Improvements in electrolysis systems

C - Chemistry – Metallurgy – 25 – B

Patent

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C25B 1/06 (2006.01) B23K 5/00 (2006.01) B23K 10/00 (2006.01) C25B 1/04 (2006.01) C25B 9/00 (2006.01) C25B 9/18 (2006.01) C25B 11/02 (2006.01) C25B 13/00 (2006.01) F23D 14/28 (2006.01) F23D 14/32 (2006.01) F23D 14/38 (2006.01) F23D 14/82 (2006.01) F23G 7/06 (2006.01) H01M 8/06 (2006.01)

Patent

CA 2171007

A cell arrangement for electrolysis of water to liberate hydrogen and oxygen gases is described. A cell unit (125) has a stacked arrangement of segmentation disks (114), a first type of (anode) cell plates (90), a second type of (cathode) cell plates (98) and separation membranes (116). Interconnecting conductive shafts (126-131) pass through holes (100, 102) of the cell plates (90, 98) to have selective electrical interconnection therewith. Water and electrolyte, are supplied by inlet ports (108, 110) to immerse the cell plates (90, 98). The membranes (116) normally isolate adjacent cathode and anode plates (90, 98) from the mixing of liberated oxygen and hydrogen gases whilst allowing ionic current flow. By selective adjustment of the water/electrolyte pressure differential on respective sides of the separation membranes (116), admixture of the liberated gases can be produced. The liberated gases discharge by outlet ports (104, 106).

Agencement de cellule destiné à l'électrolyse de l'eau et permettant de libérer de l'hydrogène et de l'oxygène. Un ensemble cellule (125) comprend des disques de séparation (114) disposés sous forme de pile, un premier type de plaques (90) (anodiques), ainsi que des membranes de séparation (116). Des tiges conductrices d'interconnexion (126-131) passent à travers des trous (100, 102) ménagés dans les plaques (90, 98) afin de constituer une interconnexion électrique sélective avec ces dernières. De l'eau et un électrolyte sont introduits par des orifices d'entrée (108, 110) afin d'immerger les plaques (90, 98). Les membranes (116) isolent généralement des plaques anodiques et cathodiques adjacentes (90, 98) afin d'éviter le mélange de l'oxygène et de l'hydrogène, tout en permettant le flux de courant ionique. L'ajustement sélectif du différentiel de pression eau/électrolyte sur les côtés respectifs des membranes de séparation (116) permet le mélange des gaz libérés. Ceux-ci sont évacués par des orifices de sortie (104, 106).

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