Membraneless direct-type fuel cells

US2019173116A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2019173116-A1
Application numberUS-201616323300-A
CountryUS
Kind codeA1
Filing dateAug 5, 2016
Priority dateAug 5, 2016
Publication dateJun 6, 2019
Grant date

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

The present invention relates to a membraneless direct-type fuel cell, which directly uses oxidizable phosphorus compound, sulphur compound or nitrogen compound as fuel.

First claim

Opening claim text (preview).

1 . A membraneless direct-type fuel cell comprising: (i) An anode configured and arranged for electro-oxidizing a reductant being an oxidizable compound selected from a group consisting of phosphorus compound, sulphur compound, nitrogen compound and any combination thereof, (ii) A cathode configured and arranged for electro-reducing an oxidant, (iii) A solvent, (iv) Optionally an electrolyte, wherein the anode and cathode are spaced apart and the reductant and oxidant freely communicate between the anode and cathode. 2 . The fuel cell according to claim 1 , wherein the oxidizable phosphorus compound is hypophosphorous acid compound or phosphorous acid compound. 3 . The fuel cell according to claim 2 , wherein the hypophosphorous acid compound is selected from a group consisting of hypophosphorous acid, its alkali metal salts, its alkaline earth metal salts, its ammonium salt and any combination thereof; or wherein the phosphorous acid compound is selected from a group consisting of phosphorous acid, its alkali metal salts, its alkaline earth metal salts, its ammonium salt and any combination thereof. 4 . (canceled) 5 . The fuel cell according to claim 1 , wherein the oxidizable sulphur compound is sulphurous acid compound or thiosulfuric acid compound. 6 . The fuel cell according to claim 5 , wherein the sulphurous acid compound is selected from a group consisting of sulphurous acid, its alkali metal salts, its alkaline earth metal salts, its ammonium salt and any combination thereof; or wherein the thiosulfuric acid compound is selected from a group consisting of thiosulfuric acid, its alkali metal salts, its alkaline earth metal salts, its ammonium salt and any combination thereof. 7 . (canceled) 8 . The fuel cell according to claim 1 , wherein the oxidizable nitrogen compound is an amine or is selected from a group consisting of nitrous acid, its alkali metal salts, its alkaline earth metal salts, its ammonium salt and any combination thereof. 9 . (canceled) 10 . The fuel cell according to claim 1 , wherein electrode catalyst for anode or cathode comprises metal element selected from a group consisting of (i) Transition metals, (ii) Lanthanides, (iii) Actinides, (iv) Elements of Groups IA, IIA, IIIA, IVA, VA, VIA, VIIA of Periodic Table and (v) Any combination thereof; or comprises non-metal element selected from a group consisting of elements of Groups IA, IVA, VA, VIA, VIIA of Periodic Table and any combination thereof. 11 . The fuel cell according to claim 10 , wherein the metal element comprised in anode or cathode is in the form of elemental metal, metal alloy, metal oxide or metal complex. 12 . (canceled) 13 . The fuel cell according to claim 1 , wherein anode catalyst comprises an element selected from a group consisting of elements of Groups IIIA, IVA, VA of Periodic Table and Transition metals. 14 . The fuel cell according to claim 1 , wherein anode catalyst comprises an element selected from a group consisting of Pd, Pt, Ru, Ir, Au, Rh, Bi, B or Sn and any combination thereof. 15 . The fuel cell according to claim 1 , wherein cathode catalyst comprises an element selected from a group consisting of elements of Groups IA, IIA, IIIA, IVA, VA, VIA, VIIA of Periodic Table, Transition metals and Lanthanides. 16 . The fuel cell according to claim 1 , wherein cathode catalyst comprises an element selected from a group consisting of Ag, Ni, Ru, Ir, Os, Mn, La, Co, Ce and any combination thereof; or comprises oxide selected from a group consisting of MnO 2 , RuO 2 , CeO 2 , Eu 2 O 3 , Sm 2 O 3 , CoO, Co 3 O 4 , LaNiO 3 , LaCoO 3 and any combination thereof. 17 . (canceled) 18 . The fuel cell according to claim 1 , wherein at least 20 wt % reductant contact the cathode based on total weight of reductant employed or wherein at least 20 wt % oxidant contact the cathode based on total weight of oxidant employed. 19 . The fuel cell according to claim 18 , wherein reductant contacting the cathode is comprised between 20 wt % and 80 wt % based on total weight of reductant employed or wherein oxidant contacting the cathode is comprised between 20 wt % and 80 wt % based on total weight of oxidant employed. 20 . (canceled) 21 . (canceled) 22 . The fuel cell according to claim 1 , wherein the concentration of reductant in solution is preferably comprised between 0.01 M and 12 M. 23 . The fuel cell according to claim 1 , wherein electrode catalyst is applied to a support. 24 . The fuel cell according to claim 1 , wherein the loading of electrode catalyst on substrate is comprised between 0.01 and 500 mg/cm −2 . 25 . The fuel cell according to claim 1 , wherein the distance between the two electrodes is comprised between 0.1 cm and 10 cm. 26 . The fuel cell according to claim 1 , wherein a separator is placed between the anode and cathode. 27 . The fuel cell according to claim 26 , wherein the separator is selected from a group consisting of fibers, polymers and naturally occurring substances.

Assignees

Inventors

Classifications

  • having sulfur, e.g. sulfonated-polyethersulfones [S-PES] · CPC title

  • having nitrogen, e.g. sulfonated polybenzimidazoles [S-PBI], polybenzimidazoles with phosphoric acid, sulfonated polyamides [S-PA] or sulfonated polyphosphazenes [S-PPh] · CPC title

  • with one of the reactants being liquid, solid or liquid-charged (H01M8/12 takes precedence) · CPC title

  • Fuel cells in which the fuel is based on materials comprising carbon or oxygen or hydrogen and other elements; Fuel cells in which the fuel is based on materials comprising only elements other than carbon, oxygen or hydrogen · CPC title

  • H01M8/18Primary

    Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US2019173116A1 cover?
The present invention relates to a membraneless direct-type fuel cell, which directly uses oxidizable phosphorus compound, sulphur compound or nitrogen compound as fuel.
Who is the assignee on this patent?
Rhodia Operations, Univ Fudan
What technology area does this patent fall under?
Primary CPC classification H01M8/18. Mapped technology areas include Electricity.
When was this patent published?
Publication date Thu Jun 06 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).