USPatent applicationPatented

Method for reducing carbon dioxide

Granted 15 Apr 2014 · 1 office action

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Abstract

The present subject matter provides a method for reducing carbon dioxide with the use of a device for reducing carbon dioxide. The device includes a cathode chamber, an anode chamber and a solid electrolyte membrane. The cathode chamber includes a working electrode which includes a metal or a metal compound. The anode chamber includes a counter electrode which includes a region formed of a nitride semiconductor. First and second electrolytic solutions are held in the cathode and anode chamber, respectively. The working electrode and the counter electrode are in contact with the first and second electrolytic solution, respectively. The solid electrolyte membrane is interposed between the cathode and anode chambers. The first electrolyte solution contains the carbon dioxide. An electric source is not interposed electrically between the working electrode and the counter electrode.

Description

13 parts
›This is a continuation of International Application No…

This is a continuation of International Application No. PCT/JP2011/004728, with an international filing date of Aug. 25, 2011, which claims priorities of Japanese Patent Application No. 2010-226338, filed on Oct. 6, 2010, Japanese Patent Application No. 2011-034087, filed on Feb. 21, 2011, and International Application No. PCT/JP2011/002391, filed on Apr. 22, 2011, the contents of each of which are hereby incorporated by reference.

The present disclosure relates to a method for reducing carbon dioxide.

Patent Literatures 1-2 disclose a method for reducing carbon dioxide by using an anode electrode formed of n-type photosemiconductor material such as TiO 2 .

Patent Literatures 3-4 disclose a method for electrolyzing water.

›CITATION LIST

Patent Literature

[Patent Literature 1]

Japanese Laid-Open Patent Application Publication No. Hei 07-188961

[Patent Literature 2]

Japanese Laid-Open Patent Application Publication No. Hei 05-311476

[Patent Literature 3]

Japanese Laid-Open Patent Application Publication No. Sho 50-115178

[Patent Literature 4]

Japanese Laid-Open Patent Application Publication No. Hei 2003-024764

›SUMMARY

Technical Problem

The methods disclosed in Patent Literatures 1-2 require an electric source between the anode electrode and a cathode electrode to reduce carbon dioxide. The present disclosure provides a novel method for reducing carbon dioxide without such an electric source.

Solution to Problem

The present disclosure relates to a method for reducing carbon dioxide with the use of a device for reducing carbon dioxide. The method includes the following steps. A step (a) is a step of preparing the device for reducing carbon dioxide. The device for reducing carbon dioxide includes a cathode chamber, an anode chamber and a solid electrolyte membrane. The cathode chamber includes a working electrode, and the working electrode includes a metal or a metal compound. The anode chamber includes a counter electrode and the counter electrode includes a region formed of a nitride semiconductor on the surface thereof. In the device, a first electrolytic solution is held in the cathode chamber, and a second electrolytic solution is held in the anode chamber. The working electrode is in contact with the first electrolytic solution and the counter electrode is in contact with the second electrolytic solution. The solid electrolyte membrane is interposed between the cathode chamber and the anode chamber. The first electrolyte solution contains the carbon dioxide. The working electrode is connected to the counter electrode. An electric source is not interposed electrically between the working electrode and the counter electrode.

A step (b) is a step of irradiating the region with a light having a wavelength of 250 nanometers to 400 nanometers to reduce the carbon dioxide contained in the first electrolyte solution. The working electrode is not irradiated with the light.

The novel method for reducing carbon dioxide according to the present disclosure does not require an electric source interposed between the anode electrode and the cathode electrode.

›BRIEF DESCRIPTION OF DRAWINGS

FIG. 1 shows an exemplary schematic view of a device for reducing carbon dioxide according to the embodiment 1.

FIG. 2A shows an exemplary schematic view of a counter electrode 104 where a metal wire 303 is not formed.

FIG. 2B shows an exemplary schematic view of a counter electrode 104 where a plurality of linear metal wires 303 are formed.

FIG. 2C shows an exemplary schematic view of a counter electrode 104 where a plurality of linear metal wires 303 with a shape of a mesh are formed.

FIG. 3 is a graph showing a current change before and after the nitride semiconductor region 302 was irradiated with the light in example 1.

FIG. 4 shows a relationship between the charge amount (horizontal axis) and the amount of the formic acid (vertical axis) in example 1.

FIG. 5 is a graph showing a current change before and after the nitride semiconductor region 302 was irradiated with the light in example 1, example 2, and example 3.

FIG. 6 is a graph showing the period of the irradiation of the light (horizontal axis) and the product amount of the formic acid (vertical axis) in examples 1-3.

›DESCRIPTION OF EMBODIMENTS

The embodiment of the present disclosure is described below.

›Embodiment 1 · 1 of 2

(Device for Reducing Carbon Dioxide)

FIG. 1 shows an exemplary schematic view of a device for reducing carbon dioxide according to the embodiment 1. The device includes a cathode chamber 102 , an anode chamber 105 , and a solid electrolyte membrane 106 .

The cathode chamber 102 includes a working electrode 101 .

The working electrode 101 is in contact with a first electrolytic solution 107 . Particularly, the working electrode 101 is immersed in the first electrolytic solution 107 .

An example of the material of the working electrode 101 is copper, gold, silver, cadmium, indium, tin, lead, or alloy thereof. Copper is preferred. In order to increase an amount of formic acid, indium is preferred. Another example of the material of the working electrode 101 is a metal compound capable of reducing carbon dioxide. Only a part of the working electrode 101 may be immersed in the first electrolytic solution 107 , as long as the material is in contact with the first electrolytic solution 107 .

The anode chamber 105 includes a counter electrode 104 .

The counter electrode 104 is in contact with a second electrolytic solution 108 . Particularly, the counter electrode 104 is immersed in the second electrolytic solution 108 .

As shown in FIG. 2A , the counter electrode 104 includes a nitride semiconductor region 302 formed of nitride semiconductor on the surface thereof. It is preferred that the nitride semiconductor is gallium nitride or aluminum gallium nitride. In FIG. 2A , the square nitride semiconductor region 302 is formed on a part of the surface of the counter electrode 104 . However, the nitride semiconductor region 302 may be formed on the whole surface of the counter electrode 104 . The shape of the nitride semiconductor region 302 is not limited to a square.

As shown in FIG. 2B and FIG. 2C , it is preferable that a metal wire 303 is provided on the nitride semiconductor region 302 . It is preferred that the metal wire 303 is in contact with the nitride semiconductor region 302 . As described later, the nitride semiconductor region 302 is irradiated with a light from a light source 103 . The metal wire 303 is also irradiated with the light.

As shown in FIG. 2B , a plurality of metal wires 303 may be provided. Each metal wire has a line shape. The plurality of metal wires 303 are arranged in parallel to one another.

As shown in FIG. 2C , a plurality of metal wires 303 having a shape of a mesh may be provided. The shape of the metal wire(s) is not limited.

It is preferable that the metal wire 303 forms an ohmic contact with the nitride semiconductor. An example of the suitable material of the metal wire 303 is titanium. Particularly, the metal wire 303 is a titanium wire, a titanium/nickel stacked wire, a titanium/aluminum stacked wire, a titanium/gold stacked wire, or a titanium/silver stacked wire. A titanium/nickel stacked wire is preferred.

Only a part of the counter electrode 104 may be immersed in the second electrolytic solution 108 as long as the nitride semiconductor is in contact with the second electrolytic solution 108 .

The first electrolytic solution 107 is held in the cathode chamber 102 . The second electrolytic solution 108 is held in the anode chamber 105 .

An example of the first electrolytic solution 107 is a potassium bicarbonate aqueous solution, a sodium bicarbonate aqueous solution, a potassium chloride aqueous solution, a potassium sulfate aqueous solution, or a potassium phosphate aqueous solution. A potassium bicarbonate aqueous solution is preferred. Preferably, the first electric solution 107 is mildly acidic in the condition where carbon dioxide is dissolved in the first electric solution 107 .

An example of the second electrolytic solution 108 is a sodium hydroxide aqueous solution or a potassium hydroxide aqueous solution. A sodium hydroxide aqueous solution is preferred. Preferably, the second electrolytic solution 108 is strongly basic.

The solute of the first electrolytic solution 107 may be identical to that of the second electrolytic solution 108 ; however, it is preferable that the solute of the first electrolytic solution 107 is difficult from that of the second electrolytic solution 108 .

The first electrolytic solution 107 contains carbon dioxide. The concentration of the carbon dioxide is not limited.

In order to separate the first electrolytic solution 107 from the second electrolytic solution 108 , the solid electrolyte membrane 106 is interposed between the cathode chamber 102 and the anode chamber 105 . Namely, the first electrolytic solution 107 and the second electrolytic solution 108 are not mixed in the present device.

A material for the solid electrolyte membrane 106 is not limited, as long as only a proton penetrates the solid electrolyte membrane 106 and other materials can not penetrate the solid electrolyte membrane 106 . An example of the solid electrolyte membrane 106 is Nafion (Registered Trade Mark).

The working electrode 101 includes a working electrode terminal 110 . The counter electrode 104 includes a counter electrode terminal 111 . The working electrode terminal 110 and the counter electrode terminal 111 are electrically connected through a conductive wire 112 . Namely, the working electrode 101 is electrically connected to the counter electrode 104 through the conductive wire 112 . As shown in FIG. 2B and FIG. 2C , the metal wire 303 is electrically connected to the counter electrode terminal 111 . Unlike Patent Literatures 1-2, an electric source is not interposed electrically between the working electrode 101 and the counter electrode 104 in the present disclosure. An example of the electric source is a battery and a potentiostat.

(Method for Reducing Carbon Dioxide)

Next, the method for reducing carbon oxide with the use of the above-mentioned device is described below.

The device is put at a room temperature and under atmospheric pressure.

As shown in FIG. 1 , a nitride semiconductor region 302 is irradiated with the light from the light source 103 . At least part of the nitride semiconductor region 302 is irradiated with the light. The whole nitride semiconductor region 302 may be irradiated with the light.

›Embodiment 1 · 2 of 2

An example of the light source 103 is a xenon lamp.

The working electrode 101 is not irradiated with the light.

It is preferred that the light from the light source 103 have a wavelength of not less than 250 nanometers and not more than 400 nanometers. Preferably, the light has a wavelength of not less than 250 nanometers and not more than 365 nanometers.

The metal wire 303 may be provided on the obverse surface of the nitride semiconductor region 302 . Namely, the metal wire 303 and the nitride semiconductor region 302 are irradiated with the light from the light source 103 . Furthermore, it is preferable that the metal wire 303 is covered with an insulating material (not shown).

As shown in FIG. 1 , the device preferably includes a tube 109 . It is preferred that the carbon dioxide contained in the first electrolytic solution 107 is reduced while carbon dioxide is supplied through the tube 109 to the first electrolytic solution 107 . One end of the tube 109 is immersed in the first electrolytic solution 107 . It is preferred that a sufficient amount of carbon dioxide is dissolved in the first electrolytic solution 107 by supplying carbon dioxide through the tube 109 before the reduction of carbon dioxide starts.

The carbon dioxide contained in the first electrolytic solution 107 is reduced to form carbon monoxide or formic acid, when the working electrode 101 includes metal such as copper, gold, silver cadmium, indium, tin, or lead.

›EXAMPLES

The present subject matter is described in more detail with reference to the following example.

›Examples3
›Example 1

(Preparation of the Counter Electrode)

An n-type gallium nitride film was epitaxially grown on a sapphire substrate by a metal organic chemical vapor deposition method. The n-type gallium nitride film corresponds to the nitride semiconductor region 302 . Next, metal wires 303 having a shape of a mesh were formed with an ordinary semiconductor process such as a photolithography, an electron beam deposition, and a lift off technique. The metal wires 303 were made of a Ti/Ni bilayer. The metal wires 303 had a width of 20 micrometers and a thickness of 0.5 micrometers. The interval between two adjacent wires in the mesh was 50 micrometers. A counter electrode terminal 111 which was electrically connected to the metal wires 303 was formed. Thus, as shown in FIG. 2C , obtained was the counter electrode 104 including a nitride semiconductor region 302 formed of the n-type gallium nitride including the metal wires 303 .

(Assemblage of the Device)

The device for reducing carbon dioxide shown in FIG. 1 was formed with the use of the counter electrode 104 . The device is described below in more detail.

Working electrode 101 : A Copper plate

First electrolytic solution 107 : Aqueous potassium bicarbonate with a concentration of 0.1 mol/L (180 ml)

Second electrolytic solution 108 : Aqueous sodium hydroxide with a concentration of 1.0 mol/L (180 ml)

Solid electrolyte membrane 106 : Nafion membrane (available from DuPont Kabushiki Kaisha, trade name: Nafion 117)

Light source 103 : Xenon Lamp (Output: 300 W)

The light source 103 emitted a broad light with a wavelength of 250 nanometers to 400 nanometers.

(Reduction of Carbon Dioxide)

Carbon dioxide was supplied for thirty minutes through the tube 109 to the first electrolytic solution 107 by bubbling.

The anode chamber 105 had a window (not shown). The nitride semiconductor region 302 was irradiated with the light from the light source 103 through the window.

FIG. 3 is a graph showing a current change before and after the nitride semiconductor region 302 was irradiated with the light. As shown in FIG. 3 , when the nitride semiconductor region 302 was irradiated with the light, a current flew through the wire 112 . When the region was not irradiated with the light, the flow of the current stopped. This means that a reaction was occurred in at least one electrode of the working electrode 101 and the counter electrode 104 .

The present inventors investigated the reaction in more detail as below. Particularly, after the cathode chamber 102 was sealed, the nitride semiconductor region 302 was irradiated with the light once again. A gas component generated in the cathode chamber 102 was analyzed with a gas chromatography. A liquid component generated in the cathode chamber 102 was analyzed with a liquid chromatography.

As a result, it was confirmed that formic acid, carbon monoxide, and methane were generated in the cathode chamber 102 .

Furthermore, a charge amount (coulomb amount) relevant to the reaction was calculated from the light current amount caused by the irradiation of the light. FIG. 4 shows a relation ship between the charge amount (horizontal axis) and the amount of the formic acid (vertical axis). As is clear from FIG. 4 , the amount of the formic acid was proportional to the charge amount. This means that a catalytic reaction where the carbon dioxide was reduced was occurred due to the irradiation of the light.

›Example 2

An identical experiment to example 1 was performed except that metal wires 303 made of nickel were used instead of the metal wires 303 made of the Ti/Ni bilayer.

›Example 3

As shown in FIG. 2A , an identical experiment to example 1 was performed except that metal wires 303 were not formed.

FIG. 5 is a graph showing a current change before and after the nitride semiconductor region 302 was irradiated with the light in example 1, example 2, and example 3. In FIG. 5 , the referential signs (a), (b), and (c) indicate the results of example 1, example 2, and example 3, respectively. As shown in FIG. 5 , the current amount in example 1 was the largest, and the current amount in example 3 was the smallest.

FIG. 6 shows the period of the irradiation of the light (horizontal axis) and the product amount of the formic acid (vertical axis). In FIG. 6 , the referential signs (a), (b), and (c) indicate the results of example 1, example 2, and example 3, respectively. As shown in FIG. 6 , when the periods of the irradiation of the light are identical, the amount of the formic acid produced in example 1 was the largest, and the amount of the formic acid produced in example 3 was the smallest.

As is clear from FIG. 5 and FIG. 6 , the production amount per unit time of the formic acid was increased when the metal wires 303 were used. The production amount per unit time of the formic acid was more increased when the metal wires 303 made of the Ti/Ni bilayer was used.

›INDUSTRIAL APPLICABILITY

The present subject matter provides a method for reducing carbon dioxide.

›REFERENCE SIGNS LIST

101 : working electrode

102 : cathode chamber

104 : counter electrode

105 : anode chamber

106 : solid electrolyte membrane

107 : first electrolyte solution

108 : second electrolyte solution

302 : region

303 : metal wire

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Classifications

4 codes
IPC · International Patent Classification
Section B — Performing operations; transporting
  • B01J35/00
Section C — Chemistry; metallurgy
  • C25B3/25
  • C25B9/17
USPC · US Patent Classification
205/340

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Keith Hendricks
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