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11 results about "Regasification" patented technology

Regasification is a process of converting liquefied natural gas (LNG) at −162 °C (−260 °F) temperature back to natural gas at atmospheric temperature. LNG gasification plants can be located on land as well as on floating barges. Floating barge mounted plants have the advantage that they can be towed to new offshore locations for better usage in response to changes in the business environment. In a conventional regasification plantᴿᵁ, LNG is heated by sea water to convert it to natural gas / methane gas.

LNG regasification device and cogenerator of cold water and cold dry air

ActiveUS12687258B2ThermodynamicsWater vapor
A device for regasification of LNG, and cogeneration of fresh water and dry air, having a casing hermetically sealed from the exterior withstanding vacuum conditions, and containing a working fluid in its liquid and gaseous phases; the casing is traversed by t a cryogenic tube through which LNG is fed and regasified natural gas is collected via the other end. The external surface of the cryogenic tube condenses the gaseous working fluid, releasing energy, and evaporative condenser tubes located outside the casing, with the external condensing surface in contact with damp air, and the air vapor contained in the damp air condenses thereupon, generating cold fresh water and releasing energy to the working fluid in its liquid phase which flows through the evaporative condenser and which evaporates, generating a gaseous phase working fluid, which exits through the evaporative condenser and is directed into the casing for the condensation
Owner:WGA WATER GLOBAL ACCESS SL +2

Arctic cascade modified process for natural gas liquefaction and plant for its implementation.

PendingJP2026508723ASolidificationLiquefactionEvaporationFluvial
The present invention relates to a technology for liquefying natural gas, which is subsequently transported by rivers and oceans and ultimately regasified. Pretreated natural gas is compressed by a compressor 1, the heat of compression is removed in an air or water cooler 2, and multi-stage pre-cooling is subsequently performed by evaporating a heavy refrigerant in an evaporator 3. The light refrigerant vapor and its pre-evaporation cold are recovered in a shell-and-tube heat exchanger 7, where the pressure of the gas to be liquefied is reduced by a pressure reducer 10, unliquefied gas is separated, and liquefied natural gas is discharged. The heavy refrigerant obtained by evaporation is compressed by a compressor 4, condensed in an air or water cooler 5, and reused in the multi-stage pre-cooling of natural gas. A light refrigerant is compressed by at least two compressors 11, the heat of compression is removed in an air or water cooler 12, and then passes through continuous cooling by a low-pressure light refrigerant in a double-flow superheater 12 and an evaporating heavy refrigerant in an evaporator 3. The high-pressure light refrigerant is then split into two streams. The first stream is expanded through an isentropic process in an expander 14. The second stream passes through continuous cooling in a shell-and-tube heat exchanger 7, then expanded through an isenthalpic process in a throttle valve 15, and evaporated by subcooling natural gas in an evaporator 8. The streams are then mixed at equal pressure and used as a single stream of low-pressure light refrigerant to cool the second stream of light refrigerant before expansion and evaporation in the isenthalpic process with natural gas in the shell-and-tube heat exchanger 7, and to cool a single stream of high-pressure light refrigerant in a double-flow superheater 13. The present invention provides stronger cooling of the natural gas, reduces the amount of boil-off gas and the work required for its recompression and recycling, and provides a simpler hardware design for the heat exchanger.
Owner:PUBLICHNOE AKTSIONERNOE OBSHCHESTVO NOVATEK

Floating regasification system for liquefied natural gas (LNG)

A floating regasification system for liquefied natural gas (LNG) comprises a floating structure having an upper installation surface, at least one regasification module attached to the upper installation surface, a first fluid transfer assembly in fluid communication with an input side of the at least one regasification module, and a second fluid transfer assembly in fluid communication with an output side of the at least one regasification module, wherein the at least one regasification module is configured to receive LNG through the first fluid transfer assembly, to vaporize the LNG to generate a gas, and to deliver the gas into the second fluid transfer assembly, and wherein each of the fluid transfer assemblies has at least one flexible hose for transferring LNG to the at least one regasification module or gas to an onshore consumer, respectively.
Owner:ECONNECT ENERGY AS

Liquefied natural gas vehicle assisted data center cooling apparatus

The invention comprises a coupled data center cooling / liquid natural gas (LNG) regasification heating apparatus, such as an apparatus configured to cool a data center, comprising: a heat transfer fluid pipe configured to hold a heat transfer fluid, the heat transfer fluid configured to transfer a heat from the data center to a liquefied natural gas; and a phase change container, such as positioned on a fuel transport vehicle, configured to hold a portion of the liquefied natural gas during a phase change of the liquefied natural gas to a gas phase natural gas, the phase change container further comprising a heat exchanger configured to transfer from the heat transfer fluid at least thirty percent of an enthalpy of vaporization energy used in a phase change of the liquefied natural gas into a gas phase natural gas.
Owner:COHEN BRIAN +4

Liquefied natural gas assisted data center cooling apparatus

The invention comprises a coupled data center cooling / liquid natural gas (LNG) regasification heating apparatus, such as an apparatus configured to remove heat generated in a data center by a processing unit, comprising: a heat exchanger, the heat exchanger comprising: an input connector connected to a supply of a liquefied natural gas (LNG); a phase change chamber, wherein a gas phase natural gas (NG) forms from the liquefied natural gas in a phase change; and an output connector connected to an output pipe configured to move the gas phase natural gas out of the phase change chamber, the heat exchanger configured to move at least thirty percent of an energy required in the phase change from the data center to the liquefied natural gas.
Owner:COHEN BRIAN +4

A method for hoisting a booster pump on an LNG regasification ship

The application discloses a kind of LNG re-gasification ship booster pump's real ship hoisting method, hoist FSRU re-gasification ship booster pump using crane, method includes the following steps: adjusting ballast water, inspection balance;Confirm hoisting trajectory to coincide with the top and bottom of pump well line;Adjust the center of gravity of gourd sling and the center of object coincide;Slowly hoist booster pump with 1# crane to make it enter pump well;Tighten the bolt and nut of top plate and seat table connection.The application has achieved the following beneficial effects through practical application: (1) the tooling tool is less, and the booster pump is hoisted easily;(2) strong, can hoist the equipment with precision surface for the first contact surface during hoisting;(3) lower than traditional hoisting cost.
Owner:HUDONG ZHONGHUA SHIPBUILDINGGROUP

Floating electrical energy generation plant

A floating electrical energy generation plant is disclosed. The floating electrical energy generation plant can include a floatable vessel. The floating electrical energy generation plant may include onboard storage for liquefied natural gas, and a regasification unit for regasifying the liquefied natural gas to facilitate combustion in at least one gas turbine generator of an onboard power generator. The floating electrical energy generation plant can further include an onboard carbon capture system to capture carbon dioxide present in exhaust gases from the onboard power generator, liquefy, and store the liquefied natural gas in one or more onboard storage tanks. Steam from operation of the onboard power generator can be used as heat source for a regeneration column of the carbon capture system, and the coldness of the liquefied natural gas may be utilized to help liquefy the captured carbon dioxide.
Owner:TECHNIP ENERGIES FRANCE SAS

FSRU re-gasification hybrid heat source scheduling method based on load prediction and rule learning

This invention relates to the field of intelligent scheduling technology for FSRU heat sources, specifically disclosing a method for scheduling FSRU regasification hybrid heat sources based on load forecasting and rule learning. The method includes: collecting basic operational data of the FSRU, marine environmental data, and coupled correlation data, and performing data cleaning and standardization preprocessing; inputting the preprocessed data into a three-dimensional coupled load forecasting model; dynamically switching the network structure complexity of the model based on real-time collected marine environmental parameters; and outputting the load forecast value and deviation probability. This invention, by constructing a three-dimensional coupled environment-load-equipment model and introducing a dynamic switching mechanism, can intelligently select simplified or complex network structures according to real-time sea conditions, significantly improving the prediction accuracy for nonlinear environmental impacts while ensuring computational efficiency.
Owner:SHANGHAI COSCO SHIPPING HEAVY IND CO LTD +1

Coupled data center cooling and LNG regasification apparatus and method of use thereof

The invention comprises a coupled data center cooling / liquid natural gas (LNG) regasification heating and cooling apparatus and method of use thereof. For example, a method is described for cooling a data center, comprising the steps of: (1) transferring heat from the data center to a liquid phase combustible refrigerant and (2) phase changing the liquid phase combustible refrigerant, carried by the trailer, to a gas phase combustible refrigerant, at least fifty percent of an enthalpy of vaporization energy used in the step of phase changing transferred to the gas phase combustible refrigerant in the step of transferring, the gas phase combustible refrigerant comprising an energy density of greater than 10,000 kJ / kg. Optionally, the step of phase changing boils a liquefied natural gas (LNG), carried by the trailer, to a gas phase natural gas (NG).
Owner:COHEN BRIAN +4

Liquid natural gas (LNG) regasification systems and combined cycle power plants including same

PCT designated stageWO2026005771A1SolidificationLiquefactionPower stationCombustor
A regasification system includes a first cooling apparatus in flow communication with a liquid natural gas conduit for receiving liquid natural gas (LNG), and a second cooling apparatus in flow communication and downstream from the first cooling apparatus. The second cooling apparatus is in flow communication with a cooling assembly including cooling water. The cooling assembly facilitates cooling a carbon dioxide stream flowing through a compression train of a carbon capture system included in a combined cycle power plant. The regasification system also includes a heat exchanger in flow communication and downstream from the second cooling apparatus. The heat exchanger is in flow communication with a combustor of a gas turbine assembly for the combined cycle power plant.
Owner:GE VERNOVA INFRASTRUCTURE TECHNOLOGY LLC +1