KR20120060083A - Method of determining the relations of hydrogen-absorbing alloys - Google Patents

Abstract

PURPOSE: A pressure-composition isotherm measuring system of a hydrogen absorbing alloy is provided to accurately measure the absorption or desorption diagram of hydrogen by automatically implementing experiments based on a controlling part. CONSTITUTION: A pressure-composition isotherm measuring system of a hydrogen absorbing alloy includes a hydrogen injecting part(112), a measuring container(114), a first valve(115), a reacting part(116), a second valve(117), a pressure sensor part(118), a hydrogen discharging part(119), a third valve(120), and a controlling part. The measuring container is in connection with a hydrogen injecting part and stores hydrogen. The first valve opens and closes a part between the hydrogen injecting part and the measuring container. The second valve opens and closes a part between the measuring container and the reacting part. The pressure sensor measures the pressure of the measuring container and pressures between the measuring container and the reacting part. The third opens and closes the discharging part. Hydrogen is injected into the measuring container based on a pre-set pressure. Valves are closed, and a second valve is opened to measure pressures between the measuring container and the reacting part. The absorbing rate of the hydrogen according to the changing of pressure with respect to a specimen inserted into the reacting part is calculated by the controlling part.

Description

Method for determining the relations of hydrogen-absorbing alloys

The present invention is a system for measuring the absorbance diagram and the emission diagram of the hydrogen is absorbed in the various (Metallic alloy for hydrogen storage) samples, more specifically, the size of the capacity of the measuring vessel and the reaction unit is formed as a set capacity And a pressure-forming isotherm measurement system for hydrogen storage alloys to automatically obtain more accurate and reliable measurements of hydrogen absorption and emission diagrams.

Conventionally, there is no separate device for measuring the absorption or release curve of hydrogen absorbed by the sample, and the user subjectively measures the absorption or release curve of hydrogen by various methods and systems.

However, the use of different, non-standardized methods and systems makes the measurement data unreliable and presents a difficult problem in accurately measuring the absorption or release curves of hydrogen.

In other words, the temperature of the reaction part and the measuring part where the sample is accommodated should be kept constant at the set temperature, but the user cannot take accurate measurements because the subjective measurement does not take into account the influence of other equipment and the surrounding temperature. There are numerous problems and reliability of measurement data.

In addition, in order to measure the freshness or release of hydrogen in the sample, an accurate ratio of hydrogen uptake or release can be measured only when the internal volume of the measuring vessel and the reaction portion is in an appropriate ratio. However, as a combination of various equipments is used, there is a problem in that the absorption or release diagram of hydrogen is not properly measured due to lack of compatibility. In addition, if the ratio of the internal volume of the measuring vessel and the reaction volume of the reaction unit is larger than the standard in the process of combining several equipments, there is a problem that the unnecessary hydrogen gas increases and the measurement time is delayed. It is difficult to match the amount of gas, which leads to the problem that the accurate absorption or emission curves cannot be measured.

The present invention has been made to solve the above problems, by tightly sealing the surrounding environment of the reaction unit and the measuring device to minimize the temperature change of the reaction unit and the measuring device, the volume ratio of the inner space of the measuring vessel and the reaction unit Optimized to accurately measure the freshness of hydrogen absorbed or released on the sample put into the reaction part within a short time, automatically control the heater to maintain the reaction part at the set temperature, and hydrogen storage for easy and smooth replacement of the sample Its purpose is to provide a system for measuring the pressure-forming isotherms of an alloy.

An object of the present invention, the hydrogen injection unit in which hydrogen is injected from the outside; and a measuring vessel connected to the hydrogen injection unit for storing hydrogen; and a first valve for opening and closing between the hydrogen injection unit and the measuring vessel; and measurement A reaction unit into which a sample is inserted to react with hydrogen by receiving hydrogen stored in the container; and a second valve for opening and closing between the measuring container and the reaction part; and measuring the pressure of the measuring container or the pressure between the measuring container and the reaction part. A pressure sensor unit; and a discharge unit through which hydrogen is discharged; and a third valve opening and closing the discharge unit; And a control unit for controlling opening and closing of the first to third valves and receiving pressure information of the pressure sensor unit, injecting hydrogen into the measuring container at a set pressure, and closing the first to third valves. Opening the second valve to measure the pressure between the measuring vessel and the reaction part, and the control unit calculates a diagram in which the hydrogen is absorbed or released into the sample inserted into the reaction part according to the pressure change. It is achieved by a measuring system of isotherms (PCT curves).

In addition, the volume of the internal space of the measuring vessel may be formed in a volume of 29 to 31 times the volume of the internal space of the reaction unit so that the section of the hydrogen is absorbed in the sample according to the pressure change.

In addition, the volume of the inner space of the measuring vessel may be formed from 205.9 cm 3 to 226.3 cm 3, and the volume of the inner space of the reaction part may be formed from 7.1 cm 3 to 7.3 cm 3.

The apparatus may further include a heating unit including a heater for maintaining a constant temperature of the reaction unit and a lifting unit for elevating the heater, wherein the temperature unit may be controlled by the controller.

The apparatus may further include a suction pump connected between the measuring vessel and the third valve in order to remove the injected hydrogen or to recapture (release) the hydrogen absorbed in the sample.

The present invention optimizes the size of the internal volume of the measuring vessel and the internal volume of the reaction part, thereby minimizing the error of the absorption or desorption diagram of hydrogen and accurately measuring the absorption or desorption curve of hydrogen absorbed in the sample within a short time. There is an advantage. In addition, since the heater operates automatically, and only the reaction part containing the sample is desorbed, all the experiments are automatically made through the control unit when only the sample is replaced, so that the absorption or desorption diagram of hydrogen can be measured quickly and accurately.

In addition, by installing a suction pump, it is possible to easily remove the hydrogen gas and foreign substances inside the measuring device to a vacuum state, and if a gas leaks or a fire occurs inside the measuring device, the controller checks this and injects nitrogen. It also has the advantage that the measuring device can proactively control fire and danger from overheating.

1 is a block diagram schematically illustrating a system for measuring a pressure-forming isotherm (PCT curve) of a hydrogen storage alloy according to an exemplary embodiment of the present invention.
2 is a view schematically showing a measuring device in the present invention.
3 is a perspective view of a heating unit in the present invention.
4 and 5 are views showing the operating state of the heat generating unit in the present invention.
6 and 7 are graphs comparing and measuring a diagram in which hydrogen is absorbed or released into a sample according to an internal volume of a measuring container and a reaction part in the present invention.

An object of the present invention, the hydrogen injection unit 112 is injected hydrogen from the outside; and the measuring vessel 114 is connected to the hydrogen injection unit 112 to store hydrogen; And, the hydrogen injection unit 112 and measurement A first valve 115 for opening and closing between the containers 114; and a reaction unit 116 into which a sample is inserted to react with hydrogen by receiving hydrogen stored in the measuring container 114; and the measuring container 114; A second valve 117 that opens and closes between the reaction units 116; and a pressure sensor unit 118 that measures the pressure of the measurement container 114 or the pressure between the measurement container 114 and the reaction unit 116; And a discharge part 119 through which hydrogen is discharged; and a third valve 120 for opening and closing the discharge part 119; And a controller 20 that controls opening and closing of the first valve 115 to the third valve 120 and receives pressure information of the pressure sensor unit 118. After injecting hydrogen, closing the first valve 115 to the third valve 120, the second valve 117 is opened to measure the pressure between the measuring vessel 114 and the reaction unit 116 to change the pressure. The control system 20 calculates a diagram in which hydrogen is absorbed or released into the sample inserted into the reaction unit 116 according to the pressure-composition isotherm (PCT curve) of the hydrogen storage alloy.

In addition, the volume of the internal space of the measuring vessel 114 is formed to be 29 times to 31 times the volume of the internal space of the reaction unit 116 so that the section in which the hydrogen is absorbed by the sample is clearly revealed according to the pressure change. Can be.

In addition, the volume of the inner space of the measuring vessel 114 may be formed from 205.9 cm 3 to 226.3 cm 3, and the volume of the inner space of the reaction part 116 may be formed from 7.1 cm 3 to 7.3 cm 3.

The heating unit 30 further includes a heater 32 for maintaining a constant temperature of the reaction unit 116 and a lifting unit 31 for elevating and heating the heater 32. Controllable by 20.

In addition, the suction pump 121 is connected between the measuring vessel 114 and the third valve 120 in order to remove the injected hydrogen or to recapture (release) the hydrogen absorbed in the sample. have.

1 is a block diagram schematically illustrating a system for measuring a pressure-forming isotherm (PCT curve) of a hydrogen storage alloy according to an exemplary embodiment of the present invention;

2 is a view schematically showing a measuring device 10 in the present invention,

3 is a perspective view of the heating unit 30 in the present invention,

4 and 5 are views showing the operating state of the heat generating unit 30 in the present invention,

6 and 7 are graphs comparing and measuring the absorption or release of hydrogen in the sample according to the internal volume of the measuring vessel 114 and the reaction unit 116 in the present invention.

Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings.

1 to 5, the measurement system of the pressure-composition isotherm (PCT curve) of the hydrogen storage alloy according to the embodiment of the present invention includes a measuring device 10 and a control unit 20. Here, the heating unit 30 further includes.

The measuring apparatus 10 includes a main flow passage 111, a hydrogen injection unit 112, a nitrogen injection unit 124, a measuring vessel 114, a first valve 115, a reaction unit 116, and a second valve ( 117, a pressure sensor 118, a discharge part 119, a third valve 120, a fourth valve 123, and a suction pump 121.

The main flow passage 111 is formed of a substantially cylindrical tube.

The hydrogen injection unit 112 is provided with a substantially cylindrical hydrogen injection pipe and a backflow prevention hydrogen injection valve 113 for opening and closing the hydrogen injection pipe behind the hydrogen injection pipe, and the front end of the hydrogen injection pipe is external hydrogen injection. It is connected to the device, the rear end of the hydrogen injection pipe is connected to the main flow path 111.

The nitrogen injection unit 124 is provided with a substantially cylindrical nitrogen injection pipe and a backflow preventing nitrogen injection valve 125 that opens and closes the nitrogen injection pipe behind the nitrogen injection pipe, and the front end of the nitrogen injection pipe is external nitrogen injection. It is connected to the device, the rear end of the nitrogen injection pipe is disposed behind the hydrogen injection portion 112 is connected to the main flow path 111 line. Here, the nitrogen injection unit 124 is used for the purpose of extinguishing the fire by injecting nitrogen when a fire occurs inside the measuring device 10 of the present invention.

The measuring vessel 114 is connected to the middle portion of the main flow passage 111 and is a place for storing hydrogen flowing from the hydrogen injection unit 112. At this time, the volume of the internal space of the measuring vessel 114, is formed in the size of 29 times to 31 times the volume of the internal space of the reaction unit 116, it is formed of approximately 205.9 cm 3 to 226.3 cm 3.

The first valve 115 is disposed between the hydrogen injection valve 113 and the measurement vessel 114 and installed on the main flow passage 111, and the main flow passage between the hydrogen injection portion 112 and the measurement vessel 114. Open and close the 111. A description thereof will be described later.

The reaction part 116 is a place where the sample is inserted, and is disposed between the first valve 115 and the measuring container 114 and connected to the pipe along the line of the main flow path 111, and the internal space of the reaction part 116 is provided. The volume of is formed from approximately 7.1 cm 3 to 7.3 cm 3.

For example, when the ratio of the volume of the internal space of the measuring vessel 114 and the internal space of the reaction unit 116 is formed at a ratio of 29: 1 to 31: 1, hydrogen is absorbed or released into the sample. Although the interval is well represented, it is formed at a ratio of about 30: 1, in which the interval where hydrogen is absorbed or released in the sample is more clearly revealed. Accordingly, the volume of the internal space of the measurement container 114 is about 216 cm 3, and the volume of the internal space of the reaction part 116 is about 7.2 cm 3. Of course, each volume can be made larger and the amount of sample can be increased accordingly, but waste of unnecessary hydrogen gas and safety problems occur when measuring, so that the ratio of the amount of hydrogen absorbed by the sample can be measured relatively quickly and accurately. The volume of the inner space of the measuring vessel 114 is about 216 cm 3, and the volume of the inner space of the reaction part 116 is about 7.2 cm 3. The experimental results are well shown in the graph of FIG. 6, and the description thereof will be described later.

The second valve 117 is installed on the pipe connecting the reaction part 116 and the main flow path 111, that is, between the main flow path 111 and the main flow path 111, that is, the measuring vessel 114 and the reaction part ( 116) open and close. A description thereof will be described later.

The pressure sensor unit 118 is disposed between the first valve 115 and the measuring vessel 114, is installed on the main flow path 111, and the pressure of hydrogen injected into the measuring vessel 114 and the measuring vessel ( The pressure received in the process of moving hydrogen contained in the 114 to the reaction unit 116 is measured, and the measured pressure information is transmitted to the control unit 20. A description thereof will be described later.

The discharge part 119 is connected to the end of the main flow path 111 by a pipe, and discharges hydrogen remaining inside the measuring device 10.

The third valve 120 is installed in a pipe connecting the discharge part 119 and the main flow path 111 to open and close the discharge part 119. Accordingly, the discharge of hydrogen is determined according to the opening and closing of the third valve 120.

The fourth valve 123 is disposed between the measuring vessel 114 and the third valve 120 to be installed on the main flow passage 111 to open and close the main flow passage 111. A description thereof will be described later.

The suction pump 121 is disposed between the third valve 120 and the fourth valve 123 and connected to the main flow path 111, and makes the inside of the measuring device 10 in a vacuum state to measure the measuring device 10. Hydrogen gas and foreign matter remaining in the inside of) is used to remove all by operating the suction pump 121. For example, when there is residual amount of hydrogen gas and foreign matter inside the measuring device 10, the third valve 120 and the fourth valve 123 are closed and the suction pump 121 is operated to operate the third valve. A vacuum is formed between the 120 and the fourth valve 123. In addition, when the third valve 120 and the fourth valve 123 are opened, the remaining amount of hydrogen gas and foreign substances remaining in the measuring device 10 may be sucked and discharged through the outlet. Accordingly, the remaining amount of hydrogen gas and foreign substances remaining in the measuring apparatus 10 are removed, and pure hydrogen is injected only into the measuring apparatus 10 in a vacuum state, thereby reducing the error in the absorption diagram in which the hydrogen is absorbed into the sample. It can be minimized. In addition, the suction pump 121 is also used to recapture hydrogen absorbed by the sample. A description thereof will be described later.

On the other hand, the above-described configuration, divided into the upper space and the lower space by the partition panel 51, is installed in the interior of the housing 50, the door (not shown) formed on the front, the upper space of the housing 50 It is arrange | positioned and is installed in the upper surface of the partition panel 51. This is to be installed inside the housing 50 to minimize the temperature change of the above-described configuration. In this case, the housing 50 may be manufactured in various shapes or sizes. Here, the reaction unit 116 is installed through the partition panel 51 to protrude downward from the partition panel 51, and is detached from the partition panel 51. A description thereof will be described later.

The heat generating unit 30 includes a lifting unit 31 and a heater 32.

The lifting unit 31 is disposed in the lower space of the housing 50, and includes a motor 311, a transfer screw 312, a lifting plate 313, and a lifting check unit 314.

The motor 311 is installed on the bottom bottom of the housing 50, is connected to the transfer screw 312, and rotates the transfer screw 312.

The conveying screw 312 is connected to the axis of the motor 311 (not shown) through the bottom of the housing 50. Accordingly, when the shaft of the motor 311 rotates, the feed screw 312 also rotates together.

The elevating plate 313 is in the form of a substantially rectangular panel, in which two guide rods 315 are vertically installed on both sides of the transfer screw 312 on the bottom surface of the housing 50, respectively. And a guide rod 315. Accordingly, when the transfer screw 312 rotates, the lifting plate 313 is lifted by the guide rod 315.

The heater 32 is a cylindrical shape having a substantially upper opening, and a heating element, that is, a nichrome wire or a planar heating element, which is a heating means, is installed on the upper surface of the elevating plate 313, and is elevated with an elevating play. In addition, in order to maintain the reaction part 116 protruding to the lower part of the partition panel 51 at a set temperature, the reaction part 116 is raised to be accommodated in the heater 32 to be in close contact with the bottom surface of the partition panel 51. . Accordingly, the heater 32 is in close contact with the bottom surface of the partition panel 51 to form a closed space in the interior of the heater 32, and the temperature inside the heater 32 is cut off from the outside so that the inside of the heater 32 is closed. The temperature of the reaction unit 116 accommodated in the can be maintained stably, and by minimizing the temperature change of the reaction unit 116, it is possible to accurately measure the freshness of the hydrogen absorbed or released in the sample.

The elevating checker 314 is spaced apart from the elevating plate 313 and is provided with a pillar 314a, and two check switches 314b for checking the position of the elevating plate 313 at the upper end and the lower end of the pillar 314a. Is installed to check the highest and lowest position that the lifting plate 313 moves. That is, when the feed screw 312 continues to rotate, the lifting plate 313 moves downward while the lifting plate and the bottom of the housing 50 collide, or the lifting plate 313 moves upwards while the heater 32 moves upward. Since it may collide with the partition panel 51, the lifting check unit 314 is installed to prevent this. Accordingly, when the lifting plate 313 is raised and the check switch 314b provided at the upper end of the column 314a is pressed, the control unit 20 receives the signal of the check switch 314b to stop the motor 311. When the lifting plate 313 stops the continuous movement to the upper part and presses the check switch 314b provided at the lower end of the column 314a when the lifting plate 313 is lowered, the control unit 20 performs the above-described method. The motor 311 is stopped to stop the lifting plate 313 from continuously moving downward.

The control unit 20 controls the opening and closing of all the above-described valves and the operation of the suction pump 121, receives pressure information from the pressure sensor unit 118, calculates the absorption rate at which hydrogen is absorbed into the sample, and also checks the switch. A signal is received from 314b to control the operation of the motor 311.

Here, the present invention is connected to the control unit 20 to easily check the hydrogen absorption rate and the operation of the measuring device 10 calculated by the control unit 20, the operation of the measuring device 10 and calculated by the control unit 20 The display 40 may further include a display 40 to show the corrected value. Accordingly, the user can easily check the operation of the measuring apparatus 10 and the value calculated by the controller 20 through the display 40.

On the other hand, in order to easily adjust the pressure of the measuring vessel 114, two manual valves 122 between the hydrogen injection valve 113 and the first valve 115 and the measuring vessel 114 and the fourth valve 123 And disposed between the main passages 111 and the main passage 111. This, while the hydrogen absorption rate is measured, hydrogen may be additionally injected into the measuring vessel 114. If the injection pressure is too high, hydrogen may be excessively injected, so that the diameter of the main flow passage 111 is reduced to reduce the pressure at which hydrogen is injected. By adjusting the amount of hydrogen input. Therefore, by adjusting the hydrogen input amount by operating the manual valve 122, the hydrogen absorption rate can be measured more accurately.

In addition, a temperature sensor unit (not shown) may be further installed inside the housing 50 and around the heater 32 or the reaction unit 116. Accordingly, the control unit 20 may receive information from the temperature sensor unit to maintain the temperature of the reaction unit 116 at the set temperature, and may also suppress the fire by injecting nitrogen when a fire occurs due to overheating.

Hereinafter, the operating state of the pressure-composition isotherm (PCT curve) measuring system of the hydrogen storage alloy according to the exemplary embodiment of the present invention will be described in detail with reference to FIGS. 2 and 4 to 7.

In the initial state, all the valves are kept closed, and the inner diameter of the main flow path 111 is adjusted by the manual valve 122 to adjust the amount of hydrogen introduced.

After the adjustment of the manual valve 122 is completed, the reaction unit 116 is separated from the partition panel 51, the sample is placed inside the reaction unit 116, and the reaction unit 116 is coupled to the partition panel 51. . At this time, the reaction unit 116 may be screwed to the partition panel 51 to prevent hydrogen from leaking between the reaction unit 116 and the partition panel 51. Accordingly, the reaction part 116 and the partition panel 51 are tightly sealed.

After the installation of the reaction unit 116, the control unit 20 rotates the transfer screw 312 by operating the motor 311. When the feed screw 312 rotates, the lifting plate 313 and the heater 32 are raised.

The heater 32 is in close contact with the partition panel 51 and the lifting plate 313 presses the check switch 314b provided at the upper end of the column 314a. The control unit 20 receives a signal from the check switch 314b to stop the operation of the motor 311 and stops the lifting plate 313 from rising.

When the heater 32 is in close contact with the partition panel 51, the control unit 20 operates the heater 32 to heat the reaction unit 116 such that the reaction unit 116 is at a set temperature. At this time, the control unit 20 controls the heater 32 in real time so that the temperature of the reaction unit 116 maintains the set temperature.

When the temperature of the reaction unit 116 maintains the set temperature, the hydrogen injection valve 113 and the first valve 115 are opened to inject hydrogen into the measuring vessel 114. At this time, the pressure sensor unit 118 detects the pressure at which hydrogen is injected in real time, the control unit 20 receives the pressure information detected from the pressure sensor unit 118 and when the pressure information is equal to the set pressure hydrogen injection The valve 113 and the first valve 115 are closed to block hydrogen from being injected into the measuring vessel 114. Then, the second valve 117 is opened to inject hydrogen contained in the measuring vessel 114 into the reaction unit 116.

When the second valve 117 is opened, since the pressure of the measuring vessel 114 is higher than the reaction portion 116, the hydrogen contained in the measuring vessel 114 moves to the reaction portion 116, and as time passes, the measuring vessel The pressure of 114 and the reaction section 116 attempt to equilibrate. At this time, a portion of the hydrogen is absorbed by the sample, the rate of absorption of the hydrogen varies depending on the pressure of the hydrogen injected into the reaction unit 116.

On the other hand, in order to recover the hydrogen absorbed in the sample, the fourth valve 123 in a state in which the first valve 115, the second valve 117 and the fourth valve 123 is closed while the hydrogen is absorbed in the sample. After opening, the suction pump 121 is operated to suck hydrogen stored in the measuring vessel 114 to form the internal pressure of the measuring vessel 114 at a set pressure lower than the internal pressure of the reaction unit 116.

When the internal pressure of the measuring vessel 114 reaches the set pressure, the fourth valve 123 is closed, the operation of the suction pump 121 is stopped, and the second valve 117 is opened. In this process, since the internal pressure of the measuring vessel 114 is lower than the internal pressure of the reaction unit 116, the recapture of hydrogen absorbed by the sample is started.

For example, as illustrated in FIG. 7, the absorption volume of hydrogen to the sample is formed by using the reaction portion 116 having an internal volume of about 214 cm 3 and an internal volume of about 9.6 cm 3. As a result of measuring the release rate, it can be seen that the pressure gradually rises after the pressure rises rapidly in the initial state. At this time, the number of points shown in the graph indicates the number of experiments, the square black dots indicate that the hydrogen is absorbed in the sample, and the rhombus dots indicate the recapture of hydrogen absorbed in the sample. However, it is not possible to determine in which section of the graph the hydrogen is absorbed or released from the sample. This is a very small amount of hydrogen absorbed by the sample. When the internal volume of the reaction unit 116 is large, the difference in pressure is small compared to the amount of hydrogen absorbed by the sample, so that it is difficult to distinguish in which section hydrogen is absorbed or released. It is impossible to know whether hydrogen is being absorbed into the sample or no longer being absorbed or released.

In order to solve this problem, the internal volume of the reaction part 116 is manufactured in various sizes until the reaction section in which the effort is absorbed or released in the sample is clearly observed, and as a result, the internal volume of the reaction part 116 is In the ratio of about 1/31 to about 1/29 based on the internal volume of the measuring vessel 114, a section in which hydrogen is absorbed in the sample was clearly seen.

As shown in FIG. 6, a measuring vessel 114 having an inner volume of about 216 cm 3 is used, and an inner volume of the reaction unit 116 is about 1/30 of the inner volume of the measuring vessel 114, that is, When using the reaction portion 116 having an internal volume of about 7.2 cm 3, the freshness of hydrogen absorbed or released in the sample is most pronounced.

If the capacity of the measuring vessel 114 and the reaction unit 116 is large, it takes a long time to measure the hydrogen absorption or emission diagram, so that it takes a long time to receive the result, and also wastes hydrogen gas and costs This has a lot of drawbacks.

However, the present invention forms an internal volume of the measuring vessel 114 and an internal volume of the reaction portion 116 in a ratio of about 30: 1, that is, about 216 cm 3: 7.2 cm 3, thereby reducing hydrogen absorption or emission curves. Minimize measurement errors and accurately measure the freshness of hydrogen absorbed or released into the sample in a short time.

In addition, since the heater 32 operates automatically, and only the reaction unit 116 containing the sample is desorbed, all the experiments are automatically made through the control unit 20 when only the sample is replaced. Emission lead rates can be measured. In addition, it is possible to easily remove the foreign matter in the device by installing the suction pump 121, and if the device is overheated or a fire occurs in the device, the control unit 20 checks this to inject nitrogen to prevent the device from overheating Or extinguish a fire.

In describing the present invention described above, even if the embodiment is different, the same reference numerals are used for the same configuration, and the description may be omitted as necessary.

While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it is to be understood that the invention is not limited to the disclosed exemplary embodiments. Shall not be construed as being understood. Therefore, a person having ordinary knowledge in the technical field to which the present invention pertains may easily implement other forms of the present invention within the same scope as the above-described embodiments, or the present invention only by the description of the embodiments of the present invention. It will be possible to practice the invention in the same and equal range.

10; Measuring device
111; Maine Euro
112; Hydrogen injection part
113; Hydrogen injection valve
114; Measuring vessel
115; 1st valve
116; Reaction part
117; 2nd valve
118; Pressure sensor
119; Discharge
120; 3rd valve
121; Suction pump
122; Manual Valve
123; 4th valve
124; Nitrogen injection part
125; Nitrogen injection valve
20; Control
30; Fever
31; Lift
32; heater
311; motor
312; Feed screw
313; Lifting plate
314; Lift check unit
314a; Pillar
314b; Check switch
315; Guide rod
40; display
50; housing
51; Compartment panel

Claims (5)

A hydrogen injection unit into which hydrogen is injected from the outside;
A measuring vessel connected with the hydrogen injection unit to store the hydrogen;
A first valve for opening and closing between the hydrogen injection unit and the measurement container;
A reaction unit into which a sample is inserted to react with the hydrogen by receiving hydrogen stored in the measuring container;
A second valve for opening and closing between the measuring container and the reaction part;
A pressure sensor unit measuring a pressure of the measuring container and a pressure between the measuring container and the reaction part;
A discharge part through which the hydrogen is discharged;
A third valve for opening and closing the discharge part; And
And a control unit controlling opening and closing of the first to third valves and receiving pressure information of the pressure sensor unit.
Hydrogen is injected into the measuring vessel at a set pressure, the first to third valves are closed, and the second valve is opened to measure the pressure between the measuring vessel and the reaction unit to react the pressure according to the pressure change. And a control unit calculates an absorption rate at which hydrogen is absorbed into the sample inserted into the unit. The pressure-composition isotherm (PCT curve) of the hydrogen storage alloy is characterized in that it is.
The method of claim 1,
Hydrogen, characterized in that the volume of the internal space of the measuring vessel is formed 29 to 31 times the volume of the internal space of the reaction unit so that the section of the hydrogen is absorbed in the sample clearly according to the pressure change. Measurement system of pressure-composition isotherms (PCT curves) of storage alloys.
The method of claim 2,
Pressure-composition isotherm (PCT curve) of the hydrogen storage alloy, characterized in that the volume of the inner space of the measuring vessel is formed from 205.9 cm 3 to 226.3 cm 3, and the volume of the inner space of the reaction part is formed from 7.1 cm 3 to 7.3 cm 3. Measuring system.
The method of claim 1,
And a heating unit having a heater for maintaining a constant temperature of the reaction unit and a lifting unit for elevating the heater, wherein the temperature flow unit is controlled by the control unit. Isothermal (PCT Curve) Measurement System.
The method of claim 1,
In order to remove the injected hydrogen or to recapture the hydrogen absorbed in the sample, the suction pump is connected between the measuring vessel and the third valve; pressure-forming isotherm of the hydrogen storage alloy further comprising: PCT curve) measurement system.

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