System and method for electrolysis and heating of water

• US 5,616,219 A
• Filed: 06/13/1995
• Issued: 04/01/1997
• Est. Priority Date: 06/13/1995
• Status: Expired due to Fees

• Current Assignee: James A. Patterson
• Original Assignee: James A. Patterson
• Inventors: Patterson, James A.
• Primary Examiner(s): Gorgos, Kathryn
• Assistant Examiner(s): Mee, Brendan
• Application Number:
  US08/489,894
• Time in Patent Office: 658 Days
• Field of Search: 204/242, 204/249, 204/1.11, 204/239, 204/241
• US Class Current: 204/241
• CPC Class Codes: F24V 99/00 Subject matter not provided for in other main groups of this subclass
• CPC Class Codes: G21B 3/00 Low temperature nuclear fusion reactors, e.g. alleged cold fusion reactors
• CPC Class Codes: Y02E 30/10 Nuclear fusion reactors

Abstract

A system and method for electrolysizing and/or heating a liquid electrolyte containing water having a conductive salt in solution and for producing excess heat within the water for use. An electrolytic cell includes a non-conductive housing having an inlet and an outlet and spaced apart first and second conductive foraminous grids connected within the housing. A plurality of microspheres each having improved conductive exterior multi-layers of uniform thickness are positioned within the housing in electrical contact with the first grid adjacent the inlet. The conductive microspheres are plated first with a metal cation which will reduce with hydrazine to form a conductive metal flash coating. The microspheres are then plated with a uniform layer of nickel, followed by plated layer of metallic hydride which is readily combinable with hydrogen or an isotope of hydrogen, then a uniform metallic support plating having a high hydrogen diffusion rate and a low hydride formation ratio. An electric power source in the system is operably connected across the first and second grids whereby electrical current flows between the grids within the liquid electrolyte. Heat is added to the water to elevate system electrolyte operating temperature for increased yields of heat for use.

Claims

1. A system for electrolysis and heating of a liquid electrolyte within an electrolytic cell comprising:

said electrolytic cell including a non-conductive housing and an inlet and an outlet;

a first conductive foraminous grid positioned within said housing adjacent to said inlet;

a second conductive foraminous grid positioned within said housing spaced from said first conductive grid and adjacent to said outlet;

a plurality of conductive beads each having a conductive metallic surface which will combine with hydrogen or an isotope of hydrogen to form a metallic hydride, said conductive beads in electrical communication with said first conductive grid end electrically isolated from said second grid;

means for pumping said liquid electrolyte into said electrolytic cell through said inlet, said electrolyte having a conductive salt in solution with water;

means for heating said liquid electrolyte external to said electrolytic cell as said liquid electrolyte flows through said system;

an electric power source operably connected to said first and second grids

wherein each said conductive bead includes;

a conductive metal flash coating of uniform thickness formed by chemical combination with a cation exchange surface of a spherical cross-linked polymer microbead from a metal cation which has been chemically reduced with hydrazine;

a nickel layer of uniform thickness formed atop said flash coating;

a metallic hydride forming layer of uniform thickness formed atop said nickel layer;

a metallic support layer of uniform thickness formed atop said metallic hydride forming layer.

2. A system as set forth in claim 1, wherein:

said conductive salt comprises an element from the group consisting of lithium, boron, aluminum, gallium and thallium.

3. A system as set forth in claim 1, wherein said electrolytic cell further comprises:

a foraminous non-conductive mesh positioned within said housing adjacent to and spaced from said second grid;

said electrolytic cell being in an upright position and said conductive beads are loosely packed within said electrolytic cell;

said conductive beads being elevated and mixed above said first grid by said electrolyte, said non-conductive mesh preventing said conductive beads from contacting said second grid.

4. A system as set forth in claim 1, wherein:

each said conductive bead is sized in the range of about 1 mm or less in diameter.

5. A system as set forth in claim 1, wherein:

said liquid electrolyte includes a heavy water.

6. A system as set forth in claim 5, wherein:

said heavy water is deuterium oxide (D₂ O).

7. A system as set forth in claim 1, wherein:

said metallic hydride forming layer is taken from the group consisting of;

palladium, lanthanum, praseodymium, cerium, titanium, zirconium, vanadium, tantalum, uranium, hafnium and thorium.

8. A system as set forth in claim 1, wherein each said conductive bead further includes:

a metallic stabilizer layer of uniform thickness formed atop said support layer.

9. A system as set forth in claim 1, wherein:

said flash coating has a thickness in the range of 1 to 10 angstroms;

said nickel layer and said support layer each have a thickness in the range of about 10 angstroms to 1 micron;

said metallic hydride forming layer has a thickness in the range of about 10 angstroms to 2 microns;

said metallic stabilizer layer has a thickness in the range of about 1 to 60 angstroms.

10. A system as set forth in claim 1, wherein:

said flash coating is taken from the group consisting of;

copper, palladium, nickel and titanium;

said metallic hydride forming layer is taken from the group consisting of;

palladium, lanthanum, praseodymium, cerium, titanium, zirconium, vanadium, tantalum, uranium, hafnium and thorium;

said support layer is taken from the group consisting of;

nickel, gold, silver and titanium; and

said metallic stabilizer layer is taken from the group consisting of;

chromium, iron, cobalt and nickel.

11. A system as set forth in claim 1, further comprising:

a plurality of non-metallic beads each having a sulfonated surface which has been ion exchanged with a lithium salt;

said plurality of non-metallic beads positioned between said second grid and said conductive beads;

said plurality of non-metallic beads forming a conductive salt bridge thereacross.

12. A system for producing useful excess heating of a liquid electrolyte which is heated while flowing through an electrolytic cell, said system comprising:

said electrolytic cell including a non-conductive housing an inlet and an outlet;

a first conductive foraminous grid positioned within said housing adjacent to said inlet;

a second conductive foraminous grid positioned within said housing spaced from said first conductive grid and adjacent to said outlet;

a plurality of conductive beads each having a conductive metallic surface which will combine with hydrogen or an isotope of hydrogen to form a metallic hydride, said conductive beads in electrical communication with said first conductive grid and electrically isolated from said second grid;

means for pumping said liquid electrolyte into said electrolytic cell through said inlet, said electrolyte having a conductive salt in solution with water;

means for heating said liquid electrolyte external to said electrolytic cell as said liquid electrolyte flows through said system;

an electric power source operably connected to said first and second grids

wherein each said conductive bead includes;

a conductive metal flash coating of uniform thickness formed by chemical combination with a cation exchange surface of a spherical cross-linked polymer microbead from a metal cation which has been chemically reduced with hydrazine;

a nickel layer of uniform thickness formed atop said flash coating;

a metallic hydride forming layer of uniform thickness formed atop said nickel layer;

a metallic support layer of uniform thickness formed atop said metallic hydride forming layer.

13. A system as set forth in claim 12, wherein:

said conductive salt comprises an element from the group consisting of lithium, boron, aluminum, gallium and thallium.

14. A system as set forth in claim 12, wherein said electrolytic cell further comprises:

p1 a foraminous non-conductive mesh positioned within said housing adjacent to and spaced from said second grid;

said electrolytic cell being in an upright position and said conductive beads are loosely packed within said electrolytic cell;

said conductive beads being elevated and mixed above said first grid by said electrolyte, said non-conductive mesh preventing said conductive beads from contacting said second grid.

15. A system as set forth in claim 12, wherein:

each said conductive bead is sized in the range of about 1 mm or less in diameter.

16. A system as set forth in claim 12, wherein:

said liquid electrolyte includes a heavy water.

17. A system as set forth in claim 12, wherein:

said liquid deuterium oxide (D₂ O).

18. A system as set forth in claim 12, wherein:

said metallic hydride forming layer is taken from the group consisting of;

palladium, lanthanum, praseodymium, cerium, titanium, zirconium, vanadium, tantalum, uranium, hafnium and thorium.

19. A system as set forth in claim 12, wherein each said conductive bead further includes:

a metallic stabilizer layer of uniform thickness formed atop said support layer.

20. A system as set forth in claim 12, wherein:

said flash coating has a thickness in the range of 1 to 10 angstroms;

said nickel layer and said support layer each have a thickness in the range of about 10 angstroms to 1 micron;

said metallic hydride forming layer has a thickness in the range of about 10 angstroms to 2 microns;

said metallic stabilizer layer has a thickness in the range of about 1 to 60 angstroms.

21. A system as set forth in claim 12, wherein:

said flash coating is taken from the group consisting of;

copper, palladium, nickel and titanium;

said metallic hydride forming layer is taken from the group consisting of;

palladium, lanthanum, praseodymium, cerium, titanium, zirconium, vanadium, tantalum, uranium, hafnium and thorium;

said support layer is taken from the group consisting of;

nickel, gold, silver and titanium; and

said metallic stabilizer layer is taken from the group consisting of;

chromium, iron, cobalt and nickel.

22. A system as set forth in claim 12, further comprising:

a plurality of non-metallic beads each having a sulfonated surface which has been ion exchanged with a lithium salt;

said plurality of non-metallic beads positioned between said second grid and said conductive beads;

said plurality of non-metallic beads forming a conductive salt bridge thereacross.