JP2017150661A - Control method of high pressure hydrogen charging system with expansion turbine and compressor - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a control method of a high pressure hydrogen charging system with an expansion turbine and compressor, which has a simple structure, can reduce a site construction cost, can reduce load of work for maintenance management, can reduce an operation cost including a cost of power consumption, extracts energy occurring in an expander, does not need to separately provide effectively usable means to the outside of a dynamo or the like, and can be applicable to a temperature lowering system technology, such as a pre-cooling function, at a final charging part of a hydrogen station.SOLUTION: A charging system, which when pressurizing and charging hydrogen gas accumulated in a high pressure state to a tank 6, performs enthalpy lowering of hydrogen gas with an expansion turbine, includes a process of assembling an expansion turbine compressor 11 into an expansion turbine portion, and a cooler 12 at an inlet part on the expansion turbine side, and is configured to control an outlet temperature of hydrogen gas of the cooler 12.SELECTED DRAWING: Figure 7

Description

  The present invention relates to hydrogen for filling a fuel tank of a hydrogen vehicle from a hydrogen gas supply source with hydrogen gas serving as a fuel for a hydrogen vehicle such as a fuel cell vehicle (hereinafter sometimes simply referred to as “hydrogen vehicle”). The present invention relates to a method for controlling a high-pressure hydrogen expansion turbine / compressor filling system applied to a temperature drop system technology such as a precooler function in a final filling section of a filling facility (hereinafter also referred to as “hydrogen station”).

Hydrogen gas used as a fuel for hydrogen automobiles is subject to reversal temperature (-58 ° C) due to its properties when adiabatic expansion (equal enthalpy expansion) is performed from high pressure in a portion such as an expansion valve provided in a path filled with hydrogen gas. Furthermore, since the expansion occurs in a high region, the temperature after expansion is increased by the Joule-Thompson effect.
Therefore, when hydrogen gas serving as fuel for a hydrogen vehicle is filled from a hydrogen gas supply source into a fuel tank of the hydrogen vehicle at a hydrogen station, the hydrogen gas is generated at a portion such as an expansion valve provided in a path for filling the hydrogen gas. The gas temperature rises.

This increase in the temperature of the hydrogen gas becomes more significant as the expansion ratio of the hydrogen gas increases. Therefore, the pressure of the supply gas from the hydrogen gas supply source at the hydrogen station is increased, for example, the pressure of the supply gas (supply source As the tank pressure is increased from 45 to 70 MPa (G), and further to 82 MPa (G), the amount of increase in self-temperature further increases.
As an example, FIG. 1 shows an example of a self-temperature change at each secondary pressure when hydrogen gas is expanded from 70 MPa (G), which is a tank pressure of a supply source, in one step.

  On the other hand, in the fuel cell vehicles that have started to spread at present, the maximum temperature upper limit at the time of hydrogen filling is set to 85 ° C. due to the temperature limitation by the material of the fuel tank and the limitation of the operation temperature of the fuel cell main body cell.

  And, due to the nature of hydrogen, if hydrogen gas is charged as it is without any means, the temperature at the time of hydrogen filling exceeds the maximum upper limit of 85 ° C., the temperature limit depending on the material of the fuel tank and the fuel cell Since problems such as pressure drop due to cooling of the main body cell and cooling after filling occur, a cooling means such as a heat exchanger is arranged in the path filled with hydrogen gas. A method of filling a hydrogen automobile while cooling gas has been proposed and put into practical use (see, for example, Patent Document 1).

JP 2004-116619 A

Here, FIG. 2 shows a configuration diagram of the current general 70 MPa (G) hydrogen station (source “NEDO Hydrogen Energy White Paper”).
This hydrogen station is composed of a compressor facility 1 composed of a compressor unit that receives hydrogen gas, a hydrogen pressure accumulation facility 2 composed of a pressure accumulator unit that accumulates hydrogen gas sent from the compressor facility 1, and a hydrogen pressure storage facility 2. An expansion valve 3 and a hydrogen gas precooler 4 provided in a path for filling the fuel tank 6 of the hydrogen vehicle with hydrogen gas, and a hydrogen precooling system 5 that cools the hydrogen gas via the precooler 4. The hydrogen precooling system 5 is provided with a refrigerator equipment 7 including a compressor, a condenser, an expansion valve, an evaporator, an accumulator, and the like, and a brine circuit 8 including a brine tank, a primary brine pump, a secondary pump, and the like. ing.
In this hydrogen station, both the on-site type and off-site type hydrogen stations receive the hydrogen in the compressor facility 1 at an intermediate pressure (40 MPa (G) in the example) or high pressure (82 MPa (G in the example). )) And is held in the form of compressed gas in the accumulator unit of the hydrogen accumulator 2 at each pressure.
In order to fill these on-demand fuel tanks 6 with the hydrogen gas, expansion is performed through the expansion valve 3. At this time, the temperature of the hydrogen gas itself is increased. It is cooled to −40 ° C. by a certain hydrogen precooling system 5.
In the current technology, the hydrogen precool system 5 is configured by combining a normal refrigerator equipment 7 such as a chlorofluorocarbon refrigerant and a brine circuit 8 that operates near −40 ° C. In addition, many rotary devices such as a refrigerant compressor for a refrigerator, a primary brine pump, and a secondary brine pump are also required.

For this reason, the hydrogen precooling system used for lowering the temperature of the hydrogen gas in the final filling section of the conventional hydrogen station has the following problems.
1) An external independent hydrogen precooling system is a system that itself operates with external power. It is about 40 kW at a general hydrogen station (300 Nm ³ / h), and the operation of the hydrogen precool system itself increases the operating cost.
2) Because of the use of chlorofluorocarbon (alternative chlorofluorocarbon) as the refrigerant of the refrigerator, it is legally treated, and the precooler equipment itself is subject to the refrigeration safety law of the High-Pressure Gas Safety Law, and is restricted in equipment and operation.
3) Holding chlorofluorocarbons or brine in the station requires measures to prevent environmental accidents against external leakage of chlorofluorocarbons or brine.
4) Since the hydrogen precooling system is complicated with a two-stage configuration of a refrigeration circuit and a brine circuit, and there are a plurality of rotating machines such as a refrigerant compressor and a brine pump, many maintenance management services arise.
5) Since it is a system via brine, it takes time from the start of operation to the steady state. For this reason, it is necessary to start the hydrogen precooling system in advance and fill the system in a steady state long before the filling operation.
6) When the installation space of the hydrogen station itself is reduced in size, the space occupied by the hydrogen precool system becomes a limitation.
7) At the current temperature of −40 ° C., there is a limit to further rapid hydrogen filling. In the future, in order to further shorten the filling time, pre-cooling may be required at a temperature lower than the current -40 ° C.

  By the way, in view of the problems of the hydrogen precooling system used for lowering the temperature of the hydrogen gas in the final filling portion of the conventional hydrogen station, the applicant of the present application previously described in Japanese Patent Application No. 2015-059323. We propose a hydrogen precooling system used to lower the temperature of hydrogen gas at the final filling section of the hydrogen station, which is simple, has less burden on maintenance management services, and can reduce operating costs including power consumption. .

The hydrogen precooling system used to lower the temperature of the hydrogen gas in the final filling section of this hydrogen station lowers the temperature of the hydrogen gas by an expander that extracts work in the process of expanding and depressurizing the hydrogen gas. This is a precooling of hydrogen gas using energy, and can solve the problems of the hydrogen precooling system used for lowering the temperature of the hydrogen gas in the final filling section of the conventional hydrogen station. However, there were the following problems.
8) It is necessary to separately provide a means for taking out and effectively using energy generated in the expander.

  In view of the problems of the hydrogen precooling system used for lowering the temperature of hydrogen gas in the final filling section of the conventional hydrogen station, the present invention has a simple configuration, can reduce the construction cost, and can be used for maintenance management services. The operation cost including the power consumption can be reduced, and there is no need to separately provide a means for taking out the energy generated in the expander and effectively using it outside the generator, etc. An object of the present invention is to provide an expansion turbine / compressor filling system for high-pressure hydrogen that can be applied to a temperature drop system technology such as a precooler function in a filling section.

  In order to achieve the above object, the control method of the high-pressure hydrogen expansion turbine / compressor filling system according to the present invention uses an expansion turbine to compress the hydrogen gas when the hydrogen gas accumulated at high pressure is charged into the tank. A method for controlling a filling system for performing enthalpy lowering, characterized in that a process for incorporating an expansion turbine / compressor in an expansion turbine section, a cooler is provided at an inlet portion of the expansion turbine, and a hydrogen gas outlet temperature of the cooler is controlled. To do.

  In this case, the hydrogen gas outlet temperature of the cooler can be detected, and the amount of cold energy of the cooler can be adjusted and followed so that the outlet temperature becomes an appropriate temperature.

  In addition, the distribution of the filling time when the hydrogen gas is pressurized and filled into the tank can adjust and follow the amount of cold energy of the cooler so that the optimum gas temperature is obtained at each filling stage.

  It is also possible to detect the pressure and temperature rise of the tank and adjust and follow the amount of cold energy of the cooler so that the optimum gas temperature is obtained at each filling stage.

According to the control method of the high-pressure hydrogen expansion turbine / compressor filling system of the present invention, when the hydrogen gas accumulated at a high pressure is pressurized and filled into the tank, the filling is performed using the expansion turbine to lower the enthalpy of the hydrogen gas. In the system control method, a process for incorporating an expansion turbine / compressor into an expansion turbine section and a cooler at an inlet portion on the expansion turbine side are controlled, and an outlet temperature of hydrogen gas of the cooler is controlled. The hydrogen is expanded to fill the adjustment tank with hydrogen gas with reduced enthalpy (temperature drop), which makes the configuration simple, reduces the burden of maintenance management services, and includes the cost of power consumption. Can be used to lower operating costs, for example, to lower the temperature of hydrogen gas in the final filling section of a hydrogen station It is possible to provide a hydrogen pre-cool system.
And a process for incorporating an expansion turbine / compressor in the expansion turbine section, that is, in an expander by using an expansion turbine / compressor having an expansion impeller on one side of the rotating shaft and a compression impeller on the other side. There is no need to separately provide a means for taking out the energy to be used effectively, and further, the rotational energy obtained on the expansion turbine side is used to increase the pressure of the hydrogen gas on the compressor side, leading to the inlet of the expansion turbine. As a result, the expansion ratio of the expansion turbine is increased by the amount boosted by the compressor, and a larger heat drop (= cold generation amount) can be obtained. Equipped with a cooler to reduce the temperature of the hydrogen gas to an appropriate value. Process establishment of a low expansion turbine of securing and more efficient in the margin can be achieved.
By the way, when the expander used in this process, that is, the turbine is designed with a capacity suitable for the current standard hydrogen filling station (hydrogen station), it is inevitable that it becomes a very small and high-speed rotating body. . In the case of a system in which 5 kg of high-pressure hydrogen gas is filled in about 3 minutes, the diameter of the expansion turbine is 8 to 12 mm, and the rotation speed corresponding to the maximum expansion ratio corresponds to 1.2 million revolutions / minute.
Therefore, in the high-pressure hydrogen expansion turbine / compressor filling system of the present invention, specifically, an impeller (turbine) that performs expansion action on one side of the rotor shaft of the rotor is obtained by expansion on the other side. Impellers (compressors) that perform a compression action that consumes the rotational energy are provided and configured.
The energy extracted by the expansion of the hydrogen gas by the turbine is extracted as kinetic energy in the form of high-speed rotation of the turbine rotor. To realize this high-speed rotation, the expansion turbine compressor is supplied with the supplied hydrogen gas. Use the hydrodynamic gas bearing type bearing.
For this reason, the “work” taken out as rotational energy can be one in which the friction loss (shaft loss) by the bearing is suppressed to a very small value.
The amount of energy obtained by subtracting this shaft loss from the rotational energy obtained by the turbine is consumed by centrifugally boosting the process gas on the compressor side, and the rotation balances.
That is, the rotational energy (turbine power) extracted by the turbine is consumed by boosting the process gas in a compressor provided on the opposite side of the rotating shaft and driven at the same rotational speed.
With this dynamic pressure type gas bearing type bearing, a compact and high-speed rotating body bearing as in the present invention is configured, so that it is possible to ensure ultra-high speed rotation and very low shaft loss.
In this way, the power recovery can be made as a turbine / compressor system without generating power or recovering the outside, and the configuration is simple and the construction cost can be reduced.
The process gas pressurized on the compressor side is accompanied by an increase in pressure and temperature due to thermodynamic compression. The rise in temperature is cooled to about 20 ° C., for example, by disposing it as heat by providing a cooler (air-cooled or water-cooled aftercooler) as necessary. The increase in pressure results in an increase in pressure at the turbine inlet, so that the expansion ratio in the turbine is further increased, and as a result, the amount of cold generation is increased.
In the present invention, the technical reason for adopting a turbine compressor in the process without converting the power extracted by the turbine into electric power by a generator or the like is that a device that is too small and fast rotating is a generator. The process itself may be small and high-frequency, and may not be established. In addition, the process gas has an advantage from the viewpoint of explosion prevention because of hydrogen.

It is a graph which shows the change of the filling flow rate by the expansion | swelling (valve expansion) using the expansion valve of hydrogen gas, pressure, and temperature. It is explanatory drawing of the hydrogen station using the conventional hydrogen precool system. It is explanatory drawing which shows one Example of the expansion turbine compressor compression type | system | group of the high pressure hydrogen which implements the control method of the expansion turbine compressor compression type | system | group of the high pressure hydrogen of this invention. It is explanatory drawing which shows the deformation | transformation Example of the expansion turbine compressor compression type | system | group of a high pressure hydrogen which implements the control method of the expansion turbine compressor compression type | system | group of the high pressure hydrogen of this invention. It is a graph which shows the expansion (valve expansion) (conventional system) using the expansion valve of hydrogen gas, and the change of the filling flow rate and pressure by the expansion turbine compressor type filling system (example) of the present invention. It is a graph which shows the change of the temperature by the expansion (valve expansion) (conventional system) using the expansion valve of hydrogen gas, and the expansion turbine compressor type filling system (example) of the high-pressure hydrogen of the present invention. It is explanatory drawing which shows one Example of the system configuration | structure of the expansion turbine compressor compression type | system | group of a high pressure hydrogen which implements the control method of the expansion turbine compressor compression type | system | group of the high pressure hydrogen of this invention. It is a graph which shows the relationship between the filling completion temperature at the time of providing the cooler in the expansion turbine side inlet part, and changing the temperature of hydrogen gas, and turbine efficiency. It is explanatory drawing which shows one Example of the system configuration | structure of the expansion turbine compressor compression type | system | group of a high pressure hydrogen which implements the control method of the expansion turbine compressor compression type | system | group of the high pressure hydrogen of this invention.

  Embodiments of a control method for an expansion turbine / compressor filling system for high-pressure hydrogen according to the present invention will be described below with reference to the drawings.

  The control method of the high-pressure hydrogen expansion turbine / compressor filling system is the same as the control method of the high-pressure hydrogen expansion turbine / compressor filling system of the present invention in order to lower the temperature of the hydrogen gas in the final filling portion of the hydrogen station. The hydrogen precooling system is applied to a used hydrogen precooling system, and the hydrogen precooling system uses an expansion turbine to lower the enthalpy of the hydrogen gas when the hydrogen gas accumulated at a high pressure is charged into the tank. In the above, the process of incorporating the expansion turbine / compressor into the expansion turbine portion and the cooler at the inlet side of the expansion turbine are configured.

Here, in order to provide a process for incorporating an expansion turbine / compressor into the expansion turbine portion, in the present embodiment, for example, for the purpose of expansion on one side of a rotary shaft that has been conventionally used for compressing and expanding refrigerant. A turbine compressor having an impeller and a compression impeller on the other side (hereinafter referred to as “expansion turbine compressor”) can be used.
The expansion turbine / compressor can be configured to include a hydrodynamic gas bearing type bearing using a supplied hydrogen gas (bearing that supports both radial and thrust directions).

  Specifically, like the hydrogen gas final expansion mechanism of the hydrogen station shown in FIG. 3, the hydrogen precooling system 10 is configured by connecting the hydrogen gas source line 9 to the circuit of the expansion turbine / compressor 11. The hydrogen gas finally expanded by the expansion turbine / compressor 11 and reduced in enthalpy (temperature drop) is filled into the fuel tank 6 of the hydrogen vehicle via the hydrogen gas supply unit 13. ing.

  Here, the expansion turbine / compressor 11 was obtained on the side of the expansion turbine 11a by including an expansion turbine 11a having an expansion impeller on one side of the rotating shaft and a compressor 11b having a compression impeller on the other side. Rotational energy is used to increase the pressure of hydrogen gas on the compressor 11b side so that it is guided to the inlet of the expansion turbine 11a (hydrogen gas is supplied to the compressor 11b and then supplied to the expansion turbine 11a. As a result, the expansion ratio of the expansion turbine 11a is increased by the amount boosted by the compressor 11b, and a larger heat drop (= cold generation amount) can be obtained.

Further, the cooler 12 and its control device 14 can be provided at the inlet portion of the expansion turbine / compressor 11 on the expansion turbine 11a side.
As the cooling heat source 12a of the cooler 12, a water cooling type or a chiller unit type can be suitably used.
Moreover, although illustration is abbreviate | omitted, the same cooler can also be provided in the inlet_port | entrance part by the side of the compressor 11b.
As a result, the temperature drop of the hydrogen gas can be assisted. By reducing the temperature of the hydrogen gas to an appropriate value, it is possible to secure a temperature margin at the completion of tank filling and to establish a process with a less efficient expansion turbine. It becomes.

  FIG. 5 and FIG. 6 show the filling flow rate, pressure and temperature of the expansion (valve expansion) using a hydrogen gas expansion valve (conventional method) and the high-pressure hydrogen expansion turbine / compressor filling system (example) of the present invention. Showing change.

By applying the high pressure hydrogen expansion turbine-compressor filling system to the hydrogen precooling system used to lower the temperature of the hydrogen gas in the final filling section of the hydrogen station, the high pressure (82 MPa) of the hydrogen gas source line 9 ( The expansion turbine / compressor 11 can be driven from the hydrogen gas of the original pressure) to the fuel tank 6 of the hydrogen automobile by using the pressure difference to directly fill the expanded hydrogen gas.
In this case, since the difference between the original pressure and the internal pressure of the fuel tank 6 is large in the initial stage of filling, the expansion ratio in the expansion turbine 11a and the expansion ratio in the compressor 11b can be relatively large, so that more cold is generated. be able to.
As the filling progresses, the internal pressure of the fuel tank 6 rises, and the cold generated by the expansion turbine / compressor 11 decreases, but the filling can finally be completed at 85 ° C. or lower.

Incidentally, in the embodiment shown in FIG. 3, one expansion turbine / compressor 11 is used. However, as shown in the modified embodiment shown in FIG. 4, a plurality of units are arranged in series. In addition, a plurality of units arranged in series can be arranged in parallel.
As a result, the turbine efficiency of the expansion turbine / compressor 11 can be operated in the maximum region at the respective expansion ratios, and the amount of cold generated can be given a margin, or the facility flow rate can be easily increased. A large fuel cell bus or truck filling facility can be constructed without a precool cooler.

In the embodiment shown in FIG. 3 (the same applies to the embodiment shown in FIG. 4), as shown in FIG. 7, the cooler 12 and its control are provided at the inlet portion of the expansion turbine / compressor 11 on the expansion turbine 11a side. A device 14 is provided to control the outlet temperature of the hydrogen gas from the cooler 12.
By configuring in this way, the outlet temperature of the hydrogen gas of the cooler 12 can be appropriately lowered, and thereby a margin of temperature in the fuel tank 6 at the completion of filling can be provided.

  In FIG. 7, the hydrogen gas outlet temperature of the cooler 12 is lowered by the control device 14 from, for example, the normal vicinity of 33 ° C. to 25 ° C. and 20 ° C., as shown in FIG. In addition to providing a margin for the temperature rise in the tank 6, it is possible to configure a process having lower expansion turbine efficiency as a process. That is, instead of lowering the temperature with a new cooler, the desired temperature can be achieved by adjusting the cooling of the cooler 12.

In this case, the outlet temperature of the hydrogen gas of the cooler 12 is detected, and the setting is relatively low at the initial stage of filling (the first 20 to 30 seconds), and as the filling proceeds (as the cold load decreases), proper cold generation is generated. It is desirable to program so that the outlet temperature of the hydrogen gas follows the target temperature.
Specifically, control of the protocol for filling hydrogen gas into the fuel tank 6 is performed by a control device (controller) provided in the hydrogen gas supply unit 13. In this case, by calculating the optimum cold suitable for the filling time distribution specified in advance and optimally controlling the inlet temperature of the expansion turbine 11a (the outlet temperature of the cooler 12), without unnecessary cooling, Filling can be performed with minimal external energy.

It is also possible to detect the pressure and temperature rise in the fuel tank 6 so that the outlet temperature of the hydrogen gas follows the target temperature.
Specifically, as shown in FIG. 9, the current pressure and temperature of the fuel tank 6 are detected on the hydrogen gas supply unit 13 side, the optimum cold amount until completion of filling is calculated, and the expansion turbine is automatically controlled. By optimally controlling the inlet temperature of 11a (the outlet temperature of the cooler 12), it is possible to perform charging with minimum external energy without performing unnecessary cooling.

By applying the control method of the high-pressure hydrogen expansion turbine / compressor filling system of the present invention to the hydrogen precooling system used to lower the temperature of the hydrogen gas in the final filling section of the hydrogen station, The problem of the hydrogen precooling system used for lowering the temperature of the hydrogen gas in the final filling section can be solved as follows.
As for the problem 1), since no external electric power is required for the operation of the expansion turbine / compressor itself, little electric power is required for the operation cost (electricity cost) of the conventional hydrogen precooling system.
Regarding the problem 2), since there is no refrigerant, the system does not separately follow the refrigeration law. It can be dealt with in the high-pressure gas safety law of the entire hydrogen station.
As for the problem 3), since there is no chlorofluorocarbon refrigerant or brine itself, there is no risk for an environmental accident.
As for Problem 4), since the system configuration is quite simple, not only the operation cost but also the maintenance cost can be greatly reduced.
Regarding the problem 5), since the temperature drop state can be created simultaneously with the start of the expansion turbine / compressor, the time constant in the system is very small. There will be little pre-launch time.
With respect to the problem 6), only a cold box for the expansion turbine / compressor is required, so that a large space can be saved. The volume ratio is about 10% of the conventional one.
As for Problem 7), it is possible to easily increase the facility flow rate by combining multiple expansion turbines / compressors or using an expansion turbine / compressor with an optimal flow rate. It is possible to configure a battery bus or truck filling facility.
As for Problem 8), it is not necessary to separately provide a means for taking out the energy generated in the expander by using an expansion turbine / compressor and using it effectively. Furthermore, the rotational energy obtained on the expansion turbine side is used. By increasing the pressure of the hydrogen gas on the compressor side and guiding it to the inlet of the expansion turbine, the expansion ratio of the expansion turbine is increased by the amount boosted by the compressor, and more heat drop (= cold In addition, by providing a cooler at the inlet side of the expansion turbine and lowering the hydrogen gas temperature to an appropriate value, it is possible to ensure the temperature margin at the time of tank filling completion and more efficiency It is possible to establish a process with a low expansion turbine.

  The control method of the high-pressure hydrogen expansion turbine / compressor filling system according to the present invention has been described based on the embodiment. However, the present invention is not limited to the configuration described in the above embodiment, and the gist thereof is described. The configuration can be changed as appropriate without departing from the scope of the invention.

  The control method of the high-pressure hydrogen expansion turbine / compressor filling system of the present invention has a simple configuration, can reduce the cost of construction work, has a low burden of maintenance management service, and can reduce the operation cost including the power consumption cost. Furthermore, since there is no need to separately provide means for taking out the energy generated in the expander and effectively using it outside the generator, the temperature of the hydrogen gas is adjusted at the final filling section of the hydrogen station. It can use suitably for the use of the hydrogen precool system used in order to make it fall.

1 Compressor equipment 2 Hydrogen pressure storage equipment 3 Expansion valve
4 Precooler 5 Hydrogen precooling system 6 Fuel tank (tank)
7 Refrigerator equipment 8 Brine circuit 9 Hydrogen gas source line 10 Hydrogen precool system 11 Expansion turbine / compressor 11a Expansion turbine 11b Compressor 12 Cooler 12a Cold heat source 13 Hydrogen gas supply unit 14 Control device

Claims (4)

  In a method for controlling a filling system in which an enthalpy of hydrogen gas is lowered using an expansion turbine when hydrogen gas stored at a high pressure is charged into a tank, a process for incorporating an expansion turbine / compressor into the expansion turbine portion and the expansion turbine A control method for an expansion turbine / compressor filling system of high-pressure hydrogen, comprising a cooler at a side inlet portion, and controlling an outlet temperature of hydrogen gas of the cooler.   2. The high pressure according to claim 1, wherein the outlet temperature of the hydrogen gas of the cooler is detected and the amount of cold energy of the cooler is adjusted and followed so that the outlet temperature becomes an appropriate temperature. A control method for a hydrogen expansion turbine / compressor filling system.   The cooling energy amount of the cooler is adjusted and followed so that an optimum gas temperature is obtained at each filling stage by distributing filling time when hydrogen gas is pressurized and filled into the tank. 3. A method for controlling an expansion turbine / compressor filling system for high-pressure hydrogen according to 1 or 2.   The pressure and temperature of the tank are detected, and the amount of cold energy of the cooler is adjusted and followed so that the optimum gas temperature is obtained in each filling stage. A control method for the high-pressure hydrogen expansion turbine / compressor filling system according to claim 1.

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