Electrolytic cells for hydrogen gas production

Claim 2

A bank of electrolytic cell for electrolytically converting water into its constituent gases of hydrogen and oxygen upon the application of a voltage source comprising: two end plate electrodes, a plurality of intermediate electrodes spaced between said end plate electrodes, a plurality of dielectric separators individually spacing and electrically separating adjacent electrodes from one another and together with the said electrodes forming impervious electrolytic cell chambers between adjacent electrodes, pressure developing in said chamber during the converting of water into hydrogen and oxygen, a plurality of gas separator diaphragms individually spaced between adjacent electrodes to divide each said electrolytic cell chamber into two sections to prevent the remixing of hydrogen and oxygen, alkaline electrolyte contained in each cell chamber, means for connecting a voltage source to said electrodes, means for introducing water to each of said electrolytic cell chambers, first manifold means connected with like sections of each of said electrolytic cell chambers for allowing off-gas withdrawal of hydrogen, first automatic valve means for closing said first manifold whenever the pressure within said electrolytic cell chambers is equal to or less than a preselected pressure, second manifold means connected with the other like sections of each electrolytic cell chambers for allowing off-gas withdrawal of oxygen, second automatic valve means for closing said second manifold means whenever pressure within said electrolytic cell chambers is equal to or less than preselected pressure, means for back-pressuring the exterior walls of each end plate electrode to counter-balance any pressure developed within the adjacent electrolytic cell chambers and exerted against the inside wall of the end plate electrodes.

Claim 3

The modular bank of claim 1 wherein said intermediate electrodes are clad with a thin sheet of stainless steel to obviate electrode corrosion and provide a surface for the evolution and break away of gas bubbles and wherein said dialectric separators are formed of fluorinated ethylene-propylene.

Claim 4

The modular bank of claim 1 wherein said dialectric separators are adhered to said stainless steel electrode surfaces by a hot-melt process practiced at a temperature greater than 1000° R. and at a pressure greater than 25 psig.

Claim 5

The modular bank of claim 1 wherein said gas separator diaphragm is formed of two layers of finely woven glass fabric which permits the free migration of electrolyte through said diaphragm.

Claim 6

The modular bank of claim 1 wherein said electrolyte is 15% NAOH.

Claim 7

The modular bank of claim 1 wherein said electrolyte comprises 25% KOH.

Claim 8

The modular bank of claim 1 wherein said first manifold means includes a manifold filled with compressed glass wool to offer a surface area for plating out of liquids carried by off-gas.

Claim 9

The modular bank of claim 1 wherein said back-pressuring means comprises a material adhered to the exterior wall of each end plate to form pressure pockets and back-pressure manifold connected to said pressure pockets.

Claim 10

The modular bank of claim 8 wherein said back-pressure manifold is connected with said second manifold means.

Claim 11

The modular bank of claim 1 wherein said connecting means comprise extensions of said end plate electrodes for connection to DC power bus bars.

Claim 12

The modular bank of claim 1 wherein said bank includes means for permitting operation at temperatures up to 810° R. and pressures up to 1000 psig.

Claim 13

A bank of electrolytic cells for electrolytically converting water into its constituent gases of hydrogen and oxygen upon the application of a voltage source and for producing hydrogen at a pressure equal to or greater than the working pressure of a gas transmission line comprising: two end plate electrodes, a plurality of intermediate, bipolar planar electrodes spaced between said end plate electrodes, said intermediate electrodes being clad with a thin sheet of stainless steel to obviate electrode corrosion and provide a surface for the evolution and break-away of gas bubbles, a plurality of dielectric separators spacing and electrically separating adjacent electrodes from one another and together with said electrodes forming impervious electrolytic cell chambers capable of withstanding pressures equal to or greater than the gas transmission pressure, a plurality of gas separator diaphragms individually spaced between adjacent electrodes to divide each said electrolytic cell chamber into two sections to prevent the remixing of hydrogen and oxygen, alkaline electrolyte contained in each cell chamber, means for connecting a voltage source to said electrodes, means for introducing water to each of said electrolytic cell chambers, first manifold means connected with like sections of each of said electrolytic cell chambers for allowing off-gas withdrawal of hydrogen, first automatic valve means for closing said first manifold means whenever pressure within said electrolytic cell chambers is equal to or less than the working pressure of the gas transmission line, second manifold means connected with the other like sections of each electrolytic cell chamber for allowing off-gas withdrawal of oxygen, second automatic valve means for closing said second manifold means whenever the pressure within said electrolytic cell chambers is equal to or less than the working pressure of the gas transmission line, and means for back-pressuring the exterior walls of each end plate electrode to counter-balance pressure developed within said electrolytic cell chambers and exerted against the inside wall of the end plate electrodes.

Claim 14

A bank of electrolytic cells for electrolytically converting water into its constituent gases of hydrogen and oxygen upon the application of a voltage source and for producing hydrogen at a pressure equal to or greater than the working pressure of a gas transmission line comprising: two end plate electrodes, a plurality of intermediate, bipolar planar electrodes spaced between said end plate electrodes, said intermediate electrodes being clad with a thin sheet of stainless steel to obviate electrode corrosion and provide a surface for the evolution and break-away of gas bubbles, a plurality of dielectric separators spacing and electrically separating adjacent electrodes from one another and together with said electrodes forming impervious electrolytic cell chambers capable of withstanding pressures equal to or greater than the gas transmission pressure, a plurality of gas separator diaphragms individually spaced between adjacent electrodes to divide each said electrolytic cell chamber into two sections to prevent the remixing of hydrogen and oxygen, alkaline electrolyte contained in each cell chamber, means for connecting a voltage source to said electrodes, means for introducing water to each of said electrolytic cell chambers, first manifold means connected with like sections of each of said electrolytic cell chambers for allowing off-gas withdrawal of hydrogen, first automatic valve means for closing said first manifold means whenever pressure within said electrolytic cell chambers is equal to or less than the working pressure of the gas transmission line, second manifold means connected with the other like sections of each electrolytic cell chamber for allowing off-gas withdrawal of oxygen, second automatic valve means for closing said second manifold means whenever the pressure within said electrolytic cell chambers is equal to or less than the working pressure of the gas transmission line, and means for back-pressuring the exterior walls of each end plate electrode to counter-balance pressure developed within said electrolytic cell chambers and exerted against the inside wall of the end plate electrodes.

Claim 15

The modular bank of claim 12 wherein said dielectric separators are formed of fluorinated ethylene-propylene and are adhered to said stainless steel electrode surfaces by a hot-melt process practiced at a temperature greater than 1000° R. and at a pressure greater than 25 psig.