COOLING AND / OR LIQUIDATION PROCESS, DEVICE AND SYSTEM

Description

[0001] The invention relates to a method, device, and installation for refrigeration and / or liquefaction. More particularly, the invention relates to a method for refrigerating and / or liquefying a user fluid stream, in particular natural gas. The method uses a cooling and / or liquefaction installation comprising a low-temperature refrigeration device, i.e., at a temperature between -100 degrees Celsius and -273 degrees Celsius, and in particular between -100 degrees Celsius and -253 degrees Celsius. The refrigeration device comprises a working circuit forming a loop and containing a working fluid. The working circuit forms a cycle comprising, in series: a working fluid compression mechanism, a working fluid cooling mechanism, a working fluid expansion mechanism, and a working fluid heating mechanism.The refrigeration device comprising a cooling exchanger intended to extract heat from the user fluid stream by heat exchange with the working fluid circulating in the working circuit; the installation comprising a circulation line for said user fluid stream in the cooling exchanger; the process comprising a cooling step in which the refrigeration device is in a first operating mode of cooling the cooling exchanger while a user fluid stream is circulated in this cooling exchanger; the process comprising, after this cooling step, a step of cleaning solidified impurities in the cooling exchanger.

[0002] The invention relates in particular to cryogenic refrigerators or liquefiers, for example of the "Turbo Brayton" cycle type or "Turbo Brayton coolers" in which a cycle gas (helium, nitrogen, hydrogen or other pure gas or mixture) undergoes a thermodynamic cycle producing cold which can be transferred to an organ or gas to be cooled.

[0003] These devices are used in a wide variety of applications, including cooling natural gas from a tank (for example, on ships). Liquefied natural gas is, for instance, subcooled to prevent vaporization, or the gaseous portion is cooled to facilitate liquefaction.

[0004] For example, a natural gas stream can be circulated in a heat exchanger cooled by the cycle gas of the refrigerator / liquefier.

[0005] The gas cooled in this heat exchanger may contain impurities (such as carbon dioxide) that can solidify at the low temperatures reached within the exchanger. This can clog the heat exchanger and reduce the system's efficiency.

[0006] One solution could be to actively heat the heat exchanger with an electric heater. However, this is energy-intensive and often unsuitable for explosive atmospheres.

[0007] A method and device conforming to the preamble of independent claims 1 and 8 are described in US 2012 / 180520 A1.

[0008] One aim of the present invention is to overcome all or part of the disadvantages of the prior art noted above.

[0009] To this end, the method according to the invention, which also conforms to the generic definition given in the preamble above, comprises the characteristics defined in independent claim 1.

[0010] Furthermore, embodiments of the invention may include one or more of the features as defined in dependent claims 2 to 7.

[0011] The invention also relates to a low temperature refrigeration device, i.e. at a temperature between minus 100 degrees Celsius and minus 273 degrees Celsius, according to independent claim 8.

[0012] The preferred embodiments of the invention are described in dependent claims 9 to 10.

[0013] The invention also relates to a refrigeration and / or liquefaction installation for a user fluid stream, in particular natural gas, according to claim 11, comprising a refrigeration device according to any one of claims 8 to 10, the installation comprising at least one user fluid reservoir, a circulation line for said user fluid stream in the cooling exchanger.

[0014] Other features and advantages will become apparent upon reading the description below, made with reference to the figures in which: [ Fig. 1 ] represents a schematic and partial view illustrating the structure and operation of an example of a device and installation that can implement the invention.

[0015] The cooling and / or liquefaction installation of the [ Fig. 1The system includes a refrigeration device 1 that provides cooling (cooling power) to a cooling exchanger 8. The system also includes a circulation pipe 25 for a flow of fluid to be cooled, which is subjected to heat exchange with this cooling exchanger 8. For example, the fluid is liquefied natural gas pumped into a tank 16 (for example, via a pump), then cooled (preferably outside the tank 16) and returned to the tank 16 (for example, as a spray into the gaseous phase of the tank 16). This allows the contents of the tank 16 to be cooled or subcooled and limits vaporization. For example, the liquid in the tank 16 is subcooled below its saturation temperature (a drop in temperature of several degrees K, in particular 5 to 20 K and especially 14 K) before being reinjected into the tank 16.Alternatively, this cooling can be applied to the vaporization gas in the tank, particularly for the purpose of its reliquefaction. That is to say, the refrigeration device 1 produces a cooling capacity at the level of the cooling exchanger 8.

[0016] The refrigeration device 1 includes a working circuit 10 (preferably closed) forming a circulation loop. This working circuit 10 contains a working fluid (helium, nitrogen, neon, hydrogen or other suitable gas or mixture (for example helium and argon or helium and nitrogen or helium and neon or helium and nitrogen and neon).

[0017] The working circuit 10 forms a cycle comprising in series: a working fluid compression mechanism 2, 3, a working fluid cooling mechanism 6, a working fluid expansion mechanism 7, and a working fluid heating mechanism 6, 8.

[0018] Device 1 includes a cooling heat exchanger 8 intended to extract heat from at least one component 25 by heat exchange with the working fluid circulating in the working circuit 10.

[0019] The working fluid cooling and heating mechanisms classically include a common heat exchanger 6 in which the working fluid flows counter-currently in two separate transit portions of the working circuit 10 depending on whether it is being cooled or heated.

[0020] The cooling heat exchanger 8 is located, for example, between the expansion mechanism 7 and the common heat exchanger 6. As illustrated, the cooling heat exchanger 8 can be a separate heat exchanger from the common heat exchanger 6. However, alternatively, this cooling heat exchanger 8 could be formed from a portion of the common heat exchanger 6 (i.e., the two exchangers 6 and 8 can be monobloc, meaning they can have separate fluid circuits that share the same heat exchange structure).

[0021] Thus, the working fluid which exits relatively hot from the compression mechanism 2, 3 is cooled in the common heat exchanger 6 before entering the expansion mechanism 7. The working fluid which exits relatively cold from the expansion mechanism 7 and the cooling heat exchanger 8 is, in turn, heated in the common heat exchanger 6 before returning to the compression mechanism 2 3 in order to start a new cycle.

[0022] Typically, in normal operating mode, hereafter referred to as "first operating mode," the working gas undergoes a compression, cooling, expansion, and heating cycle, producing cold at the cooling exchanger 8. Generally, an equal or nearly equal mass flow rate circulates through the two transit sections in the common heat exchanger 6.

[0023] As illustrated, in normal operating mode, a fluid flow (e.g., liquefied natural gas) can be cooled in the cooling exchanger 8. If this fluid contains impurities (carbon dioxide or other) that may solidify during cooling, a blockage 17 or obstruction may occur in the cooling exchanger 8.

[0024] This blockage can be removed by a cleaning step carried out by the refrigeration device 1 itself by adopting a second mode of operation in which the working gas still circulates in the working circuit 10 as described above, but in which the cooling of the cooling exchanger 8 is reduced compared to the first mode of operation.

[0025] For example, the refrigeration device 1 provides occasional zero cooling or provides heating of the cooling exchanger 8.

[0026] During this cleaning process, a flow of user fluid can be circulated through the cooling exchanger 8 to carry away the impurities heated by the exchanger. The user fluid flow can be further heated during this second operating mode.

[0027] The compression mechanism 2, 3 comprises, according to the invention, several compressors and at least two drive motors 14, 15 for rotating the compressor(s) 2, 3. Furthermore, preferably, the cooling capacity of the device is variable and can be controlled by regulating the rotational speed of at least one of the drive motors 14, 15 (cycle speed). Preferably, the cooling capacity produced by the device 1 can be adjusted from 0 to 100% of a nominal or maximum capacity by changing the rotational speed of the motor(s) 14, 15 between zero and a maximum or nominal speed. Such an architecture makes it possible to maintain high efficiency over a wide operating range (for example, 97% of nominal efficiency at 50% of the nominal cooling capacity).

[0028] For example, in the second operating mode, the rotational speed of at least one of the drive motors 14, 15 is reduced to a value between 1% and 60%, and preferably between 10% and 50%, in particular between 20% and 30%, of the rotational speed of said motor 14, 15 during the first cooling operating mode. For example, this reduced rotational speed corresponds to between 1% and 60%, and preferably between 10% and 50%, in particular between 20% and 30%, of the nominal or maximum rotational speed of said motor 14, 15.

[0029] In this configuration, the cooling power produced at the cooling exchanger 8 is reduced or eliminated (or even reduced to heat). This causes the heating exchanger 8 to heat up, leading to the melting and subsequent vaporization of the solidified impurities. This heating, possibly combined with the flow of user fluid through the cooling heat exchanger 8, will carry these impurities out of the exchanger 8, for example, towards the user fluid reservoir 16.

[0030] In the non-limiting example shown, the refrigeration device 1 comprises two compressors 2, 3 in series driven respectively by two separate motors 14, 15 and a turbine 7 coupled to the drive shaft of one 15 of the two motors.

[0031] That is to say, a first engine 14 drives only a compressor 3 (motor-compressor) while the other engine 15 drives a compressor 2 and is coupled to a turbine 7 (motor-turbocompressor).

[0032] For example, in a second operating mode of the refrigeration device (1), not in accordance with the invention, the motor 15, to whose drive shaft a turbine 7 is coupled, is stopped, and the other motor 14, which drives only a compressor 3, operates at a rotational speed between 1% and 60%, and preferably between 10% and 50%, particularly between 20% and 30%, of the maximum rotational speed or the rated speed of the motor. The rated speed or maximum speed of a motor refers to the maximum speed that the motor can produce at maximum refrigeration capacity. This maximum or rated speed is the maximum recommended speed for the operation of the refrigeration device 1 and may, where applicable, be lower than the maximum speed that the motor can intrinsically reach.

[0033] In this configuration, the turbine 7 and the compressor 2 coupled to the drive shaft of the stopped engine 15 can be in freewheeling mode.

[0034] As before, the reduced speed of the other motor 14 will circulate the working fluid in the working circuit 10 with low efficiency. The turbine 7 and the compressor 2, in free-running mode, will further increase pressure losses in the working gas circuit 10. This will increase the relative heating at the cooling exchanger 8 used to remove impurities, without increasing the already low electrical consumption of device 1.

[0035] To further increase heating and the speed of impurity removal, an additional pressure drop can be introduced in this operating mode. For example, the motor 15, when stopped, is braked. The rotation of its shaft and / or the corresponding compressor 2 and / or turbine 7 can be braked or blocked. This braking or blocking can be mechanical via a sliding stop and / or electrical and / or magnetic. For example, the motor(s) are electric motors, particularly synchronous motors. Motor braking can be achieved by including a braking resistor in its control circuit for this operating mode. Similarly, such an electric motor can have a three-phase electrical system (three-phase) where the phases can be momentarily short-circuited to provide this braking.The motor 15 can notably be reversible and braking can be achieved by switching from its reverse generator mode in which instead of producing torque it will produce a current and brake its drive shaft.

[0036] These braking modes can be implemented on the control circuits (drives) of such electric motors. Therefore, simple software control allows these braking modes to be enabled without modifying the existing motor structure.

[0037] In yet another embodiment according to the invention, in the second mode of operation, at least one motor 15, for example a motor comprising a turbine 7 fixed in rotation to its shaft, is set in rotation in the opposite direction.

[0038] That is to say that in the first mode of operation of the refrigeration device 1, the rotating shafts of the drive motors 14, 15 rotate in their respective first directions of rotation and the working fluid circulates in the working circuit 10 in a first direction of circulation and in the second mode of operation of the refrigeration device 1, at least one motor 15 preferably to whose shaft a turbine 7 is coupled is set in reverse rotation, that is to say that its rotating shaft rotates in the opposite direction of rotation to the first direction of rotation.

[0039] The working fluid will continue to flow in the first direction in the working circuit 10, but the reverse rotation of the turbine 7 (which is not optimized for this direction) will, instead of extracting mechanical work from the working gas (expansion), supply it with work and thus heat it. This works particularly well with centripetal turbine technology. Preferably, the compressor(s) should also be centrifugal.

[0040] While this motor 15 is rotating in the opposite direction (backwards), the other motor 14 (or the other motors if there are several) can be stopped, notably by freewheeling; however, preferably the other motor 14 (or the other motors) are operated at a reduced rotational speed. For example, this other motor 14 (or at least one of the other motors) is rotated at a speed between 1% and 60%, and preferably between 10% and 50%, in particular between 20% and 30% of the maximum or nominal rotational speed of said motor 14.

[0041] This reduced speed of the motor(s) increases the efficiency of the heating and allows a faster and more efficient restart of the refrigeration device in the first cooling operating mode.

[0042] Preferably, the motor(s) 14 rotated in the opposite direction is rotated at a reduced speed, for example at a speed between 1% and 60% and preferably between 10% and 50%, in particular between 20% and 30% of the maximum or nominal rotation speed of said motor.

[0043] In one possible variant, however, the reverse rotational speed could be higher and could reach the motor's rated or maximum speed.

[0044] According to the invention as defined in independent claim 8, the device comprises at least one electronic controller 12 connected to all or part of the components of the installation (motors, valves, pump, etc.). The electronic controller 12 may include a microprocessor or a computer and may be configured to dynamically control all or part of the components of the installation and is configured to provide the operating modes described above (automatically and / or in response to a command, in particular from a user).

[0045] For example, switching to the second operating mode of the refrigeration device 1 to ensure cleaning of the cooling exchanger 8 can be controlled by a user and / or in response to the detection of a plug of impurity in the cooling exchanger 8 (pressure sensor or other in the circuit).

[0046] Furthermore, the electronic controller 12 can be configured (programmed or controlled) to dynamically control the heating of the cooling exchanger 8 in the second operating mode. For example, this control (the relative heating power compared to the first operating mode) can be linked to the temperature rise rate of the common heat exchanger 6 according to a predetermined profile and / or to limit the temperature rise rate of the common heat exchanger 6 below a predetermined threshold. This can prevent excessively rapid heating of the common heat exchanger 6 and / or the cooling exchanger 8, which is advantageous, for example, in the case of an aluminum plate heat exchanger.

[0047] In the example shown, the refrigeration device 1 comprises two compressors 2, 3 forming two compression stages and an expansion turbine 7. That is to say, the compression mechanism comprises two compressors 2, 3 in series, preferably of the centrifugal type, and the expansion mechanism comprises a single turbine 7, preferably centripetal. Of course, any other number and arrangement of compressor(s) and turbine(s) can be considered, for example, three compressors in series and one turbine, or three compressors and two turbines, or three turbines, or two compressors and two turbines...

[0048] In the illustrated example, a cooling exchanger 4, 5 is provided at the outlet of each compressor 2, 3 (for example, cooling by heat exchange with water at ambient temperature or any other fluid or cooling agent).

[0049] This allows for isentropic, isothermal, or nearly isothermal compression. Of course, any other arrangement can be considered (for example, no cooling exchanger 4, 5 at one or more of the compression stages). Similarly, a heating exchanger may or may not be included at the outlet of all or part of the expansion turbines 7 to achieve isentropic or isothermal expansion. Preferably, the heating and cooling of the working fluid are also isobaric, although this is not a limitation.

[0050] For example, device 1 includes two high-speed motors 14, 15 (for example 10,000 revolutions per minute or several tens of thousands of revolutions per minute) for driving the respective compression stages 2, 3. Turbine 7 can be coupled to motor 2 of one of the compression stages 2, 3, i.e. the device can have a turbine 8 constituting the expansion mechanism which is coupled to motor 2 for driving a compression stage 2 (the first in particular).

[0051] Thus, the power of turbine(s) 7 can be advantageously recovered and used to reduce the fuel consumption of the motor(s). By increasing the motor speed (and therefore the flow rate in the working gas cycle), the refrigeration power produced is increased, and consequently, so is the electrical consumption of the liquefier (and vice versa). Compressors 2, 3 and turbine(s) 7 are preferably directly coupled to an output shaft of the relevant motor (without a gear-driven transmission mechanism).

[0052] The output shafts of the motors are preferably mounted on magnetic or gas-charged dynamic bearings. These bearings are used to support the compressors and turbines.

[0053] Furthermore, all or part of the device, in particular its cold components, can be housed in a thermally insulated sealed casing (in particular a vacuum chamber containing the common counter-current heat exchanger).

[0054] To further improve the efficiency and speed of the process, simultaneously and / or after the cleaning step, a purge 18 of the cooling exchanger 8 can be provided with a flow of purge fluid injected into the cooling exchanger 8 to sweep and remove from the cooling exchanger 8 the impurities detached during the cleaning step.

[0055] For example, a neutral gas circuit (18) or another gas (such as nitrogen) can be provided to purge the heated impurities. This purging can, if necessary, replace the circulation of the user fluid flow during heating. The resulting mixture can be discharged to a discharge area (for example, to the atmosphere).

[0056] Alternatively, this purge 18 can be carried out with a flow of user fluid. For example, a portion of user fluid is drawn from the circulation line 12 (via a bypass equipped with a valve, for example). The purge user fluid can vaporize in the cooling heat exchanger 8 and release the impurities. The resulting mixture can be returned to the outside or to a recovery area and can, in particular, be reinjected into the user fluid reservoir 16.

[0057] The invention can be applied to a process for cooling and / or liquefying another fluid or mixture, in particular hydrogen.

Claims

1. A method of refrigeration and / or liquefaction of a user fluid flow, notably natural gas, the method utilizing a cooling and / or liquefaction installation comprising a low-temperature refrigeration device (1), i.e. at a temperature comprised between minus 100 degrees centigrade and minus 273 degrees centigrade, the refrigeration device (1) comprising a working circuit (10) forming a loop and containing a working fluid, the working circuit (10) forming a cycle comprising in series: a mechanism (2, 3) for compressing the working fluid, a mechanism (6) for cooling the working fluid, a mechanism (7) for expanding the working fluid and a mechanism (6, 8) for reheating the working fluid, the refrigeration device (1) comprising a cooling exchanger (8) intended to extract heat from the user fluid flow by heat exchange with the working fluid circulating in the working circuit (10), the installation comprising a circulation line (15) for said user fluid flow in the cooling exchanger (8), the method comprising a cooling step in which the refrigeration device (1) is in a first operational cooling mode of the cooling exchanger (8) while a user fluid flow is circulated in this cooling exchanger (8), the method comprising, after this cooling step, a cleaning step for solidified impurities in the cooling exchanger (8), wherein, during the cleaning step, the refrigeration device (1) being in a second operational mode in which the working gas circulates in the working circuit (10) but in which the cooling of the exchanger (8) is reduced compared to the first operational mode, characterized in that the compression mechanism comprises several rotary compressors (2, 3) and at least two drive motors (14, 15), each comprising a rotating drive shaft, the compressors (2, 3) being driven in rotation by the respective rotating shaft(s), the working fluid expansion mechanism comprising at least one rotary turbine (7) integral in rotation with a shaft of one of the drive motors (14, 15) of at least one compressor (2), and in that in the first operational mode of the refrigeration device (1), the rotating shafts of the drive motors (14, 15) turn according to first respective rotation directions and the working fluid circulates in the working circuit (10) according to a first circulation direction and in that, in the second operational mode of the refrigeration device (1), at least one motor (15) of the drive motors (14, 15), notably the motor (15) to whose shaft the turbine (7) is coupled, is set in reverse rotation, that is to say that its rotation shaft turns in the rotation direction opposite to the first rotation direction.

2. The method according to claim 1, characterized in that, during the cleaning step, the refrigeration device (1) ensures zero cooling or ensures heating of the cooling exchanger (8).

3. The method according to claim 1 or 2, characterized in that, during the cleaning step, a user fluid flow is circulated in the cooling exchanger (8) and is reheated by the latter.

4. The method according to any one of claims 1 to 3, characterized in that the refrigeration capacity of the refrigeration device (1) is variable and controlled by regulating the rotation speed of at least one of the drive motors (14, 15), and in that, in the second operational mode, the rotation speed of at least one of the drive motors (14, 15) is comprised between 1% and 60% and preferably between 10% and 50%, notably between 20% and 30% of the maximum or nominal rotation speed of said motor (14, 15).

5. The method according to any one of claims 1 to 4, characterized in that the at least one compressor (2) driven by the motor (15) comprising the turbine (7) integral in rotation with its shaft is of the centrifugal type, and in that, in the second operational mode of the refrigeration device (1), the working fluid circulates in the working circuit (10) according to the first circulation direction.

6. The method according to any one of claims 1 to 5, characterized in that, in the second operational mode of the refrigeration device (1), at least one drive motor (14) of the drive motors (14, 15) distinct from the motor (2) set in reverse rotation is set to stop or operates with a rotation speed comprised between 1% and 60% and preferably between 10% and 50%, notably between 20% and 30% of the maximum or nominal rotation speed of said motor (14).

7. The method according to any one of claims 1 to 6, characterized in that the circulation of a user fluid flow in the cooling exchanger (8) is carried out by pumping into a user fluid reservoir (16) and in that the user fluid having undergone thermal exchange with the cooling exchanger (8) is returned to the reservoir (16).

8. An apparatus for low-temperature refrigeration, i.e. at a temperature comprised between minus 100 degrees centigrade and minus 273 degrees centigrade, comprising a working circuit (10) forming a loop and containing a working fluid, the working circuit (10) forming a cycle comprising in series: a mechanism (2, 3) for compressing the working fluid, a mechanism (6) for cooling the working fluid, a mechanism (7) for expanding the working fluid and a mechanism (6) for reheating the working fluid, the device (1) comprising a cooling exchanger (8) intended to extract heat from at least one organ (25) by heat exchange with the working fluid circulating in the working circuit (10), the refrigeration device comprising an electronic controller (12) configured to control the refrigeration capacity of the refrigeration device (1) and to switch the refrigeration device (1) into a first operational cooling mode of the cooling exchanger (8) to cool a user fluid flow circulated in this cooling exchanger (8), and a cleaning mode for solidified impurities in the cooling exchanger (8), wherein, in the cleaning mode, the electronic controller (12) being configured to lower the refrigeration capacity of the refrigeration device (1) and to reduce the cooling of the cooling exchanger (8) compared to the first operational mode, characterized in that the compression mechanism comprises several rotary compressors (2, 3) and at least two drive motors (14, 15), each comprising a rotating drive shaft, the compressors (2, 3) being driven in rotation by the respective rotating shaft(s), the working fluid expansion mechanism comprising at least one rotary turbine (7) integral in rotation with a shaft of one of the drive motors (14, 15) of at least one compressor (2) and characterized in that in the first operational mode, the drive motors (14, 15) are configured to turn their rotating shafts according to first respective rotation directions, and in that at least the motor (15) comprising the turbine (7) integral in rotation with its shaft is of the reversible rotation direction type and in that the electronic controller (12) is configured to turn said motor (15) in the rotation direction opposite to the first rotation direction during the second operational mode of the refrigeration device (1).

9. The apparatus according to claim 8, characterized in that the refrigeration capacity of the refrigeration device (1) is variable and controlled by regulating the rotation speed of at least one of the motors (14, 15) of drive, and in that, the electronic controller (12) is configured to establish the rotation speed of at least one of the drive motors (14, 15) in the second operational mode at a value comprised between 2% and 60% and preferably between 10% and 50%, notably between 20% and 30% of the maximum or nominal rotation speed of said motor (14, 15).

10. The apparatus according to any one of claims 8 to 9, characterized in that in the second operational mode of the refrigeration device (1), the electronic controller (12) is configured to set to stop at least one drive motor (14) of the drive motors (14, 15) distinct from the motor (2) set in reverse rotation, or to limit the rotation speed of this drive motor distinct from the motor (2) set in reverse rotation to a value comprised between 1% and 60% and preferably between 10% and 50%, notably between 20% and 30% of the rotation speed of said motor (2) during the first operational mode of operation.

11. An installation for refrigeration and / or liquefaction of a user fluid flow, notably natural gas, comprising a refrigeration device (1) according to any one of claims 8 to 10, the installation comprising at least one user fluid reservoir (16), a circulation line (25) for said user fluid flow in the cooling exchanger (8).