377418 | SYSTEM AND METHOD FOR STORING AND DISPENSING FUEL AND BALLAST FLUID - A system for storing and dispensing fuel and a ballast fluid is disclosed. The system may be employed in a vehicle or facility having a power plant. Fuel and ballast fluid may be stored cryogenically in a liquid phase and dispensed to the vapor phase. The system may employ a thermal and volumetric compensatory arrangement wherein fuel dispensed from storage for use in a power plant is used as a heat exchange medium (refrigerant) for ballast fluid received for storage; during refueling, ballast fluid stored in the vehicle or facility may be dispensed and used as a refrigerant for fuel being stored in the vehicle in space made available by the dispensed ballast fluid. The fuel may be natural gas with a main component of methane; the ballast fluid may be a fluid obtainable from ambient environmental air, such as nitrogen or oxygen. The fuel and ballast fluid may be conditioned so that the respective boiling points are approximately equal. The system may employ a heat transfer system with a microchannel heat exchanger. | 12-31-2015 |
| 20160203940 | Anti-Contamination Trap, and Vacuum Application Device | 07-14-2016 |
| 062480200 | And subsequently restored to receptacle as liquid | 20 |
| 20090100844 | Apparatus and method for controlling temperature in a boil-off gas - An apparatus and method for controlling temperature in a boil-off gas in a liquefaction plant prior to compression, wherein boil-off gas originating from an LNG storage tank is compressed and at least partially condensed, and wherein the condensed boil-off gas (LNG) is being returned to the storage tank. A heat exchanger ( | 04-23-2009 |
| 20090211262 | LNG TANK SHIP HAVING LNG CIRCULATING DEVICE - Disclosed is a liquefied natural gas storage apparatus. The apparatus includes a heat insulated tank and liquefied natural gas contained in the tank. The tank has heat insulation sufficient to maintain liquefied natural gas therein such that most of the liquefied natural gas stays in liquid. The contained liquefied natural gas has a vapor pressure from about 0.3 bar to about 2 bar. The apparatus further includes a safety valve configured to release a part of liquefied natural gas contained in the tank when a vapor pressure of liquefied natural gas within the tank becomes higher than a cut off pressure. The cut off pressure is from about 0.3 bar to about 2 bar. | 08-27-2009 |
| 20100212329 | BOIL-OFF GAS TREATMENT PROCESS AND SYSTEM - A flowline system for transferring cryogenic liquids between a cryogenic liquid storage tank and a cryogenic liquid receiving/loading facility, and a method of maintaining the system at or marginally above cryogenic temperature during periods between transfer of cryogenic liquids between the cryogenic liquid storage tank and the cryogenic liquid receiving/loading facility are provided. The flowline system has a main transfer conduit and a vapour return line in fluid communication with the cryogenic liquid storage tank and the cryogenic liquid receiving/loading facility. A cooling medium line is provided that is in fluid communication with the main transfer conduit, the vapour return line, and a source of cooled boil-off gas, wherein the cooled boil-off gas is at or marginally above cryogenic temperature. The cooled boil-off gas is circulated between said tank and said facility through the main transfer conduit and the vapour return line during periods between transfer of cryogenic liquids to maintain the main transfer conduit and the vapour return line at or marginally above cryogenic temperature. | 08-26-2010 |
| 20110173996 | METHODS FOR RECOVERING HELIUM - A method for providing cooling to the superconducting coils of a magnet with cryogenic helium gas at a helium production facility is disclosed. The cryogenic helium gas is fed to the magnet where the helium provides cooling. Cryogenic liquid helium provides additional cooling and fills the helium reservoir. Methods are also provided for recovering vaporized helium from the filling of a magnet and when the magnet is undergoing energization at the helium production facility. | 07-21-2011 |
| 20110179808 | NECK DEICER FOR LIQUID HELIUM RECONDENSOR OF MAGNETIC RESONANCE SYSTEM - A cryogenic system comprises: a liquid helium vessel containing liquid helium (LHe) in which are immersed superconducting magnet windings ( | 07-28-2011 |
| 20120011860 | METHOD AND SYSTEM FOR STORAGE AND TRANSPORT OF LIQUEFIED PETROLEUM GASES - A method for storage and transport of LPG on LPG carriers, in particular two cargoes of different LPG types on same shipment, having reliquefaction units ( | 01-19-2012 |
| 20120240600 | METHOD OF HANDLING A BOIL OFF GAS STREAM AND AN APPARATUS THEREFOR - A boil-off gas (BOG) stream ( | 09-27-2012 |
| 20120279235 | APPARATUS AND METHODS FOR DECOMPRESSING AND DISCHARGING NATURAL GAS UTILIZING A COMPRESSOR OR A TEMPERATURE-ACTUATED VALVE - One embodiment of the present invention is a portable natural gas discharge system for discharging compressed natural gas into a receiving location. The system comprises a portable chassis for holding the natural gas discharge system and all subcomponents, an inlet port for receiving the natural gas at an inlet pressure higher than a pressure of the receiving location, an expansion valve for regulating pressure of the natural gas to a stable intermediate pressure, a heat exchanger for heating up the cooled natural gas stream as a result of cooling due to expansion, a regulator for regulating a flow of the heated natural gas stream through the heat exchanger and out of the portable natural gas discharge system, and a discharge port for discharging the heated natural gas stream into the receiving location. | 11-08-2012 |
| 20130227967 | LNG VAPORIZATION EQUIPMENT - An LNG vaporization equipment is provided with: a nitrogen supply apparatus ( | 09-05-2013 |
| 20140026597 | FUEL STORAGE SYSTEM - A cryogenic fuel storage system for an aircraft is disclosed including a cryogenic fuel tank having a first wall forming a storage volume capable of storing a cryogenic liquid fuel; an inflow system capable of flowing the cryogenic liquid fuel into the storage volume; an outflow system adapted to deliver the cryogenic liquid fuel from the cryogenic fuel storage system; and a vent system capable of removing at least a portion of a gaseous fuel formed from the cryogenic liquid fuel in the storage volume. | 01-30-2014 |
| 20140041398 | BOIL-OFF GAS PROCESSING APPARATUS AND LIQUEFIED GAS TANK - A boil-off gas processing apparatus for reliquefying a boil-off gas ( | 02-13-2014 |
| 20140174105 | SYSTEMS AND METHODS FOR RE-CONDENSATION OF BOIL-OFF GAS - A system in one embodiment includes a heat exchanger, a detection unit, and a controller. The heat exchanger includes a first passage and a second passage configured for exchange of heat therebetween. The first passage is configured to receive a boil-off gas stream of a first cryogenic fluid. The second passage is configured to receive a liquid stream of a second cryogenic fluid. The detection unit is configured to detect a characteristic of the boil-off gas stream. The controller is configured to, responsive to information acquired from the detection unit corresponding to the characteristic, control the flow of the second cryogenic fluid to provide sufficient exchange of heat from the boil-off gas stream via the heat exchanger to condense at least a portion of the boil-off gas stream. A liquid stream of the first cryogenic fluid is output from the first passage and returned to a first tank. | 06-26-2014 |
| 20140290279 | LIQUEFIED GAS TREATMENT SYSTEM FOR VESSEL - A liquefied gas treatment system includes: a first stream of boil-off gas, which is generated from the liquefied natural gas in the cargo tank and is discharged from the cargo tank; a second stream of the boil-off gas, which is supplied as fuel to the engine in the first stream; and a third stream of the boil-off gas, which is not supplied to the engine in the first stream. The first stream is compressed in a compressor and is then branched into the second stream and the third stream. The third stream is liquefied by exchanging heat with the first stream in a heat exchanger, so that the boil-off gas is treated without employing a reliquefaction apparatus using a separate refrigerant. | 10-02-2014 |
| 20150007585 | Systems and Methods for Maintaining Pressure in Cryogenic Storage Tanks - A system for maintaining a substantially constant pressure within an ullage space of a cryogenic storage tank is provided. The system includes a compressor configured to receive fuel gas from the cryogenic storage tank, and compress the fuel gas to produce heated fuel gas. The system further includes a heat exchanger in flow communication with the compressor and configured to cool the heated fuel gas to produce cooled fuel gas, and a turbine in flow communication with the heat exchanger and configured to expand the cooled fuel gas to produce a gas and liquid mixture having a predetermined liquid to gas ratio, and discharge the gas and liquid mixture into the cryogenic storage tank. | 01-08-2015 |
| 20150068222 | METHOD FOR RE-LIQUEFYING BOIL-OFF GAS GENERATED AT LIQUID HYDROGEN STORAGE TANK - The boil-off gas discharged from a liquid hydrogen storage tank on a liquid hydrogen transport vessel ( | 03-12-2015 |
| 20150289500 | CRYOGENIC STORAGE DEVICE AND METHOD FOR OPERATING SAME - The invention relates to a cryogenic storage device ( | 10-15-2015 |
| 20150330574 | METHOD AND APPARATUS FOR RELIQUEFYING NATURAL GAS - Natural gas boiling off from LNG storage tanks located on board a sea-going vessel, is compressed in a plural stage compressor. At least part of the flow of compressed natural gas is sent to a liquefier operating on a Brayton cycle in order to be reliquefied. The temperature of the compressed natural gas from the final stage is reduced to below 0° by passage through a heat exchanger. The first compression stage is operated as a cold compressor and the resulting cold compressed natural gas is employed in the heat exchanger to effect the necessary cooling of the flow from the compression stage. Downstream of its passage through the heat exchanger the cold compressed natural gas flows through the remaining stages of the compressor. If desired, a part of the compressed natural gas may be supplied to the engines of the sea-going vessel as a fuel. | 11-19-2015 |
| 20150377550 | LOW-TEMPERATURE LIQUEFIED GAS TANK - A low-temperature liquefied gas tank is a low-temperature liquefied gas tank including a storage tank configured to store a low-temperature liquefied gas, and a re-liquefaction facility configured to liquefy boil off gas generated in the storage tank. A returning unit configured to return a re-liquefaction boil off gas liquefied in the re-liquefaction facility to the storage tank is provided. The returning unit has a distributor disposed under a liquid surface of the low-temperature liquefied gas stored in the storage tank and configured to eject the re-liquefaction boil off gas into the low-temperature liquefied gas. | 12-31-2015 |
| 20160003524 | SYSTEM AND METHOD FOR STORAGE AND DELIVERY OF CRYOGENIC LIQUID AIR - One aspect of the disclosure provides a system for storing a cryogenic mixture of liquid air and providing a source of breathable air. In an embodiment, the system comprises an insulated storage vessel, a cryocooler, and a vaporizing unit. The insulated storage vessel contains a cryogenic mixture of liquid air comprising liquid nitrogen (LN | 01-07-2016 |
| 20160123531 | BOIL-OFF GAS TEMPORARY STORAGE SYSTEM - Provided is a boil-off gas temporary storage system and, more particularly, is a boil-off gas temporary storage system which compresses boil-off gas at high pressure, temporarily stores the compressed boil-off gas in a boil-off gas absorbing tank, supplies the stored boil-off gas to a high-pressure gas transmission part and a high-pressure liquefied natural gas transmission part to recycle the boil-off gas, controls the pressure of a low-pressure liquefied natural gas cargo tank and a fuel liquefied natural gas tank of a ship to be filled with gas, and removes the necessity of a complicated and high-priced re-liquefaction device, in a method for removing the boil-off gas to depressurize the fuel liquefied natural gas tank of a ship to be filled with gas in the relatively high-pressure state before supplying the liquefied natural gas to a ship to be filled with gas. | 05-05-2016 |
| 062480300 | And subsequently used to cool receptacle | 1 |
| 20090107151 | COOLED CRYOSTAT RADIATION SHIELD - A cryostat has a cryogen vessel retained within an outer vacuum container, the cryogen vessel being provided with a vent path allowing cryogen gas to escape from the cryogen vessel, the cryostat further having a thermal radiation shield interposed between the cryogen vessel and the outer vacuum container. The vent path is arranged such that escaping cryogen gas is directed through a conduit, which forms an integral part of a thermal radiation shield. | 04-30-2009 |
