法国专利FR3072304A1 DEVICE FOR GENERATING GAS

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专利摘要:
Catalytic device comprising a hollow body, a piston housed in the hollow body, a catalyst for a reaction of generation of a gas by contacting a reactive liquid with the catalyst, the catalyst being housed in a catalyst chamber, the piston and the hollow body defining a hermetic compression chamber for containing a compressible fluid, and being movable relative to each other between a closing position in which the catalyst chamber is sealed to the reactive liquid, and an open position for the entry of the reactant liquid into the catalyst chamber, the catalytic device being in accordance to move from the open position to the closed position, respectively from the closed position to the open position, when the compressible fluid is contained in the compression chamber and a force applied to the piston is superior or equal, respectiveme lower, to a closing force.
公开号:FR3072304A1
申请号:FR1759788
申请日:2017-10-18
公开日:2019-04-19
发明作者:Michael Bouvier；Philippe Capron；Jerome Delmas；Vincent MATHIEU；Isabelle Rougeaux
申请人:Commissariat a lEnergie Atomique CEA；Commissariat a lEnergie Atomique et aux Energies Alternatives CEA；
IPC主号:

专利说明:

The present invention relates mainly to an apparatus for generating a gas, and in particular dihydrogen, by bringing a reactive liquid into contact with a catalyst.
A well-known method for generating dihydrogen consists in bringing an aqueous hydride solution, for example a sodium borohydride solution, into contact with a catalyst for the hydrolysis reaction of the hydride, formed for example of cobalt, platinum, ruthenium, or nickel. On contact with the catalyst, a hydrolysis reaction of the aqueous solution occurs, generating dihydrogen.
By way of illustration, WO 2012/003112 A1 and WO 2010/051557 A1 each describe an apparatus for carrying out such a catalyzed hydrolysis of hydride. The gas generation devices described in these documents each comprise an enclosure containing, in operation, an aqueous hydride solution, and a catalytic device defining a catalysis chamber containing a catalyst for the hydrolysis of the aqueous hydride solution. The catalytic device has a body and a removable cover. In the closed position of the catalytic device, the cover and the body together isolate the catalyst from the aqueous hydride solution. There is then no generation of dihydrogen. In the open position of the catalytic device, the cover is arranged at a distance from the body. The aqueous hydride solution then comes into contact with the catalyst, thus initiating the generation of dihydrogen, which is evacuated outside the enclosure by means of an evacuation valve.
To prevent the pressure of generated hydrogen from being too high inside the enclosure, the catalytic device described in WO 2012/003112 A1 comprises an elastomeric membrane, in the form of a hollow cylindrical tube, fixed to both on the body and on the lid. The body also comprises a drain opening out of the enclosure at one of its ends and into the interior space of the membrane at its opposite end, so that the pressure in the interior space of the membrane is equal to atmospheric pressure. Thus, when the pressure of hydrogen in the enclosure results in a force greater than a closing force, the cover is pushed against the body under the effect of said force, contracting the elastomeric membrane by torsional effect, until the closed position of the catalytic device. When the pressure in the enclosure results in a force less than the closing force, the elastomeric membrane, seeking to return to its equilibrium position, unfolds and releases the cover in the open position of the catalytic device, so as to allow the access of the aqueous hydride solution to the catalyst.
However, in order to ensure optimal contraction and deployment of the elastomeric membrane, it is necessary for the height of the membrane to be low, which limits access to the catalyst of the hydride-based aqueous solution, and limits the dihydrogen production yield.
In addition, the closing force of the catalytic device is determined by the rigidity of the elastomeric membrane which depends on its shape, its dimensions, in particular its thickness, and its mechanical properties, in particular elastic properties. The dimensioning of the elastomeric membrane is therefore complex to ensure efficient hydrolysis.
There is therefore a need for an apparatus useful for generating a gas by bringing a reactive liquid into contact with a catalyst overcoming the aforementioned drawbacks.
To this end, the invention proposes a catalytic device comprising:
- a hollow body,
- a piston housed in the hollow body,
a catalyst for a reaction for generating a gas by bringing a reactive liquid into contact with the catalyst, the catalyst being housed in a catalysis chamber, the piston and the hollow body defining a hermetic compression chamber to contain a compressible fluid, and being movable relative to each other between a closed position in which the catalysis chamber is sealed against the reactive liquid, and an open position for the entry of the reactive liquid into the catalyzes, the catalytic device being shaped to pass from the open position to the closed position, respectively from the closed position to the open position, when the compressible fluid is contained in the compression chamber and that a force applied to the piston is greater than or equal to, respectively, less than a closing force.
The "closing force" corresponds to the minimum force from which the catalytic device is in the closed position.
As will become clear below, the device according to the invention makes it possible to dispense with the taking of a reference pressure, in particular atmospheric, to define the closing force. The manufacturing of the device is thus simplified. Furthermore, the stroke of the piston can easily be adapted to correspond to the needs of gas generation. As will be detailed later, it is thus possible to promote the access of the reactive liquid to the catalysis chamber and to optimize the access of the reactive liquid to the catalyst. It is thus possible to reduce the amount of catalyst compared to a catalytic device of the prior art, while maintaining a yield at least equal, or even higher. Furthermore, as will appear more clearly below, the catalytic device according to the invention can house a catalyst of various shapes, which simplifies the process of shaping the catalyst. Furthermore, the closing force can easily be defined by adapting the volume and / or the pressure of the compressible fluid in the extreme opening position, i.e. in the position where the piston is at the end of its travel. Finally, the catalytic device according to the invention makes it possible to dispense with the implementation of means, such as a pressure sensor and a servo unit, for regulating the pressure within the compression chamber. It can therefore operate independently, without further requiring electrical supply means to move the piston relative to the hollow body.
Furthermore, the invention may include one or more of the following optional features.
The catalyst is preferably suitable for catalyzing the hydrolysis of an aqueous solution comprising a hydride. Preferably, the catalyst comprises more than 95.0%, or even more than 99.0% of a metal chosen from platinum, ruthenium, cobalt, nickel and their alloys.
Preferably, the catalyst is fixed, preferably rigidly, to the piston and / or to the hollow body.
In particular, the catalyst can be placed on a catalysis support, preferably porous, in the form of a block with a thickness greater than 1 mm. The catalysis support can be formed from a ceramic, polymer or preferably metallic material. In particular, the catalyst can be placed in the pores of the catalysis support. Preferably, the percentage by mass of the catalyst, expressed on the basis of the sum of the masses of the catalyst support and mass of the catalyst, is greater than 50.0%.
Alternatively, the catalyst may be in the form of a coating having a thickness of less than 1 mm.
The compressible fluid can be contained in the compression chamber.
Preferably, the compressible fluid is a gas, preferably chosen from a neutral gas and air. Air has the advantage of low cost. A neutral gas is preferred for its inert chemical properties.
The pressure of the compressible fluid in the extreme open position may be equal to or even greater than atmospheric pressure. Preferably, in a variant where the device comprises a stop arranged in such a way that the piston is in abutment against said stop in the extreme open position, in the extreme open position, the pressure of the compressible fluid is greater than 1 , 1 bar, or even preferably greater than 1.2 bar. The "pressure" is defined with reference to the zero vacuum pressure reference.
Preferably, the piston and the hollow body are movable in translation and / or in rotation relative to one another between the open and closed positions. Preferably, the piston is movable in translation relative to the hollow body along a single axis. Preferably, the hollow body is shaped to guide the piston in translation. Preferably, the hollow body comprises a cylindrical and hollow guide barrel shaped to guide the piston in translation /
Preferably, the piston and the hollow body define the catalysis chamber. Thus the catalytic device is easy to manufacture, the catalysis chamber and the compression chamber being defined by the same members.
In one embodiment, the body can be in one piece. Alternatively, the body may include a part and a plug mounted removably on the part.
The body may include a valve configured to purge the compressible fluid from the compression chamber.
The device preferably comprises a stopper arranged so that the piston is in abutment against said stopper in the extreme open position.
In one embodiment, the body may comprise a part having a cylindrical and hollow guide barrel shaped to guide the piston, a storage tank and a fluid connection member connecting said part to the storage tank. For example, the guide barrel can be placed inside the enclosure of a gas generating device and the storage tank can be placed outside said enclosure. Thus, by shifting the volume of compressible fluid out of the enclosure, the volume accessible to the liquid in the enclosure is increased.
The piston preferably has a cover, the cover being supported on the hollow body in the closed position and completely closing the opening, and being arranged at a distance from the hollow body in the open position.
Preferably, in the open position, when the interior space of the enclosure contains the reactive liquid, more than 50%, preferably more than 80%, preferably more than 90%, or even in particular the entire surface of the catalyst. free of contact with the piston and / or with the hollow body is exposed to the reactive liquid.
Preferably, at least part of the catalyst is fixed to the hollow body and / or to the piston.
Preferably, the closing force is greater than the force exerted by the pressure of the compressible fluid on the piston in the extreme opening position.
The invention also relates to an apparatus for generating a gas comprising an enclosure defining an interior space for containing a reactive liquid, and a catalytic device according to the invention, the apparatus being configured so that when the interior space contains the reactive liquid, in the open position of the catalytic device, the catalytic chamber is in fluid communication with the interior space, so that the gas is generated by bringing the reactive liquid into contact with the catalyst, and in the position of closing the catalytic device, the catalyst is isolated from the reactive liquid.
Preferably, the catalytic device is arranged at least partially, or even entirely, in the interior space of the enclosure.
In particular, the body of the catalytic device may comprise a part having a cylindrical and hollow guide barrel shaped to guide the piston, a storage tank and a fluid connection member connecting said part to the storage tank, the storage tank being arranged. outside the interior space of the enclosure.
In one embodiment, when the interior space of the enclosure contains the reactive liquid, the piston is closer to the free surface of the reactive liquid in the closed position than in the open position.
In addition, the device may include at least two catalytic devices.
The invention also relates to a method for dimensioning a device according to the invention in which:
the stroke of the piston is defined between the closed position and the extreme open position by selecting at least one parameter chosen from the closing force, the volume of the compression chamber in the extreme open position, the pressure of the compressible fluid in the extreme opening position and, where appropriate, the diameter of the guide drum, or the closing force is defined by selecting at least one parameter chosen from the volume of the compression chamber in the extreme position d opening, the pressure of the compressible fluid in the extreme open position, the stroke of the piston and, where appropriate, the diameter of the guide barrel.
The extreme opening position can be defined by means of a stopper arranged so that the piston is in abutment against said stopper in the extreme opening position.
The invention further relates to a process for generating a gas by bringing a reactive liquid into contact with a catalyst for the gas generation reaction, the process comprising the following successive steps consisting in:
i) have an apparatus according to the invention in which the interior space of the enclosure contains the reactive liquid, ii) place the catalytic device in the open position, so that the reactive liquid comes into contact with the catalyst.
Preferably, the gas is dihydrogen, the catalyst is suitable for catalyzing the hydrolysis of an aqueous solution comprising a hydride, preferably the catalyst comprises more than 95.0% of a metal chosen from platinum, ruthenium, cobalt, nickel and their alloys, and the reactive liquid is an aqueous solution comprising a hydride.
The invention finally relates to an electric generator comprising:
- a fuel cell to generate an electric current by oxidation of a gas,
- a gas generation device according to the invention, the device being in fluid communication with the fuel cell and being configured to supply the fuel cell with said gas.
Other characteristics, variants and advantages of the invention will emerge more clearly on reading the detailed description and examples which follow, given by way of illustration and not limitation, and on examining the appended drawing, in which:
Figures 1 and 2 show, in section along a longitudinal plane, an example of gas generating apparatus according to the invention, in which the catalytic device is arranged in the open position, respectively in the closed position, Figures 3 to 8 illustrate different variants of the catalytic device according to the invention, and FIGS. 9 and 10 are graphs representing the evolution of the flow rate and the evolution of the pressure in the enclosure of an appliance outside the invention and of an appliance according to the invention respectively, during the implementation of the process for generating dihydrogen using said devices.
In the figures, the scales and proportions of the various organs and units making up the apparatus and the device are not necessarily observed. Furthermore, for the sake of clarity, organs can be represented as not being in contact with each other when they are in practice. Furthermore, different references may designate the same body.
FIG. 1 represents an exemplary embodiment of an apparatus 5 for generating gas according to the invention.
The device comprises an enclosure 10 defining an interior space 15, in which is arranged a catalytic device 20 according to the invention.
In the example illustrated in FIG. 1, the enclosure contains a reactive liquid 25. For example, when the apparatus is intended to generate dihydrogen, the reactive liquid contained in the enclosure is an aqueous hydride solution, comprising for example sodium borohydride and / or potassium borohydride. Furthermore, prior to the generation of gas, the interior space may be free of the reactive liquid.
The enclosure has a side wall 30 which extends in a longitudinal direction X, a bottom wall 35 defining a bottom of the enclosure when the longitudinal direction X is parallel to the direction of gravity and oriented in the opposite direction to the gravity, as illustrated in FIG. 1 and an upper wall 40, having an opening 45 for discharging the gas. As illustrated in Figures 1 and 2, a valve 50 can be arranged in the gas discharge opening.
In the example of FIG. 1, the catalytic device is arranged in the interior space of the enclosure, and is fixed to the bottom of the enclosure. Other provisions of the catalytic device are however possible. For example, the catalytic device can be attached to at least one of the side walls or to the top wall. Furthermore, the catalytic device can be arranged partially outside the interior space, as illustrated in FIG. 7. It can even be disposed completely outside the interior space.
The catalytic device illustrated in FIGS. 1 and 2 comprises a hollow body 55 in which is housed a piston 60. The hollow body and the piston together define a compression chamber 65 to contain a compressible fluid. In the examples of Figures 1 and 2, the chamber contains said compressible fluid 70. In the example of Figures 1 and 2, the hollow body comprises a part 75 having an opening 80 passing through the wall of the part in its thickness and a plug 85 removably mounted on the workpiece. The opening is made on a wall of the part in contact with the bottom of the container, and the bottom of the container has a hole 90 opening out on the opening of the part. In this way, by removing the plug from the part, it is possible to fill the compression chamber with the compressible fluid. In order to ensure a seal against the compressible fluid, the plug is preferably surmounted by a sealing joint sandwiched between the piece and the plug when the plug is mounted on the piece. In a variant not shown, the piston has an opening closed by a removable plug, so as to introduce the compressible fluid into the compression chamber. In another variant, the opening 80 is provided with an inflation valve, for adjusting the pressure of the compressible fluid depending on the application for which the device is intended. For example, according to an alternative embodiment of the catalytic device, the compression chamber is free of compressible fluid, the catalytic system is placed in the closed position, and less than an hour, or even less than 10 minutes, or even less. 5 minutes before the catalytic system is placed in the open position, the compressible fluid is injected into the compression chamber via the inflation valve.
As stated above, the compression chamber is hermetic. Thus, when the compressible fluid is contained in the compression chamber, the leakage of the compressible fluid from said compression chamber is substantially zero.
Furthermore, the hollow body includes a valve 92 disposed in an opening in the wall of the body and in the wall of the enclosure. The valve is configured so that when the pressure in the compression chamber exceeds a critical value, the valve is opened, putting the enclosure in fluid communication with the external environment 94 to the enclosure, which is preferably under pressure atmospheric.
The piston and the hollow body are movable relative to each other, preferably in translation and / or in rotation. Preferably, they are movable in translation along a single axis relative to one another, as illustrated in Figures 1 and 2, between an open position and a closed position. Obviously, as appears clearly on the said figures, the catalytic device can be arranged in several positrons of openings. In particular when the piston has reached its stroke, the device is disposed in the extreme open position.
In the example illustrated in FIGS. 1 and 2, the hollow body comprises a cylindrical and hollow guide barrel 100 of axis Y, preferably of revolution, and the piston comprises a piston head 105, one face of which partially defines the chamber compression. The piston head has a shape of a plate in Figures 1 and 2, but other shapes are possible. Furthermore, in the example of FIGS. 1 and 2, the device is in the extreme open position when the piston head is in contact with a stop 95 disposed on the internal wall of the guide barrel.
The piston head has a section, observed in the normal plane at Tax Y of the guide barrel, of shape complementary to the section of the internal wall of the guide barrel, so as to seal the compression chamber. In order to further improve said seal, the piston head may include an annular seal 108 bearing on the internal wall of the guide barrel.
Furthermore, the piston comprises a shaft 110, coaxial with the guide barrel, rigidly fixed at one of its ends to the piston head, as well as a cover 115, rigidly fixed at its opposite end. A catalyst 118 of the reaction for generating gas by bringing the catalyst into contact with the reactive liquid is disposed on the cover. It is housed in the hollow body in the closed position of the catalytic device.
In the closed position, the cover rests on the hollow body. Thus, as clearly appears in FIG. 2, the piston and the hollow body together define a catalysis chamber 120.
In the example of FIG. 1, the body also comprises a shoulder 125 of which extends an annular portion 128, the end face of which is surmounted by a seal 130, on which the cover 115 rests in the closed position.
The assembly formed by the shoulder and the annular portion defines a receptacle for housing the catalyst in the closed position. The annular portion is cylindrical, preferably of revolution, and can be of axis coincident with the axis Y of the guide barrel. The diameter Da of the annular portion is greater than the diameter Dp of the piston head, the diameters being measured perpendicular to the axis Y of the annular portion. The diameter of the annular portion, greater than that of the guide portion and of the piston head, also makes it possible to define a large volume catalysis chamber, thus promoting the exchange between the reactive liquid and the catalyst in position d 'opening. In an embodiment not shown, the device may have neither the shoulder nor the annular portion and the cover may rest in the closed position directly on the guide barrel, possibly surmounted by a seal. In a variant, the face of the cover opposite the catalysis chamber may be covered with a layer of a flexible polymer, for example silicone or of “epdm” elastomer, to ensure the sealing of the catalytic chamber in the position of closing.
In the example of FIG. 1, the catalyst 118 is placed on a catalysis support 119 fixed on the cover 115. As a variant, it can be placed on the piston. In another variant, it can be placed on the hollow body and / or fixed to the hollow body. In particular, it can be placed on the shoulder 125 and / or on the annular portion 128. In another variant, part of the catalyst can be placed in contact with the hollow body and another part of the catalyst can be placed on the piston. .
As regards the shape of the catalyst, it may be in the form of a coating, of thickness less than 1 mm, for example deposited on the face of the cover, a normal of which is oriented towards the catalysis chamber or on the internal face of the wall of the hollow body, for example on the internal wall of the annular portion 128 or of the shoulder 125. The coating can be deposited chemically or electrochemically or by physical vapor deposition or by chemical deposition in vapor phase.
As detailed above, the catalyst can alternatively be deposited in the pores of a porous catalysis support.
An embodiment of the method according to the invention is detailed below by means of a catalysis device according to the invention, as for example illustrated in FIG. 1.
Prior to the generation of gas, the catalytic device is preferably arranged in the closed configuration. Thus, the generation of gas is prevented, the reactive liquid contained in the enclosure being unable to enter the catalysis chamber. In order to initiate the generation of gas, the device is then placed in the open position.
In a variant, prior to the generation of gas, the catalytic device can be arranged in the opening configuration. The generation of gas is initiated, the gas pressure in the enclosure increases until the resulting force which it exerts on the catalytic device places the catalytic system in the closed position.
In another variant, prior to the generation of gas, the enclosure can comprise the reactive liquid under pressure, and the force exerted by the pressure of the reactive liquid under pressure keeps the catalytic system in the closed position until the gas generation be initiated.
Alternatively, prior to the generation of gas, the catalytic device is disposed in the open position, and the enclosure is free of the reactive liquid. The enclosure may however contain a liquid other than the reactive liquid, for example water, but which in contact with the catalyst does not react to generate a gas. For example, to initiate the gas generation reaction, a salt, especially borohydride, is poured into the interior space to form the reactive liquid by dissolving in water.
Prior to the generation of gas, an initial pressure of reactive liquid prevails in the interior space of the enclosure. The initial pressure is less than or equal to or even equal to the pressure in the compression chamber. In particular, it can be equal to atmospheric pressure.
In the variant where, prior to the generation of gas, the device is in the open position and the pressure of the compressible fluid is greater than the pressure in the enclosure, the compressible fluid exerts a pushing force on the piston so to increase the volume of the compression chamber. Preferably, the catalytic device includes a stop, such as that bearing the reference 95 illustrated in FIG. 1, so as to limit the stroke of the piston in the hollow body and thus define the extreme position of opening.
In the variant where, prior to any generation of gas, the device is in the open position and the pressure in the compression chamber is equal to the pressure in the enclosure, the forces resulting from the effects of the pressures of the compressible fluid and reactive liquid as well as by the weight of the piston compensate each other, defining the extreme open position of the device.
In the open position, the reactive liquid contained in the enclosure can enter the catalysis chamber through the opening defined between the piston and the hollow body. The reactive liquid comes into contact with the catalyst, and the gas is thus generated. The gas is then evacuated by Archimedes pushing effect out of the catalysis chamber towards the interior space of the enclosure as illustrated by the arrow S. The volume of the enclosure accessible to the gas being limited, the pressure of the gas and the pressure of the reactive liquid increase in the enclosure. In particular, as long as the reactive liquid comes into contact with the catalyst, the gas is generated and the gas pressure and the pressure of the reactive liquid increase. The gas contained in the enclosure can also be evacuated through the evacuation valve outside the enclosure.
The pressure in the enclosure being greater than the pressure of the compressible fluid in the compression chamber, the resulting force on the piston displaces the piston which compresses the compressible fluid. The volume of the compression chamber decreases and the pressure of the compressible fluid in the compression chamber increases. The compression movement of the piston takes place until the pressure in the compression chamber is balanced with the pressure in the enclosure. The device can thus be arranged in the intermediate open position between the extreme open position and the closed position. In the example of Figure 2, the pressure in the enclosure is equal to a threshold pressure such that the device is brought into the closed position. In the example of FIGS. 1 and 2, the device is closed by moving the piston by covering the annular portion 128 with the cover 115, closing the catalysis chamber. The generation of gas is then inhibited, the catalysis chamber being sealed against the reactive liquid in the closed position. The reactive liquid contained in the enclosure can no longer enter the catalysis chamber. The device is thus placed in the closed position as soon as the pressure in the enclosure results in a force exerted on the piston greater than or equal to the closing force. In the variant where the catalytic device feeds a fuel cell, the gas generated prior to the closing of the catalytic device still contained in the enclosure is then evacuated from the enclosure through the valve.
Thus, the pressure of the reactive liquid becomes less than or equal to the pressure of the compressible fluid in the compression chamber. The resulting force on the piston is then such that the compressible fluid pushes the piston from the closed position to the open position, or even to the extreme open position. The reactive liquid then comes back into contact with the catalyst and gas generation begins again. The succession of opening / closing cycles continues as long as the contacting of the reactive liquid with the catalyst results in the production of gas.
Furthermore, as has been detailed previously, the dimensioning of the catalytic device can be adapted to the specific constraints linked to the use of the gas generated by means of the catalytic device. For example, when the gas generated is dihydrogen and is intended to supply a fuel cell, the catalytic device can be dimensioned so that the dihydrogen leaving the appliance has a pressure corresponding to that necessary for optimal efficiency of the Fuel cell.
In particular, the stroke of the piston between the closed position and the extreme open position can be defined by selecting at least one parameter chosen from the closing force, the volume of the compression chamber in the extreme position of opening, the pressure of the compressible fluid in the extreme open position and, where appropriate, the diameter of the guide drum. As a variant, the closing force can be defined by selecting at least one parameter chosen from the volume of the compression chamber in the extreme open position, the pressure of the compressible fluid in the extreme open position, the stroke piston and if necessary the diameter of the guide barrel.
Thus, the exposure of the catalyst to the reactive liquid in the open position can be optimized while retaining a compact device, occupying a limited volume within the gas generating apparatus.
For example, Figures 3 and 4 illustrate examples of devices arranged in the extreme open position and configured to reach their closed position for an identical closing force. The catalytic devices of FIGS. 3 and 4 comprise identical hollow bodies and pistons, and differ only in the volume of compressible fluid which they contain in the extreme open position. In particular, the pressure of the compressible fluid in the extreme open position is identical for the two devices. For an identical pressure variation between the extreme opening and closing positions, the stroke Ci of the piston of the catalytic device of FIG. 3 is greater than the stroke C2 of the piston of the catalytic device of FIG. 4. Thus, between the position extreme opening and closed position, the catalytic device of figure 3 favors more the exposure of the catalyst to the reactive liquid compared to the catalytic device of figure 4. The catalytic device illustrated on figure 4 presents however the advantage better compactness than that illustrated in FIG. 3.
Figures 5 and 6 illustrate catalytic devices configured to reach their closed position for an identical closing force. The catalytic device of FIG. 6 differs from the catalytic device of FIG. 5 in that it has a guide barrel of larger diameter. In the extreme open positions, the catalytic devices of Figures 5 and 6 have an identical volume of compressible fluid. Furthermore, the pressure of the compressible fluid in the extreme open position is identical for the two devices. For an identical pressure variation between the extreme opening and closing positions, the stroke C3 of the piston of the catalytic device of FIG. 5 is greater than the stroke C4 of the piston of the device of FIG. 6. Thus, between the extreme position opening and closing position, the catalytic device of figure 5 favors more the exposure of the catalyst to the reactive liquid compared to the catalytic device of figure 6.
The device shown in Figure 7 differs from that illustrated in Figure 1 in that the catalytic device is partially arranged within the enclosure. The catalytic device has a body comprising a part having a hollow cylindrical guide barrel 100 in which is housed the piston, a storage tank 135 and a fluid connection member 140 connecting said part to the storage tank. The fluid connection member can be a flexible pipe as shown in FIG. 7, or a rigid connector. It can be mounted removably, for example screwed on the part or on the enclosure. Alternatively, the fluid connection member and the part define a monolithic assembly. Regarding the storage tank, in the example of Figure 7, it is disposed outside the enclosure. Alternatively, it can be placed in the enclosure. Furthermore, as illustrated in FIG. 7, it may include an opening 145 passing through a wall of the tank in its thickness, on which is mounted a removable tank cap 150. Thus, the compressible fluid can be injected into the compression chamber, for example prior to the generation of gas or during the generation of gas to compensate for any leaks of compressible fluid.
The apparatus illustrated in FIG. 8 differs from the apparatus illustrated in FIG. 1 in that the catalytic device is such that the cover 115 of the piston faces the bottom 35 of the enclosure. In order to allow the piston to move within the enclosure, the catalytic device is kept at a distance from the enclosure by means of a spacer 160 in the form of fixing lugs. When the interior space includes the reactive liquid as illustrated, the piston is located at a greater distance from the free surface 165 of the reactive liquid in the open position of the device than in the closed position. The apparatus illustrated in FIG. 8 has the advantage of allowing the catalyst to be exposed with the reactive liquid when the volume of reactive liquid remaining following the generation of gas is low in the enclosure. It is particularly suitable in the case where the catalytic device has a height greater than the height of the reactive liquid in the enclosure when the interior space of the enclosure is completely filled with reactive liquid, the heights being measured in the direction of the gravity.
Examples
The invention is illustrated by means of the following nonlimiting examples. Comparative example
A generation of gas is carried out by means of an apparatus as illustrated in FIG. 1, in which a catalytic device is arranged in the form of the buoy described in WO 2012/003112. The catalytic device comprises 700 mg of cobalt ruthenium deposited on a metallic and porous catalysis support with a mass of 400 mg and the interior space of the enclosure, with a capacity of 1600 ml, contains 500 g of a solution sodium borohydride. The compression chamber of the catalytic device contains air.
The device is connected to an adjustable flow meter which imposes a set flow of 1000 ml / min.
FIG. 9 illustrates the evolution of the pressure Pg of dihydrogen generated by bringing the hydride solution into contact with the catalyst in the enclosure as well as the evolution of the flow rate Dg of dihydrogen during the generation of gas as a function of the time t for implementing the process for generating dihydrogen.
At to = O, the catalytic device is arranged in the opening configuration. The reactive liquid enters the catalysis chamber and comes into contact with the catalyst. The set flow is immediately reached and the pressure increases in the chamber, until the piston is pushed back to the closed position. The buoy opening and closing cycles of WO 2012/003112 thus take place so that the target flow is maintained throughout the generation of gas, until the pressure reaches 1.1 bar. The pressure of dihydrogen in the enclosure decreases at ti = 110 min. From this moment, the pressure in the enclosure becomes equal to atmospheric pressure. The apparatus of the prior art can no longer produce gas in an amount sufficient to ensure the target flow. A total volume Vi = 1101 of gas is thus produced. Hydrides remain in the aqueous solution, but their low concentration in the solution and the limited accessibility to the catalyst results in a decrease in the flow rate of gas generated, which becomes lower than the set flow rate.
Thus, the yield of the process, defined as the ratio between the total mass of hydrogen generated and the total mass of solution of the process of the prior art is 1.8%.
Example according to the invention
A gas generation test is carried out with the apparatus illustrated in FIG. 1, comprising the same quantities of catalyst and of sodium borohydride solution as in the comparative example.
The catalytic device is dimensioned so that, in the extreme opening position, the air pressure within the compression chamber is equal to 1.25 bar.
FIG. 10 illustrates the evolution of the pressure Pg and flow rate Dg of dihydrogen in the enclosure as a function of the time t of implementation of the process for generating dihydrogen.
At time to = O, the catalytic system is placed in the open position. The generation of gas begins and the set flow rate of generated gas is reached (value of 1000 ml / min) from the first cycle of implementation of the process.
The generation of gas continues in this way until the hydride concentration is too low to maintain the set flow rate (instant ti = l 80 min), as observed in FIG. 10. A total volume V2 = 1801 of dihydrogen is thus produced.
Thus, the dihydrogen yield of the process according to the invention is 3.0%.
As is clear from the present description, the generation of gases, in particular of dihydrogen, by means of an apparatus provided with the device according to the invention can easily be adapted according to the application for which the gas generated is intended. In particular, the pressure range of the gas leaving the appliance can be adjusted by a suitable choice of the stroke of the piston and of the pressure and volume of compressible fluid in the extreme open position. The invention makes it possible to initiate a generation of dihydrogen in an efficient, reliable and safe manner with a high yield.
Of course, the invention is not limited to the embodiments of the apparatus and the device according to the invention as well as to the embodiments of the method described and shown.
In particular, the catalytic device can be placed outside the enclosure of the device. The enclosure may contain a reactive liquid other than an aqueous solution of hydrides and be intended to generate a gas other than dihydrogen, for example oxygen.

权利要求:
Claims (15)
[1" id="c-fr-0001]
1. Catalytic device (20) comprising:
- a hollow body (55),
- a piston (60) housed in the hollow body,
- a catalyst for a reaction for generating a gas by bringing a reactive liquid (25) into contact with the catalyst (118), the catalyst being housed in a catalysis chamber (120), the piston and the body hollow defining a compression chamber (65) hermetic to contain a compressible fluid (70), and being movable relative to each other between a closed position in which the catalysis chamber is impermeable to the reactive liquid, and a open position for the entry of the reactive liquid into the catalysis chamber, the catalytic device being shaped to pass from the open position to the closed position, respectively from the closed position to the open position, when the compressible fluid is contained in the compression chamber and that a force applied to the piston is greater than or equal to, respectively less than, a closing force.
[2" id="c-fr-0002]
2. A catalytic device according to claim 1, in which the catalyst is suitable for catalyzing the hydrolysis of an aqueous solution comprising a hydride, preferably the catalyst comprises more than 95.0% of a metal chosen from platinum, ruthenium, cobalt, nickel and their alloys.
[3" id="c-fr-0003]
3. Catalytic device according to any one of claims 1 and 2, in which the compressible fluid is contained in the compression chamber, the compressible fluid preferably being a gas, preferably chosen from a neutral gas and air.
[4" id="c-fr-0004]
4. Catalytic device according to any one of the preceding claims, in which the body comprises a valve (92) configured to purge the compressible fluid from the compression chamber.
[5" id="c-fr-0005]
5. Catalytic device according to any one of the preceding claims, comprising a stop (95) arranged so that the piston is in abutment against said stop in the extreme open position.
[6" id="c-fr-0006]
6. A catalytic device according to any one of claims 3 to 5, wherein the pressure of the compressible fluid in the extreme open position is equal to or greater than atmospheric pressure.
[7" id="c-fr-0007]
7. Catalytic device according to any one of the preceding claims, in which the catalyst is fixed, preferably rigidly, to the piston and / or to the hollow body.
[8" id="c-fr-0008]
8. A catalytic device according to any one of the preceding claims, in which the catalyst is disposed on a catalysis support, preferably porous, in the form of a block with a thickness greater than 1 mm, or is in the form the shape of a coating having a thickness of less than 1 mm.
[9" id="c-fr-0009]
9. A catalytic device according to the preceding claim, in which the percentage by mass of the catalyst, expressed on the basis of the sum of the mass of the catalyst support and mass of the catalyst, is greater than 50.0%.
[10" id="c-fr-0010]
10. Catalytic device according to any one of the preceding claims, in which the piston includes a cover (115), the cover being in abutment on the hollow body in the closed position and completely closing the catalysis chamber, and being arranged to distance from the hollow body in the open position.
[11" id="c-fr-0011]
11. An apparatus (5) for generating a gas comprising an enclosure (10) defining an interior space (15) for containing a reactive liquid (25), and a catalytic device (20) according to any one of the preceding claims, the apparatus being configured so that when the interior space contains the reactive liquid, in the open position of the catalytic device, the catalytic chamber is in fluid communication with the interior space, so that the gas is generated by bringing the reactive liquid into contact with the catalyst, and in the closed position of the catalytic device, the catalyst is isolated from the reactive liquid.
[12" id="c-fr-0012]
12. Apparatus according to the preceding claim, wherein the catalytic device is disposed at least partially, or even entirely, in the interior space of the enclosure.
[13" id="c-fr-0013]
13. Apparatus according to any one of claims 11 and 12, wherein, when the interior space of the enclosure contains the reactive liquid, the piston is closer to the free surface (165) of the reactive liquid in the closed position than in the open position.
[14" id="c-fr-0014]
14. A process for generating a gas by bringing a reactive liquid into contact with a catalyst for the gas generation reaction, the process comprising the following successive steps consisting in:
iii) have an apparatus according to any one of claims 11 to 13 in which the interior space of the enclosure contains the reactive liquid, iv) place the catalytic device in the open position, so that the liquid reagent comes into contact with the catalyst.
[15" id="c-fr-0015]
15. Method according to the preceding claim, in which:
- the gas is dihydrogen,
the catalyst is suitable for catalyzing the hydrolysis of an aqueous solution comprising a hydride, preferably the catalyst comprises more than 95.0% of a metal chosen from platinum, ruthenium, cobalt, nickel and their alloys , and
- the reactive liquid is an aqueous solution comprising a hydride.

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同族专利:

公开号 | 公开日

JP6831089B2|2021-02-17|

JP2021500220A|2021-01-07|

US11267701B2|2022-03-08|

CN111542491B|2022-02-11|

CN111542491A|2020-08-14|

KR20200054274A|2020-05-19|

EP3697729A1|2020-08-26|

FR3072304B1|2019-11-01|

US20200325016A1|2020-10-15|

KR102287123B1|2021-08-05|

WO2019077024A1|2019-04-25|

引用文献:

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US20080014479A1|2006-06-20|2008-01-17|Lynntech, Inc.|Microcartridge hydrogen generator|

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WO2017164812A1|2016-03-22|2017-09-28|Nanyang Technological University|Hydrogen generator|EP3763669A1|2019-07-11|2021-01-13|Commissariat à l'Energie Atomique et aux Energies Alternatives|Dihydrogen generator|

WO2021023637A1|2019-08-07|2021-02-11|Commissariat A L'energie Atomique Et Aux Energies Alternatives|Reusable dihydrogen generator|

WO2021023636A1|2019-08-07|2021-02-11|Commissariat A L'energie Atomique Et Aux Energies Alternatives|Reusable dihydrogen generator|

WO2021037939A1|2019-08-30|2021-03-04|Safran Electronics & Defense|Device for generating a gas|KR100671281B1|2003-03-28|2007-01-18|템코|Hydrogen gas generator|

RU2008115149A|2005-10-03|2009-11-10|Сосьете Бик |OPTIMIZATION OF HYDROGEN FORMATION EFFICIENCY IN FUEL CELLS|

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法律状态:
2018-10-30| PLFP| Fee payment|Year of fee payment: 2 |

2019-04-19| PLSC| Publication of the preliminary search report|Effective date: 20190419 |

2019-10-31| PLFP| Fee payment|Year of fee payment: 3 |

2020-10-30| PLFP| Fee payment|Year of fee payment: 4 |

2021-10-29| PLFP| Fee payment|Year of fee payment: 5 |

优先权:

申请号 | 申请日 | 专利标题

FR1759788A|FR3072304B1|2017-10-18|2017-10-18|DEVICE FOR GENERATING GAS|

FR1759788|2017-10-18|FR1759788A| FR3072304B1|2017-10-18|2017-10-18|DEVICE FOR GENERATING GAS|

EP18785665.3A| EP3697729A1|2017-10-18|2018-10-18|Device for generating gas|

KR1020207010842A| KR102287123B1|2017-10-18|2018-10-18|gazogene|

US16/753,238| US11267701B2|2017-10-18|2018-10-18|Gas generation device|

JP2020521930A| JP6831089B2|2017-10-18|2018-10-18|Gas generating device|

CN201880068407.4A| CN111542491B|2017-10-18|2018-10-18|Gas generating apparatus|

PCT/EP2018/078514| WO2019077024A1|2017-10-18|2018-10-18|Device for generating gas|

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