Thermal spray coating processes using HHO gas generated from an electrolyzer generator
A thermal spray coating process for depositing finely divided metallic or nonmetallic materials in a molten or semi-molten condition to form a coating on a substrate wherein the coating material may be powder, ceramic-rod, wire or molten materials. The process involves the use of a gas made from water in an electrolyzer, which includes two principal electrodes and a plurality of supplemental electrodes. The supplemental electrodes are not connected electrically to a power source. The electrolyzer is adapted to separate the water such that its constituents of H and O are not recombined and instead produced jointly to make the single combustible gas composed of combinations of clusters of hydrogen and oxygen atoms structured according to a general formula H m O n wherein m and n have null or positive integer values with the exception that m and n can not be 0 at the same time.
1 . A thermal spray coating process for depositing finely divided metallic or nonmetallic materials in a molten or semi-molten condition to form a coating on a substrate wherein the coating material may be in the form of powder, ceramic-rod, wire or molten materials, the process comprising:
using in the thermal spray coating process a gas made from water in an electrolyzer for the separation of water as a fuel and heat source, wherein said gas is used as an additive or supplemental source of said fuel and heat source to another fuel and heat source or is used as a sole source of said fuel and heat source, the electrolyzer comprising:
an aqueous electrolytic solution comprising water, the aqueous electrolyte solution partially filling an electrolysis chamber such that a gas reservoir region is formed above the aqueous electrolyte solution, said chamber being adapted to be installed in a pressurized system;
two principal electrodes comprising an anode electrode and a cathode electrode, the two principal electrodes being at least partially immersed in the aqueous electrolyte solution;
a plurality of supplemental electrodes at least partially immersed in the aqueous electrolyte solution and interposed between the two principal electrodes wherein the two principal electrodes and the supplemental electrodes are held in a fixed spatial relationship, and wherein the supplemental electrodes are not connected electrically to a power source;
for each supplemental adjacent electrodes, one is made of a high porosity latticed foam material made substantially of a nickel material and the opposing electrode is made substantially of a stainless steel material; and
said electrolyzer being adapted to separate the water such that its constituents of H and O are not recombined and instead produced jointly to make the single combustible gas composed of combinations of clusters of hydrogen and oxygen atoms structured according to a general formula H m O n wherein m and n have null or positive integer values with the exception that m and n can not be 0 at the same time.
2 . The process according to claim 1 , wherein said high porosity latticed foam material contains greater than 99% nickel.
3 . The process according to claim 1 , wherein the combustible gas produced when lighted as a flame in open air burns with a flame temperature at its core in said open air of from about 255° F. to about 288° F.
4 . The process according to claim 2 , wherein when the flame comes into contact with a target material, said combustible gas does combine by sublimation creating a catalyzing effect with the target material being impinged by the combustible gas flame that results in a rapid melting of the target material being impinged, which temperatures are dramatically increased by the sublimation and catalyzing effects of the gas flame on the target material.
5 . The process according to claim 4 , wherein said temperatures vary depending on the target material being impinged by the combustible gas flame, wherein said target material is selected from refractive materials consisting of carbon steel, tungsten, bricks and ceramic materials.
6 . The process according to claim 4 , wherein said temperatures vary depending on a percentage of mixture of the HHO gas with the other fuel and heat source being used in the process.
7 . The process according to claim 1 , wherein the two principal electrodes and the one or more supplemental electrodes are separated by a distance of about 0.15 to about 0.35 inches.
8 . The process according to claim 1 , further comprising:
routing the gas though a magnetic centrifuge prior to introducing the gas in the thermal spray process being used.
9 . The process according to claim 1 , wherein the thermal spray coating process is a plasma thermal spray process.
10 . The process according to claim 1 , wherein the thermal spray coating process is a detonation thermal spray process.
11 . The process according to claim 1 , wherein the thermal spray coating process is a high velocity oxygen fuel thermal spray process.
12 . The process according to claim 1 , wherein the thermal spray coating process is a low velocity oxygen fuel thermal spray process.
13 . The process according to claim 1 , wherein the thermal spray coating process is a combustion wire thermal spray process.
14 . The process according to claim 1 , wherein the thermal spray coating process is a combustion powder thermal spray process.
15 . The process according to claim 1 , wherein the thermal spray coating process is an arc wire thermal spray process.
16 . The process according to claim 1 , wherein the supplemental electrodes are connected to a power source.