Electrochemical hydrogen flow rate control system

• US 20030232225A1
• Filed: 04/22/2003
• Published: 12/18/2003
• Est. Priority Date: 04/22/2002
• Status: Active Grant

• Current Assignee: Sony Corporation (Sony Group Corp.)
• Original Assignee: Sony Corporation (Sony Group Corp.)
• Inventors: Oogane, Makoto, Maruyama, Ryuichiro, Ata, Masafumi
• Granted Patent: US 7,029,782 B2
• Time in Patent Office: Days
• US Class Current: 429/446
• CPC Class Codes: B82Y 15/00 Nanotechnology for interacting, sensing or actuating, e.g. quantum dots as markers in protein assays or molecular motors
• CPC Class Codes: H01M 4/8807 Gas diffusion layers
• CPC Class Codes: H01M 4/92 Metals of platinum group H01M4/94 , H01M4/9058 take precedence
• CPC Class Codes: H01M 4/923 Compounds thereof with non-metallic elements
• CPC Class Codes: H01M 8/04089 of gaseous reactants
• CPC Class Codes: H01M 8/0656 by electrochemical means H01M8/065 takes precedence
• CPC Class Codes: H01M 8/1007 with both reactants being gaseous or vaporised H01M8/12 takes precedence
• CPC Class Codes: H01M 8/1023 having only carbon, e.g. polyarylenes, polystyrenes or polybutadiene-styrenes
• CPC Class Codes: H01M 8/1039 halogenated, e.g. sulfonated polyvinylidene fluorides
• CPC Class Codes: H01M 8/1048 Ion-conducting additives, e.g. ion-conducting particles, heteropolyacids, metal phosphate or polybenzimidazole with phosphoric acid
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

An electrochemical hydrogen flow rate control system is provided. The system has an electrochemical cell and a hydrogen flow rate control unit. The electrochemical cell includes a first electrode for generating protons (H⁺), a second electrode for converting the protons generated by said first electrode into hydrogen gas, and a proton conductive solid electrolyte membrane held between said first and second electrodes. The hydrogen flow rate control unit is adapted to generate a specific amount of hydrogen gas on the second electrode side. The proton conductive solid electrolyte membrane is made from a fullerene derivative obtained by introducing proton dissociative groups in carbon atoms of fullerene molecules. Such a control system is operable even in a non-humidified atmosphere and at room temperature and is configurable as lightweight and compact in system design.

Claims

1. An electrochemical hydrogen flow rate control system comprising:

an electrochemical cell including a first electrode for generating protons on a first side of the electrochemical cell, a second electrode for converting the protons generated by said first electrode into hydrogen gas on a second side of the electrochemical cell, and a proton conductive solid electrolyte membrane fixed between the first and second electrodes; and

a hydrogen flow rate control unit for generating a specific amount of hydrogen gas on the second side of the electrochemical cell, wherein the proton conductive solid electrolyte membrane includes a fullerene derivative composed of one or more fullerene molecules with carbon atoms having one or more proton dissociative groups introduced thereto.

2. The system according to claim 1, wherein a hydrogen gas is supplied to a surface side, not provided with said proton conductive solid electrolyte membrane, of the first electrode, and a specific amount of current is applied between the first and second electrodes by said hydrogen flow rate control unit allowing the hydrogen gas to be electrolyzed into the protons in an amount corresponding to the specific amount of current on the first electrode side such that the protons are capable of migrating to the second electrode through the proton conductive solid electrolyte membrane and are converted again into hydrogen gas on the second electrode side, thus obtaining a specific amount of the hydrogen gas on the second electrode side.

3. The system according to claim 1, wherein the electrochemical cell includes a membrane-electrode assembly having a multi-layer structure that includes the first and second electrodes, each of which are composed of a gas diffusive electrode having a catalyst supported thereon wherein the electrodes are disposed on both sides of the proton conductive solid electrolyte membrane.

4. The system according to claim 3, wherein the proton conductive solid electrolyte membrane and the gas diffusive electrodes are alternately stacked thereby defining a single body.

5. The system according to claim 1, wherein the hydrogen flow rate control unit is removably mounted to the electrochemical hydrogen flow rate control system.

6. The system according to claim 1, wherein the proton dissociative group includes a chemical group expressed by a molecular formula —

XH where X an atom or a group of atoms having a bivalent bond, and H is a hydrogen atom.

7. The system according to claim 6, wherein the proton dissociative group is a chemical group expressed by a molecular formula selected from the group consisting of —

OH and —

YOH where Y is an atom or group of atoms having a bivalent bond.

8. The system according to claim 7, wherein the proton dissociative group is selected from the group consisting of —

OH, —

OSO₃H, —

COOH, —

SO₃H, —

OPO(OH)₂, and —

C₆H₄—

SO₃H.

9. The system according to claim 1, wherein the fullerene molecules are spherical shell-like cluster molecules expressed by a molecular formula C_m where m is a natural number allowing C_m to form a spherical shell structure.