Patent Application
20170101717
The present invention relates to a water electrolysis method and water electrolysis device in which water is supplied to the cathode side of an electrolytic membrane including a solid polymer membrane provided with a catalyst layer on a surface thereof, and water is electrolyzed by allowing an electric current to flow between both surfaces of the electrolytic membrane.
Oxygen required for human respiration in a spacecraft or space station, etc. can be created by electrolysis of water.
An example is generally known in which electrolysis of water is performed with an electrolysis device using a solid polymer membrane, wherein water is supplied only to an electrode where oxygen is generated (anode) or to both an electrode where hydrogen is generated (cathode) and the electrode where oxygen is generated (anode).
Water is supplied because a membrane which is typically used as a solid polymer membrane has hydrogen ion conductivity, and the electrolysis is accompanied by a phenomenon of an electrochemical osmotic pressure being generated from an anode towards a cathode and thus moving water from the anode side to the cathode side, and therefore in cases where water is not supplied at least to the anode side, the membrane dries as the electrolysis progresses.
However, when oxygen is used for human respiration in a space station, etc., this oxygen needs to be dry. This is partly because wet oxygen is unsuitable for respiration, and also because providing a wet gas in a closed environment may create condensations, which in turn leads to malfunction of electronic devices.
This being the case, a method for delivering dry oxygen is needed, and in order to ensure safety, it is necessary to minimize the admixture of hydrogen generated at a counter electrode into oxygen through the membrane.
Methods and devices for obtaining hydrogen and oxygen by electrolyzing water have been advanced widely in the field of industrial technology, and various configurations thereof corresponding to the intended use of the generated hydrogen or oxygen are known.
As one example, technology for obtaining oxygen and hydrogen by electrolyzing liquid-state water or electrolytic solution by bringing it into contact with a cathode and an anode is well known, as disclosed in PTL 1, for example.
With this well-known water electrolysis method and water electrolysis device, both hydrogen and oxygen are generated as bubbles in the liquid, and a gas-liquid separator is needed so that they could be used in a gaseous state, making the device complex. In a zero-gravity state such as in a space station, in particular, a special device is needed so as to subject the bubbles in the liquid to separation, which unfavorably results in even greater complexity of the device and cost rise.
Further, a large amount of hydrogen is admixed to the generated oxygen and a large amount of oxygen is admixed to hydrogen, so measures need to be taken for both to prevent ignition and explosion, and this also leads to unfavorable cost rise of the entire device.
It is also well known, as disclosed in PTL 2, etc., that supplying water only to the cathode side of an electrolytic membrane (bilayer membrane 20) provided with a catalyst layer on the surface thereof and electrolyzing water by creating a potential difference between both surfaces of the electrolytic membrane eliminates the need for gas-water separation for oxygen generated on the anode side.
However, with the well-known technique disclosed in the aforementioned PTL 2, although purity of oxygen generated at the anode side of the electrolytic membrane (bilayer membrane 20) can be increased, a pressure on the anode side is set significantly higher than on the cathode side of the electrolytic membrane (bilayer membrane 20) in order to achieve this increase in purity.
This being the case, the electrolytic membrane (bilayer membrane 20) needs to be increased in thickness in order to prevent damage on the electrolytic membrane (bilayer membrane 20) caused by such a difference in pressure and reduce the admixture of oxygen generated on the anode side to the cathode side.
Problems arising when the electrolytic membrane (bilayer membrane 20) is made thicker are that power necessary for electrolysis also increases, the electrolysis efficiency in relation to the consumed power is degraded, and power supply equipment also becomes costly.
Another problem is that since the pressure on the anode side of the electrolytic membrane (bilayer membrane 20) is significantly higher than on the cathode side, a large amount of oxygen is still admixed to hydrogen generated on the cathode side, so measures need to be taken to prevent ignition and explosion, leading to cost rise of the entire device.
Under these circumstances, it is an objective of the present invention to resolve the problems inherent to the well-known water electrolysis methods and water electrolysis devices, such as described hereinabove, i.e. to provide a water electrolysis method and a water electrolysis device in which mixing of the generated hydrogen and oxygen is greatly reduced and which have a high electrolysis efficiency, while being simplified in structure.
The present invention resolves the aforementioned problems by providing a water electrolysis method in which water is electrolyzed by allowing an electric current to flow between both surfaces of an electrolytic membrane including a solid polymer membrane provided with a catalyst layer on a surface thereof, wherein temperature-controlled water is supplied only to a cathode side of the electrolytic membrane, while controlling a difference in pressure between both surfaces of the electrolytic membrane to 50 kPa or less.
The present invention also resolves the aforementioned problems by providing a water electrolysis device having an electrolytic membrane including a solid polymer membrane provided with a catalyst layer on a surface thereof; a housing having spaces defined by the electrolytic membrane; power supply unit for allowing an electric current to flow between both surfaces of the electrolytic membrane; water supply unit for supplying water to a cathode side of the electrolytic membrane; and pressure control unit for controlling a pressure in both the spaces in the housing defined by the electrolytic membrane, wherein the water supply unit has a water temperature control device that controls the temperature of water supplied to the cathode side of the electrolytic membrane, and a difference in pressure between both the spaces in the housing defined by the electrolytic membrane is made 50 kPa or less by the pressure control unit.
With the water electrolysis method as in claim 1 and water electrolysis device as in claim 8 of the present application, by controlling the temperature of water supplied to the cathode side, it is possible to optimize the diffusion of water to the surface of the electrolytic membrane and to obtain a wet shield effect in the vicinity of the hydrogen-generating electrode with the membrane through which water has sufficiently diffused.
As a result, oxygen generated on the anode side and hydrogen generated on the cathode side can be further prevented from passing through inside the electrolytic membrane. Therefore, the admixture of hydrogen to the generated oxygen and the admixture of oxygen to hydrogen can be suppressed, while reducing the electrolytic membrane in thickness.
Further, by setting the difference in pressure between both surfaces of the electrolytic membrane to 50 kPa or less, it is possible to prevent the electrolytic membrane from damage caused by the difference in pressure, while reducing the electrolytic membrane in thickness, and also to suppress the movement of oxygen and hydrogen in the membrane caused by the difference in pressure.
With the features disclosed in claim 2 and claim 9 of the present, application, the electrolytic membrane is subjected to internal strength reinforcement with an organic polymer or an inorganic substance with a low gas permeability. As a result, the passage of oxygen generated on the anode side and hydrogen generated on the cathode side can be prevented by the organic polymer or inorganic substance used for the reinforcement. Further, as a result of reducing the thickness of the organic polymer or inorganic substance used for the reinforcement, practically no effect is produced on the movement of ions. Therefore, the admixture of hydrogen to the generated oxygen and the admixture of oxygen to hydrogen can be suppressed, while reducing the electrolytic membrane in thickness.
Further, power needed for the electrolysis can be reduced and the electrolysis efficiency in relation to the consumed power is increased due to the decrease of the electrolytic membrane in thickness.
In addition, since the organic polymer or inorganic substance used for the reinforcement have strength, damage caused by the difference in pressure can be prevented despite the reduction in the electrolytic membrane thickness.
Further, since the admixture of hydrogen to oxygen and the admixture of oxygen to hydrogen can be suppressed, damage caused by the difference in pressure can be prevented, and the electrolysis efficiency in relation to the consumed power can be increased, the device and structure needed for implementing such measures can be simplified, and the structure can be simplified.
Since the organic polymer or inorganic substance used for the reinforcement are insulators and, therefore, not affected by any force from the applied electric field, the electrolytic membrane can be prevented from damage and deterioration.
Further, as a result of using the organic polymer or inorganic substance for the reinforcement, it is possible to use a thin film, while maintaining the strength thereof, and reduce the electric resistance in the electrolysis. Therefore, water electrolysis can be implemented at a low temperature. The usual water electrolysis is implemented at a high temperature of about 80° C., but where water electrolysis is performed in high-temperature range, water vapor is generated and the amount of water vapor admixed to the oxygen gas is increased. By contrast, since it is possible to maintain a low operation temperature, the amount of water admixed to the generated oxygen can be suppressed.
It is desirable that the operation be performed within a range from room temperature to about 60° C. since condensation of the gas which is to be discharged can be prevented.
With the features set forth in claim 3, claim 4, claim 5, claim 10, claim 11, and claim 12 of the present application, it is also possible to ensure a small thickness, a high strength, and insulating properties, and perform efficient electrolysis without affecting the movement of ions.
With the features set forth in claim 6 and claim 13 of the present application, by controlling the temperature of water supplied to the cathode side of the electrolytic membrane within a range of room temperature to 60° C., it is possible to control the amount of generated water vapor and control the water temperature in an easy manner in a practical range.
With the features set forth in claim 1 and claim 14 of the present application, it is possible to suppress sufficiently the admixture of hydrogen to oxygen and the admixture of oxygen to hydrogen in an electrolytic membrane that is significantly thinner than the conventional membranes. At the same time, it is possible to prevent damage caused by the difference in pressure, further increase the electrolysis efficiency in relation to the consumed power, and simplify the device and structure.
With the feature set forth in claim 15 of the present application, it is possible to control efficiently the temperature of water supplied to the cathode side, without providing a complex mechanism.
With the feature set forth in claim 16 of the present application, water supplied to the cathode side can be supplied under optimum conditions and in an optimum amount.
In the water electrolysis method of the present invention, water is electrolyzed by allowing an electric current to flow between both surfaces of an electrolytic membrane including a solid polymer membrane provided with a catalyst layer on a surface thereof, wherein temperature-controlled water is supplied only to a cathode side of the electrolytic membrane, while controlling a difference in pressure between both surfaces of the electrolytic membrane to 50 kPa or less. Further, the water electrolysis device of the present invention has an electrolytic membrane including a solid polymer membrane provided with a catalyst layer on a surface thereof; a housing having spaces defined by the electrolytic membrane; power supply unit for allowing an electric current to flow between both surfaces of the electrolytic membrane; water supply unit for supplying water to a cathode side of the electrolytic membrane; and pressure control unit for controlling a pressure in both spaces in the housing defined by the electrolytic membrane, wherein the water supply unit has a water temperature control device that controls the temperature of water supplied to the cathode side of the electrolytic membrane, and a difference in pressure between both spaces in the housing defined by the electrolytic membrane is made 50 kPa or less by the pressure control unit. The method and device may be implemented in any specific form, provided that the admixture of the generated hydrogen and oxygen is very small and the electrolysis efficiency is high, while the structure is simplified.
Pt/Ir, Pd/Ir, and the like, are generally used as catalysts on the electrolytic membrane surface, but those examples are not limiting.
Further, it is preferred that an organic polymer or inorganic substance with a low gas permeability that is used for reinforcement provided inside the electrolytic membrane be in the form of a film-like reinforcing membrane, and it may be a single solid polymer membrane or a thin film of a ceramic material, or the like, and may have a single-layer or laminated configuration.
An embodiment of the water electrolysis method and water electrolysis device in accordance with the present invention will be explained hereinbelow with reference to the drawings.
As depicted in
The water supply unit 120 is configured to circulate water, which is to be electrolyzed, with a pump 121 and to replenish the amount of water reduced by the electrolysis from a water tank 125.
More specifically, water, which is to be electrolyzed, is supplied from the pump 121 to the cathode side of the housing 101 through a check valve 124, this water together with hydrogen generated on the cathode side pass through a heat exchanger 122 constituting a water temperature control device, hydrogen is separated with a gas-water separator 123, and water is then returned to the pump 121 through the check valve 124 and supplied again.
Water that has passed through an ion exchange membrane 126 from the water tank 125 is replenished on the upstream of the pump 121.
The heat exchanger 122 constituting the water temperature control device is configured, for example, such as to perform heat exchange with the air inside the room and also configured to be capable of controlling the temperature of water supplied to the cathode side within a range of room temperature to 100° C. with any well-known unit, for example, by controlling the revolution speed of an air blowing fan.
Hydrogen generated on the cathode side is separated from the circulating water with the gas-water separator 123 and fed through pressure control unit 140, a flowmeter 141, and a hygrometer 142 to a hydrogen tank or hydrogen-using device (not depicted in the figures) according to the intended use.
A pressure applied to the cathode side of the electrolytic membrane 102 in the housing 101 is regulated by the pressure control unit 140 on the hydrogen side.
Meanwhile, oxygen generated on the anode side 104 in the housing 101 is fed through pressure control unit 130, a flowmeter 131, and a hygrometer 132 to an oxygen tank or oxygen-using device (not depicted in the figures) according to the intended use.
A pressure applied to the anode side of the electrolytic membrane 102 in the housing 101 is regulated by the pressure control unit 130 on the oxygen side, and this unit is configured to operate in coordination with the pressure control unit 140 on the hydrogen side, such as to control the difference in pressure between both spaces of the housing 101 defined by the electrolytic membrane 102 to 50 kPa or less.
The effects obtained with the water electrolysis method and water electrolysis device of the present invention which are configured in the above-described manner will be explained hereinbelow.
The water electrolysis device in the form of a three-cell stack was used for electrolysis in which water was supplied at a rate of 680 ml/min to a cathode as a hydrogen-generating electrode, without supplying water to an oxygen-generating electrode.
In
As follows from the figure, when the cation exchange membrane (Nafion 117 (trade name)) was used, the concentration of hydrogen in oxygen of 3500 ppm or higher was continuously detected, whereas when a solid polymer membrane having hydrogen ion conductivity and reinforced with a polytetrafluoroethylene porous film with a thickness of 30 μm was used, only the concentration of hydrogen in oxygen of 1000 ppm or less was detected at all times in the same test, and the effect of using the reinforcing membrane could be confirmed.
A 10 mm (width)×10 cm (length) sample of the membrane used herein was prepared for a tensile strength test, tension was applied to the sample at a crosshead speed of 200 mm/min at 25° C. and a relative humidity of 50% by using a gage length (distance between clamps) of 50 mm, and the maximum load at the time of rupture was recorded. The membrane demonstrated strength of 61 MPa and 56 MPa in the longitudinal direction and transverse direction, respectively. When the same test was performed with respect to Nafion 112 (trade name) having a thickness of 50 μm, the measured tensile strength was 30 MPa and 30 MPa in the longitudinal direction and transverse direction, respectively. Thus, it is clear that the reinforced membrane had an about two-fold strength.
Further, a 5 cm×5 cm sample stored for a minimum of 1 day at 25° C. and a relative humidity of 50% was put for 10 min in deionized water at 100° C. The sample was then taken out placed on a rubber mat, and flat spread. The length in the transverse and longitudinal direction after swelling was measured with a JIS first class scale, and a hydration swelling ratio was determined. The change thereof was 3% in the longitudinal direction and 0% in the transverse direction. When the same test was performed with respect to Nafion 112 (trade name) having a thickness of 50 μm, the hydration swelling ratio was 19% in the longitudinal direction and 16% in the transverse direction. It was thus found that the dimensional variability caused by hydration had a value of ⅕ or less.
With the water electrolysis method and water electrolysis device of the present invention, electrolysis efficiency is increased while ensuring the purity of the generated hydrogen and oxygen. Therefore, the method and device are advantageous for generating hydrogen and oxygen in artificial satellites and space stations where strong constraints are placed on weight, space, and equipment.
Further, the present technique which increases the electrolysis efficiency and facilitates gas separation during water electrolysis can be used not only for hydrogen and oxygen generation, but also for regenerative fuel cells and unitized regenerative fuel cells (reversible fuel cells) that require water electrolysis.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2014-064464 | Mar 2014 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2015/059322 | 3/26/2015 | WO | 00 |
