WO2011135709A1

WO2011135709A1 - Catalyst for hydrogen production

Info

Publication number: WO2011135709A1
Application number: PCT/JP2010/057653
Authority: WO
Inventors: 忠彦水野
Original assignee: エナジー・イノベーション・ワールド・リミテッド
Priority date: 2010-04-30
Filing date: 2010-04-30
Publication date: 2011-11-03
Also published as: JP4659923B1; JPWO2011135709A1

Abstract

Disclosed is a catalyst for hydrogen production, a small amount of which is capable of decomposing water and thereby producing hydrogen continuously for a long time. Specifically disclosed is a catalyst for hydrogen production, which produces hydrogen by coming into contact with water in a non-oxidizing atmosphere at a temperature of 300˚C or more and decomposing the water. The catalyst for hydrogen production comprises a pair of metals that are selected from among combinations of Ni and one metal selected from the group consisting of Pt, Pd and Cr and a combination of Cr and Pd, and an alkali that is capable of maintaining the surface activity of the metals. The catalyst (3) for hydrogen production is arranged in a reaction container (2), and the catalyst (3) for hydrogen production is brought into contact with water in a non-oxidizing atmosphere at a temperature within the range of 300-650˚C, thereby decomposing the water and producing hydrogen.

Description

Catalyst for hydrogen generation

The present invention relates to a hydrogen generation catalyst.

Currently, the use of hydrogen is rapidly expanding to gas power generation equipment, hydrogen gas automobiles, fuel cells, chemical reaction equipment, etc., and demand is also growing significantly.

Conventionally, as a catalyst for decomposing water to generate hydrogen, a catalyst for generating hydrogen using an oxidation-reduction reaction of iron is known. Examples of the conventional hydrogen generation catalyst include, for example, iron or its oxide, Rh, Ir, Ru, Pd, Pt, Os, Ti, Zr, V, Nb, Cr, Mo, Al, Ga, Mg, Sc, The thing which added one metal selected from the group which consists of Ni and Cu is proposed (refer patent document 1).

The conventional hydrogen generation catalyst generates hydrogen by reducing water when iron is oxidized. Here, one metal selected from the group consisting of Rh, Ir, Ru, Pd, Pt, Os, Ti, Zr, V, Nb, Cr, Mo, Al, Ga, Mg, Sc, Ni, Cu is It is thought to act as a cocatalyst. The conventional hydrogen generation catalyst can be regenerated by separately reducing iron oxide generated as a result of water reduction to iron.

International Publication WO2004 / 002881

However, in the conventional hydrogen generation catalyst, the catalytic activity is lost when iron is oxidized to iron oxide, so a large amount of catalyst is required to continuously generate hydrogen over a long period of time. There is an inconvenience.

An object of the present invention is to provide a hydrogen generation catalyst capable of solving such disadvantages and generating hydrogen by decomposing water continuously for a long time with a small amount of catalyst.

In order to achieve this object, the hydrogen generation catalyst of the present invention is a hydrogen generator that generates hydrogen by decomposing water by contacting it with water at a temperature of 300 ° C. or higher in a non-oxidizing atmosphere. A catalyst for use in which Ni is combined with one metal selected from the group consisting of Pt, Pd, and Cr, or a pair of metals selected from a combination of Cr and Pd, and the surface activity of the metal. And an alkali that can be maintained.

The catalyst for hydrogen generation of the present invention generates hydrogen by decomposing water by contact with water in a non-oxygen atmosphere reaction vessel. This is because when hydrogen is generated in an oxygen atmosphere, the generated hydrogen reacts with oxygen and is lost.

Also, the hydrogen generation catalyst of the present invention must be brought into contact with water at a temperature of 300 ° C. or higher in the reaction vessel. At a temperature lower than 300 ° C., the activity of decomposing water cannot be imparted to the pair of metals. The temperature at which the hydrogen generation catalyst of the present invention is brought into contact with water is more advantageous as it is higher if it is 300 ° C or higher. However, a normal reaction vessel made of stainless steel or the like is corroded at a temperature exceeding 650 ° C. unless measures such as providing a coating layer made of platinum are taken. Therefore, practically, the temperature is preferably in the range of 300 to 650 ° C.

The hydrogen generation catalyst of the present invention is a combination of Ni and one metal selected from the group consisting of Pt, Pd, and Cr, or a pair of metals selected from a combination of Cr and Pd together with an alkali. By doing so, the activity of decomposing water on the surface of the metal can be maintained. As a result, the hydrogen generation catalyst of the present invention can generate hydrogen by decomposing water over a long period of time with a small amount of catalyst.

At this time, the alkali becomes an aqueous solution by contact with water, so that the activity of the metal surface can be maintained without hindering the contact between the metal surface and water.

In the hydrogen generation catalyst of the present invention, the alkali is a substance that exhibits alkalinity when it becomes an aqueous solution, and any substance can be used as long as it can maintain the activity of decomposing water on the surface of the metal. It may be. As the alkali, for example, one compound selected from the group consisting of LiOH, KOH, and NaOH can be used. However, KOH or NaOH is preferably used, and NaOH is more preferably used from the viewpoint of cost. be able to.

In the hydrogen generation catalyst of the present invention, it is preferable that the pair of metals includes 1 to 10 parts by weight of the other metal with respect to 1 part by weight of any one of the metals. If the other metal is less than 1 part by weight relative to 1 part by weight of any one of the metals, sufficient catalytic activity may not be obtained, and if it exceeds 10 parts by weight, no further effect will be obtained.

In the hydrogen generation catalyst of the present invention, the pair of metals and the alkali may be in any form as long as they coexist, for example, the powder of the pair of metals is sintered. It can be set as the form with which the said alkali was filled in the hole of the porous body. By making the catalyst for hydrogen generation of the present invention porous, the specific surface area of the metal can be increased. At this time, since the alkali is filled in the pores of the porous body, the activity of the surface of the metal forming the porous body can be maintained.

When the hydrogen generation catalyst of the present invention comprises the porous body, the step of mixing the pair of metals and then dissolving them to obtain a metal mixture, the step of pulverizing the metal mixture to obtain a powder, Produced advantageously by a production method comprising a step of molding a powder to obtain a molded body, a step of sintering the molded body to obtain a porous body, and a step of impregnating the pores of the porous body with alkali. can do.

In the manufacturing method, the molded body can be molded, for example, by filling the powder in a predetermined shape container and pressurizing it. The sintered compact can be sintered at a temperature in the range of 1200 to 1500 ° C., for example.

In the production method, the impregnation with the alkali is preferably performed by placing the alkali on the porous body and heating to a temperature equal to or higher than the melting point of the alkali. If it does in this way, the said alkali which was heated and heated to the temperature more than melting | fusing point will impregnate the hole of the said porous body.

In the method for producing hydrogen according to the present invention, a pair of Ni selected from a combination of Ni and one metal selected from the group consisting of Pt, Pd, and Cr or a combination of Cr and Pd in the reaction vessel. And a hydrogen generating catalyst comprising an alkali capable of maintaining the surface activity of the metal, and contacting the hydrogen generating catalyst with water at a temperature of 300 ° C. or higher in a non-oxidizing atmosphere. In this way, water is decomposed to generate hydrogen.

The method for producing hydrogen of the present invention comprises a reaction vessel containing the hydrogen production catalyst of the present invention, a heating means for heating the inside of the reaction vessel to a temperature of 300 ° C. or higher, and a non-oxidizing atmosphere in the reaction vessel. Atmosphere adjusting means, water supply means for supplying water into the reaction vessel and bringing the hydrogen generation catalyst into contact with water, and a mixed gas containing hydrogen generated by the decomposition of the water is taken out from the reaction vessel The present invention can be implemented by a hydrogen production apparatus comprising a mixed gas extraction means and a hydrogen separation means for separating and extracting hydrogen from the mixed gas extracted by the mixed gas extraction means.

In the hydrogen production apparatus of the present invention, the inside of the reaction vessel is heated to a temperature of 300 ° C. or higher by the heating means, and a non-oxidizing atmosphere is set by the atmosphere adjusting means. Then, by supplying water into the reaction vessel by the water supply means at a temperature of 300 ° C. or higher in a non-oxidizing atmosphere and bringing the hydrogen generating catalyst into contact with water, the water is decomposed to generate hydrogen. Can be made.

At this time, the hydrogen produced by the decomposition of the water is taken out by the mixed gas take-out means as a mixed gas with water vapor or the like. Therefore, only hydrogen can be taken out by separating hydrogen from the mixed gas by the hydrogen separation means.

Explanatory sectional drawing which shows one structural example of the reaction container used for manufacture of the catalyst for hydrogen production of this invention. BRIEF DESCRIPTION OF THE DRAWINGS Explanatory sectional drawing which shows one structural example of the hydrogen production apparatus using the catalyst for hydrogen production of this invention. The graph which shows the time-dependent change of the hydrogen generation amount in one Example of hydrogen production using the catalyst for hydrogen production of this invention. The graph which shows the mass spectrometry result of the production | generation gas after progress for 4000 second from the reaction start in the Example shown in FIG.

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

The hydrogen generating catalyst of the present embodiment generates hydrogen by decomposing water by contact with water at a temperature of 300 ° C. or higher, preferably 300 to 650 ° C. in a non-oxidizing atmosphere. The non-oxidizing atmosphere may be an inert atmosphere such as argon or nitrogen or a reducing atmosphere such as hydrogen as long as it does not contain oxygen. Alternatively, the non-oxidizing atmosphere may be obtained by reducing the pressure in the reaction vessel to a pressure in the range of 3 to 10 mmHg.

The hydrogen generation catalyst of the present embodiment is a combination of Ni and one metal selected from the group consisting of Pt, Pd and Cr, or a pair of metal powders selected from a combination of Cr and Pd. The porous body formed by bonding and an alkali that can be filled in the pores of the porous body and maintain the surface activity of the metal. Specifically, the pair of metals is four kinds of combinations of Ni—Pt, Ni—Pd, Ni—Cr, and Cr—Pd.

When the surface activity of the pair of metals is maintained by the alkali, hydrogen can be generated by decomposing water by contact with water for a long time in a small amount. In the present embodiment, NaOH is used as the alkali. However, the alkali may be any one as long as the activity of the surface of the pair of metals can be maintained.

Next, a method for producing the hydrogen generation catalyst of this embodiment will be described.

First, with respect to 1 part by weight of one of the pair of metals, the other metal is weighed so as to be 1 to 10 parts by weight and mixed. Each of the pair of metals can be used in the form of a powder made of metal particles having a particle diameter of about several millimeters, for example.

Next, the mixture of the pair of metals is dissolved. The melting may be performed simply by heating or arc melting. In the case of performing the arc melting, for example, a vacuum arc melting furnace is used, and melting is performed by DC arc discharge of 300 A under an argon gas atmosphere at a pressure of 1 × 10 ⁻² Pa. For example, a disk-shaped (button-shaped) metal mixture is formed by the dissolution.

Next, the disk-shaped metal mixture is pulverized to form a metal mixture powder having a particle size in the range of 10 to 25 μm, for example.

Next, the powder of the metal mixture is filled in a container having a predetermined shape, and is molded by applying a pressure of 2 to 10 t, for example, to form a molded body having a predetermined shape. The said molded object can be made into a disk shape, for example.

Next, the molded body is sintered to form a porous body made of the metal mixture. The sintering is performed, for example, by using a vacuum electric furnace and holding at a temperature in the range of 1200 to 1500 ° C. for 24 hours.

Next, NaOH as the alkali is filled in the pores of the porous body. The alkali can be filled, for example, by arranging the porous body 200 in the reaction vessel 100 shown in FIG. The reaction vessel 100 is a bottomed cylindrical body made of stainless steel, and includes an openable / closable lid 101 at an upper opening. The outer surface side of the reaction vessel 100 is covered with a heater 102, and the heater 102 is electrically connected to a temperature regulator 103 provided outside.

In filling the alkali, the porous body 200 is arranged several cm above the bottom inner surface 100 a of the reaction vessel 100, and the alkali 104 is placed on the porous body 200. The amount of the alkali 104 is, for example, 1 to 5 parts by weight with respect to 1 part by weight of the porous body 200.

Next, the opening of the reaction vessel 100 is closed with the lid 101, and the inside of the reaction vessel 100 is heated to a temperature in the range of 300 to 650 ° C. with the heater 102. By doing so, the alkali 104 is melted and liquid alkali 104 is impregnated into the pores of the porous body 200, thereby filling the pores.

As a result, it is possible to obtain a hydrogen generation catalyst in which the pores of the porous body 200 made of the pair of metal mixtures are filled with the alkali 104.

Next, a hydrogen production method using the hydrogen production catalyst of the present embodiment and a hydrogen production apparatus used in the hydrogen production method will be described.

The hydrogen production method of the present embodiment generates hydrogen using the hydrogen production apparatus 1 shown in FIG. A hydrogen production apparatus 1 includes a reaction vessel 2 having a bottomed cylindrical body. The reaction vessel 2 is provided with a hydrogen generation catalyst 3 therein, and is provided with an openable / closable lid 4 at an upper opening. The side is covered with a heater 5. The heater 5 is electrically connected to a temperature regulator 6 provided outside.

A distilled water supply pipe 7 for supplying water vapor to the inside of the reaction vessel 2 is connected to the lid 4 via a valve 8. The distilled water supply pipe 7 has one end opening inside the reaction vessel 2 and the other end connected to the distilled water conduit 9. The distilled water conduit 9 is connected to a distilled water tank 10 and includes a pump 11 that supplies distilled water stored in the distilled water tank 10 to the distilled water supply pipe 7 on the way.

The lid 4 is connected to a sampling tube 12 that collects the gas inside the reaction vessel 2 as a sample via a valve 13, and a mass spectrometer 14 is connected to the end of the sampling tube 12. .

Furthermore, a gas extraction pipe 15 for taking out the gas inside the reaction vessel 2 is connected to the lid 4 via a valve 16. The end of the gas extraction pipe 15 is connected to a gas conduit 18 via a gas flow rate measuring device 17, and the gas conduit 18 is connected to a hydrogen separator 20 via a valve 19.

The hydrogen separator 20 includes a hydrogen separation membrane 21 inside, an exhaust pipe 22 is connected to the primary side of the hydrogen separation membrane 21 via a valve 23, and a hydrogen side is connected to the secondary side of the hydrogen separation membrane 21. An extraction pipe 24 is connected via a valve 25. A suction unit (not shown) is connected to the end of the exhaust pipe 22 so that the inside of the reaction vessel 2 can be depressurized. Further, as shown in FIG. 2B, the hydrogen take-out pipe 24 is provided with a backfire prevention device 26 in the pipe between the hydrogen separator 20 and the valve 25 as shown in FIG.

When generating hydrogen in the hydrogen production apparatus 1, first, a hydrogen generation catalyst 3 is disposed inside the reaction vessel 2. At this time, the reaction vessel 100 shown in FIG. By using the reaction vessel 100 shown in FIG. 1 as the reaction vessel 2 shown in FIG. 2A, the hydrogen generation catalyst 3 prepared by filling the pores of the porous body 200 with the alkali 104 is used as it is. Can be used for generation.

Next, the reaction vessel 2 is closed with the lid 4, the

valves

8, 13, 25 are closed, and the

valves

16, 19, 23 are opened, and an aspirator (not shown) connected to the end of the exhaust pipe 22. The pressure inside the reaction vessel 2 is reduced to a pressure in the range of 3 to 10 mmHg. Next, with the

valves

8, 13, 16, 19, 23, and 25 closed, the heater 5 is controlled by the temperature regulator 6 to heat the inside of the reaction vessel 2 to a temperature in the range of 300 to 650 ° C. The temperature rises to

If the temperature inside the reaction vessel 2 is raised to a temperature within the above range, the pump 11 is then operated with the valve 8 opened, and the distilled water stored in the distilled water tank 10 is converted into the distilled water conduit. 9 and the distilled water supply pipe 7 are supplied into the reaction vessel 2. If it does in this way, since the inside of the reaction container 2 is heated up to the temperature of the said range, the supplied distilled water will immediately vaporize and become water vapor | steam, and water vapor will fill the inside of the reaction container 2. FIG.

Then, the steam is directly pyrolyzed on the surface of the pair of metals forming the hydrogen generation catalyst 3 to generate hydrogen. At this time, the alkali acts to maintain the surface activity of the pair of metals. Since the alkali forms an aqueous solution with the water vapor, the alkali does not hinder the contact between the surface of the pair of metals and the water vapor (water).

The hydrogen and oxygen generated inside the reaction vessel 2 form a mixed gas together with unreacted water vapor, and are guided to the hydrogen separator 20 through the gas extraction pipe 15 and the gas conduit 18. Then, a high concentration of hydrogen is separated by the hydrogen separation membrane 21 disposed inside the hydrogen separator 20, and the separated hydrogen can be taken out from the hydrogen extraction conduit 24.

Next, examples of the present invention will be described.

In this example, first, 10 g of Ni was weighed and mixed with 5 g of Cr. The obtained mixture was put into a water-cooled copper crucible in a small vacuum arc melting furnace (manufactured by Daia Vacuum Co., Ltd., trade name: ACM-C01), and under an argon gas atmosphere at a pressure of 1 × 10 ⁻² Pa. , 300 A DC arc discharge to form a disk-like metal mixture. The metal mixture was pulverized using a pulverizer (trade name: ANM1000, manufactured by Nippon Ceramic Science Co., Ltd.) to form a metal mixture powder having a particle size in the range of 10 to 25 μm.

Next, the powder is put into a stainless steel circular container and molded using a molding machine (manufactured by ASONE Co., Ltd., trade name: High Pressure Jack J-15) by applying a pressure of 10 tons from above and below. A molded body was formed. By forming the formed body in a vacuum electric furnace (trade name: ADP-21, manufactured by Yamato Kagaku Co., Ltd.), holding it at a temperature of 1200 ° C. for 24 hours under a pressure of 0.4 kPa, and sintering it, A disk-shaped porous body was formed.

Next, the porous body 200 obtained in this example was placed inside the reaction vessel 100 shown in FIG. 1, and 40 g of solid NaOH as an alkali was placed on the porous body 200. Next, the opening of the reaction vessel 100 was closed with a lid 101, and the inside of the reaction vessel 100 was heated to a temperature of 450 ° C. with a heater 102. Further, the inside of the reaction vessel 100 was heated to a temperature of 750 ° C. and held at the temperature for 24 hours, and then the heating was stopped, and then allowed to cool to room temperature over 24 hours. As a result, molten NaOH was impregnated into the pores of the porous body 200 to obtain a hydrogen generation catalyst filled in the pores.

Next, the hydrogen generation catalyst 3 obtained in this example was placed in the reaction vessel 2 of the hydrogen production apparatus 1 shown in FIG. Next, the opening of the reaction vessel 2 is closed with the lid 4, the

valves

8, 13, 25 are closed, and the other valves are opened, with a suction device (not shown) connected to the end of the exhaust pipe 22. The inside of the reaction vessel 2 was evacuated and reduced to a pressure of 3 to 10 mmHg to make a non-oxidizing atmosphere, and then the valve 16 was closed. Next, the inside of the reaction vessel 2 was heated by the heater 5 and the temperature was raised to 570 ° C.

Next, the

valves

8, 16, 19, 23, and 25 are opened, the pump 11 is operated, and the distilled water stored in the distilled water tank 10 is supplied to the reaction vessel via the distilled water conduit 9 and the distilled water supply pipe 7. 2 was fed inside. As a result, the supplied distilled water was immediately vaporized to become water vapor, and the water vapor was filled inside the reaction vessel 2, and generation of gas was started inside the reaction vessel 2.

At this time, the gas generation amount measured by the gas flow rate measuring device 17 is shown in FIG. In addition, when 3600 seconds have elapsed from the start of the reaction, the valve 13 is opened and the gas inside the reaction vessel 2 is collected through the sampling tube 12, and the Canon Anelva Stock Mass spectrometry was performed using a company-made mass spectrometer (trade name: MSQ 400). The result is shown in FIG.

From FIG. 4, it is clear that about 99 mass% of the gas produced | generated inside the reaction container 2 is hydrogen. Further, from FIG. 3, in the inside of the reaction vessel 2, 0.12 ml / cm ² / sec per unit area of the hydrogen generating catalyst 3 continuously over 150,000 seconds (about 42 hours) from the start of the reaction. It is clear that hydrogen is generated at the hydrogen generation rate.

In this embodiment, the case where the pair of metals is a combination of Cr and Ni is described. However, the pair of metals may be a combination of Ni and Pt or Pd. And a combination of Pd may be used.

Next, a unit of hydrogen generating catalyst 3 at a temperature of 500 ° C. when a combination of Ni and Pt or Pd or a combination of Cr and Pd is used as the pair of metals and NaOH is used as the alkali. The hydrogen generation rate per area (ml / cm ² / sec) is shown in Table 1.

From Table 1, even when a combination of Ni and Pt or Pd or a combination of Cr and Pd is used as the pair of metals, hydrogen can be generated in the same manner as the combination of Ni and Cr. it is obvious.

In addition, although the present Example demonstrates the case where NaOH is used as an alkali, the said alkali may be other alkalis, such as LiOH and KOH.

DESCRIPTION OF SYMBOLS 1 ... Hydrogen production apparatus, 2 ... Reaction container, 3 ... Catalyst for hydrogen production, 5 ... Heater, 10 ... Distilled water tank, 14 ... Mass spectrometer, 20 ... Hydrogen separator.

Claims

A hydrogen generation catalyst that decomposes water by contacting water at a temperature of 300 ° C. or higher in a non-oxidizing atmosphere in a reaction vessel to generate hydrogen,
A combination of Ni and one metal selected from the group consisting of Pt, Pd, Cr, or a pair of metals selected from a combination of Cr and Pd;
A catalyst for hydrogen generation comprising an alkali capable of maintaining the surface activity of the metal.
2. The hydrogen generation catalyst according to claim 1, wherein hydrogen is decomposed to produce hydrogen by contacting with water at a temperature in a range of 300 to 650 ° C. in a non-oxidizing atmosphere in a reaction vessel. Catalyst for hydrogen generation.
3. The hydrogen generation catalyst according to claim 1, wherein the alkali is one compound selected from the group consisting of LiOH, NaOH and KOH.
4. The hydrogen generation catalyst according to claim 1, wherein the pair of metals includes 1 to 10 parts by weight of the other metal with respect to 1 part by weight of any one of the metals. A hydrogen generation catalyst characterized by the above.
5. The hydrogen generation catalyst according to claim 1, comprising a porous body obtained by sintering the pair of metal powders, wherein the alkali is filled in pores of the porous body. The catalyst for hydrogen production characterized by being made.
A step of mixing a combination of Ni and one metal selected from the group consisting of Pt, Pd, and Cr, or a pair of metals selected from a combination of Cr and Pd, and then dissolving them to obtain a metal mixture; Pulverizing the metal mixture to obtain a powder, forming the powder to obtain a molded body, sintering the molded body to obtain a porous body, and pores of the porous body And a step of impregnating the substrate with an alkali.
7. The method for producing a hydrogen generation catalyst according to claim 6, wherein the pair of metals is mixed in an amount of 1 to 10 parts by weight of the other metal with respect to 1 part by weight of any one of the metals. A method for producing a hydrogen production catalyst.
The method for producing a hydrogen generation catalyst according to claim 6 or 7, wherein the molded body is formed by filling the powder in a predetermined shape container and pressurizing the molded body. Production method.
9. The method for producing a hydrogen generation catalyst according to claim 6, wherein the compact is sintered at a temperature in the range of 1200 to 1500 ° C. Manufacturing method.
10. The method for producing a hydrogen generation catalyst according to claim 6, wherein the alkali impregnation includes placing an alkali on the porous body and heating to a temperature equal to or higher than a melting point of the alkali. A process for producing a hydrogen generation catalyst, characterized in that
In the reaction vessel, a combination of Ni and one metal selected from the group consisting of Pt, Pd, and Cr, or a pair of metals selected from a combination of Cr and Pd, and maintaining the surface activity of the metal A hydrogen generating catalyst comprising an alkali capable of being produced and decomposing water by contacting the hydrogen generating catalyst with water at a temperature of 300 ° C. or higher in a non-oxidizing atmosphere to generate hydrogen. A method for producing hydrogen.
A combination of Ni and one metal selected from the group consisting of Pt, Pd, and Cr, or a pair of metals selected from a combination of Cr and Pd, and an alkali capable of maintaining the surface activity of the metal A reaction vessel containing a hydrogen production catalyst, a heating means for heating the inside of the reaction vessel, an atmosphere adjusting means for making the inside of the reaction vessel a non-oxidizing atmosphere, and supplying water into the reaction vessel Water supply means for bringing the hydrogen generation catalyst into contact with water, a mixed gas extraction means for extracting a mixed gas containing hydrogen generated by the decomposition of the water from the reaction vessel, and the mixed gas extraction means. And a hydrogen separation means for separating and taking out hydrogen from the mixed gas.