Fuel production method and fuel production apparatus

Patent metadata

Field	Value
Publication number	US-2017335468-A1
Application number	US-201715413484-A
Country	US
Kind code	A1
Filing date	Jan 24, 2017
Priority date	May 18, 2016
Publication date	Nov 23, 2017
Grant date	—

Abstract

The present disclosure provides a fuel production method and a fuel production apparatus which efficiently convert solar light energy into a fuel. The fuel production apparatus of the present disclosure includes a laminate, an electrolytic bath, and a support tool or a proton permeable membrane. The laminate includes a photoelectromotive layer having a p-n junction structure, a cathode electrode, an anode electrode and a side surface insulating layer, and the photoelectromotive layer includes a semiconductor layer that absorbs light in a near-infrared region with a wavelength of 900 nm or more. In the fuel production apparatus, an underwater optical path length is set to an optimum design value, so that even light in a near-infrared region with a wavelength of 900 nm or more is sufficiently utilized to efficiently convert light energy into at least one fuel selected from hydrogen, carbon monoxide, formic acid, methane, ethylene, methanol, ethanol, isopropanol, allyl alcohol, acetaldehyde and propionaldehyde through a reduction reaction on the cathode electrode.

First claim

What is claimed is:

1 . A fuel production method comprising:
(a) providing a fuel production apparatus comprising an electrolytic bath, a laminate and a support tool, wherein the electrolytic bath holds an electrolytic solution, the laminate includes a cathode electrode containing a metal or a metal compound, a photoelectromotive layer having a p-n junction structure, and an anode electrode, the cathode electrode and the anode electrode are in contact with the electrolytic solution, the p-n junction structure includes a p-type layer and an n-type layer, the photoelectromotive layer includes at least one semiconductor layer capable of absorbing light in a near-infrared region having a wavelength of not less than 900 nm, the cathode electrode is formed on the photoelectromotive layer on an n-type layer side, the anode electrode is formed on the photoelectromotive layer on a p-type layer side, a side surface insulating layer is formed on a side surface of the laminate, and the laminate is supported in the electrolytic solution with surfaces of the anode electrode and the cathode electrode which are in contact with the electrolytic solution being insulated from each other by the support tool; and (b) irradiating the cathode electrode with light to produce a fuel in the cathode electrode, wherein an optical path length of the light to a surface of the photoelectromotive layer in the electrolytic solution is not more than 7 mm.

2 . The fuel production method according to claim 1 , wherein
the light in the step (b) includes light having a wavelength of not less than 900 nm.

3 . The fuel production method according to claim 1 , wherein
the metal is platinum, and in the step (b), hydrogen is obtained as a fuel.

4 . The fuel production method according to claim 1 , wherein
the metal compound is at least one selected from the group consisting of a platinum alloy and a platinum compound, and in the step (b), hydrogen is obtained as a fuel.

5 . The fuel production method according to claim 1 , wherein
carbon dioxide is dissolved in the electrolytic solution, the metal is gold, and in the step (b), carbon monoxide is obtained as a fuel by reduction of the carbon dioxide.

6 . The fuel production method according to claim 1 , wherein
carbon dioxide is dissolved in the electrolytic solution, the metal compound is at least one selected from the group consisting of a gold alloy and a gold compound, and in the step (b), carbon monoxide is obtained as a fuel by reduction of the carbon dioxide.

7 . The fuel production method according to claim 1 , wherein
carbon dioxide is dissolved in the electrolytic solution, the metal is indium, and in the step (b), formic acid is obtained as a fuel by reduction of the carbon dioxide.

8 . The fuel production method according to claim 1 , wherein
carbon dioxide is dissolved in the electrolytic solution, the metal compound is at least one selected from the group consisting of an indium alloy and an indium compound, and in the step (b), formic acid is obtained as a fuel by reduction of the carbon dioxide.

9 . The fuel production method according to claim 1 , wherein
carbon dioxide is dissolved in the electrolytic solution, the metal is copper, and in the step (b), at least one selected from the group consisting of methane, ethylene, ethanol and acetaldehyde is obtained as a fuel by reduction of the carbon dioxide.

10 . The fuel production method according to claim 1 , wherein
carbon dioxide is dissolved in the electrolytic solution, the metal compound is at least one selected from the group consisting of a copper alloy and a copper compound, and in the step (b), at least one selected from the group consisting of methane, ethylene, ethanol and acetaldehyde is obtained as a fuel by reduction of the carbon dioxide.

11 . The fuel production method according to claim 1 , wherein
carbon dioxide is dissolved in the electrolytic solution, the metal is silver, and in the step (b), carbon monoxide is obtained as a fuel by reduction of the carbon dioxide.

12 . The fuel production method according to claim 1 , wherein
carbon dioxide is dissolved in the electrolytic solution, the metal compound is at least one selected from the group consisting of a silver alloy and a silver compound, and in the step (b), carbon monoxide is obtained as a fuel by reduction of the carbon dioxide.

13 . The fuel production method according to claim 1 , wherein
the photoelectromotive layer is formed of at least one selected from the group consisting of gallium arsenide, indium gallium arsenide, silicon and germanium.

14 . The fuel production method according to claim 1 , wherein
the electrolytic solution is an aqueous solution containing at least one selected from the group consisting of potassium hydrogen carbonate and sodium hydrogen carbonate.

15 . The fuel production method according to claim 1 , wherein
a photoelectrochemical apparatus is left at rest at room temperature under atmospheric pressure in the step (b).

16 . A fuel production apparatus comprising:
an electrolytic bath; a laminate; and a support tool, wherein the electrolytic bath holds an electrolytic solution, the laminate includes a cathode electrode containing a metal or a metal compound, a photoelectromotive layer having a p-n junction structure, and an anode electrode, the cathode electrode and the anode electrode are in contact with the electrolytic solution, the p-n junction structure includes a p-type layer and an n-type layer, the photoelectromotive layer includes at least one semiconductor layer that absorbs light in a near-infrared region having a wavelength of not less than 900 nm, the cathode electrode is formed on the photoelectromotive layer on an n-type layer side, the anode electrode is formed on the photoelectromotive layer on a p-type layer side, a side surface insulating layer is formed on a side surface of the laminate, the laminate is supported in the electrolytic solution with surfaces of the anode electrode and the cathode electrode which are in contact with the electrolytic solution being insulated from each other by the support tool, and an optical path length of the light to a surface of the photoelectromotive layer in the electrolytic solution is not more than 7 mm.

17 . A fuel production apparatus comprising:
a cathode bath; an anode bath; a proton permeable membrane; and a laminate, wherein the cathode bath holds a first electrolytic solution, the anode bath holds a second electrolytic solution, the cathode bath and the anode bath are separated by the proton permeable membrane and the laminate, the laminate includes a cathode electrode containing a metal or a metal compound, a photoelectromotive layer having a p-n junction structure, and an anode electrode, the cathode electrode is in contact with the first electrolytic solution, the anode electrode is in contact with the second electrolytic solution, the p-n junction structure includes a p-type layer and an n-type layer, the photoelectromotive layer includes at least one semiconductor layer that absorbs light in a near-infrared region having a wavelength of not less than 900 nm, the cathode electrode is formed on the photoelectromotive layer on an n-type layer side, the anode electrode is formed on the photoelectromotive layer on a p-type layer side, and an optical path length of the light to a surface of the photoelectromotive layer in the first electrolytic solution is not more than 7

Assignees

• Panasonic Ip Man Co Ltd

Inventors

• Okamoto Shinya
• Sekimoto Takeyuki
• Deguchi Masahiro
• Yotsuhashi Satoshi

Classifications

• C25B11/04

  characterised by the material · CPC title

• H01G9/2045

  comprising a semiconductor electrode comprising elements of the fourth group of the Periodic Table with or without impurities, e.g. doping materials · CPC title

• C25B3/04

  Chemistry & Metallurgy · mapped topic

• H01L31/068

  Electricity · mapped topic

• C25B1/04

  by electrolysis of water · CPC title