L'air Liquide, Soci&#xe9;t&#xe9; Anonyme Pour L'etude Et L'exploitation Des Proc&#xe9;d&#xe9;s Georges Claude

Pierre Barjhoux

Fabien Durand

Jean-Marc Bernhardt

Laurent Allidieres

Franck Delcayre

Vincent Heloin

Gilles Flavien

Golo Zick

Thomas Fayer

David Grillot

Cindy Deschildre

Martin Staempflin

Camille Bouvier

Gregoire Rigout

Pierre-Germain Marlier

Grégoire Rigout

Pierre Crespi

Disclosed is a facility for the refrigeration and/or liquefaction of a fluid, comprising a circuit of fluid to be cooled comprising an upstream end intended to be connected to a source of fluid to be cooled and a downstream end intended to be connected to a member for collecting the cooled and/or liquefied fluid; the facility comprising an assembly of heat exchanger(s) in thermal exchange with the circuit of fluid to be cooled; the facility comprising a cooling device in thermal exchange with the assembly of heat exchange(s); the cooling device comprising a refrigerator with a refrigeration cycle for a cycle gas in a working circuit; the working circuit of the refrigerator comprising, a mechanism for compressing the cycle gas, a system for cooling the cycle gas, a mechanism for expanding the cycle gas and a system for heating the cycle gas; the mechanism for expanding the cycle gas comprising several turbines secured to shafts mounted so as to be able to rotate on aerostatic bearings; the facility comprising mechanisms for braking the turbines, the braking mechanisms each comprising a braking compressor secured to a shaft of a turbine and a braking gas circuit incorporating the braking compressor; the braking gas circuits comprising a system for cooling the braking gas downstream of the braking compressor and a mechanism for expanding the braking gas; the facility being equipped with a compressed lifting gas circuit comprising an end connected to a compressed lifting gas source and a downstream end connected to the bearings, and wherein the compressed lifting gas source comprises at least one of the braking circuits.

Facility and method for refrigeration and/or liquefaction of a fluid

Method for delivering liquefied gas, especially hydrogen, by means of at least one mobile storage facility, especially a storage facility transported by lorry, comprising a step of filling the mobile storage facility with liquefied gas at a source plant, the mobile storage facility containing, after filling, liquefied gas and a fraction of the vaporized gas, the method comprising a movement of the mobile storage facility from the source plant to a receiving station and a transfer of liquefied gas from the mobile storage facility to the receiving station, characterized in that it comprises a step of interim cooling of the liquefied gas contained in the mobile storage facility between the source plant and the receiving station by means of a cooling device comprising a liquefied gas tank and a refrigerating element.

Method for delivering liquefied gas

Plant and method for liquefying a flow of gas, having a cooling circuit that includes at least one exchanger () for cooling the gas, and at least one expansion turbine () which is mounted on a rotary axle which is supported by at least one bearing () of the gas-static type, the cooling circuit () also including a pressurized gas injection conduit that is configured to supply pressurized gas to the bearing () in order to provide support to the rotary axle, the plant () further includes a recovery conduit () that is configured to recycle at least a portion of the gas which has been used to support the rotary axle of the bearing () with a view to liquefying the gas.

Plant and method for liquefying gas

Process and plant for the production of liquid hydrogen with a liquefier that has a variable cooling power dependent on the electrical power consumed. The liquefier is supplied with electricity by a first source of electricity at least one additional source of electricity that provides an intermittent or variable amount of electricity over time. Liquid hydrogen is produced at first thermodynamic conditions when the liquefier is supplied with a predetermined nominal electrical energy level and produced at subcooled conditions, with respect to the first thermodynamic conditions, when electricity supplied to the liquefier exceeds the nominal level.

Process and plant for the production of liquid hydrogen

Device and method for purifying a gas mixture to produce a concentrated gas, notably neon, starting from a mixture comprising neon, said device including, in a cold box housing a cryogenic purification circuit comprising, in series, at least one unit for purifying the mixture by cryogenic adsorption at a temperature between 65K and 100K and notably 65K, then a unit for cooling the mixture to a temperature between 25 and 65 K and then a unit for cryogenic distillation of the mixture to produce the concentrated liquid at the outlet of the cryogenic distillation unit, characterized in that the unit for cooling the mixture to a temperature between 25 and 65 K comprises at least one cryocooler that extracts thermal power from the mixture via a heat exchanger.

Device and method for purifying a gas mixture

The invention relates to a method for adjusting a cryogenic refrigeration apparatus including a plurality of liquefiers/refrigerators arranged in parallel in order to cool a single device. The method includes a step of calculating in real time the dynamic mean value of at least one operating parameter for all the liquefiers/refrigerators. The apparatus controlling in real time the at least one valve for controlling the stream of working gas of at least one liquefier/refrigerator in accordance with the difference between the instantaneous values of the parameter relative to said dynamic converge toward said dynamic mean value.

Method for adjusting a Cryogenic refrigeration apparatus and corresponding apparatus

Refrigeration device comprising a working circuit in a loop for the working gas and comprising, in series: a compression station, a cold box, a system for the exchange of heat between the cooled working gas and a point of use, a system for the additional pre-cooling of the working gas leaving the compression station comprising an auxiliary cryogenic fluid volume, the cold box comprising a first cooling stage for the working gas comprising a first and a second heat exchanger, these being connected both in series and in parallel to the working circuit at the outlet of the compression station, the first cooling stage also comprising a third heat exchanger selectively exchanging heat with the auxiliary fluid, characterized in that the third heat exchanger is connected both in series and in parallel to the first and to the second heat exchangers, the working circuit comprising a recuperation pipe fitted with at least one valve and which connects the outlet of the third heat exchanger to the second heat exchanger.

Refrigeration and/or liquefaction device using selective pre-cooling, and corresponding method

A device for refrigerating and/or liquefying a working gas comprising helium, the device comprising a looped working circuit for the working gas includes, in series, a compression station, a cold box, a heat exchange system exchanging heat between the cooled working gas and a user, the device further comprising an additional pre-cooling system comprising at least one tank of auxiliary cryogenic fluid, such as liquid nitrogen, the cold box comprising a first cooling stage of the working gas comprising a first exchanger disposed at the output of the compression station as well as a second heat exchanger and a third heat exchanger, the first heat exchanger being of the aluminum plate-fin type, the second heat exchanger being of the tube or welded plate type, characterized in that the second and third heat exchangers are connected both serially and in parallel on the working circuit downstream of the first heat exchanger.

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La Tronche, France

Pierre Barjhoux