A bipolar plate includes at least one electrically conductive plate having an anode flow field on an anode major side and a cathode flow field on a cathode major side opposite to the anode major side, an electrically insulating first capping plate containing a first plenum area, and located over the anode major side, and an electrically insulating second capping plate containing a second plenum area, and located over the cathode major side. The at least one electrically conductive plate, the first capping plate and the second capping plate are bonded to each other.

A bipolar plate includes at least one electrically conductive plate having an anode flow field on an anode major side and a cathode flow field on a cathode major side opposite to the anode major side, an electrically insulating first capping plate containing a first plenum area, and located over the anode major side, and an electrically insulating second capping plate containing a second plenum area, and located over the cathode major side. The at least one electrically conductive plate, the first capping plate and the second capping plate are bonded to each other.

An electrochemical device, configured for electric power storage, including: a reactor, the wall of the reactor being configured to form a first electrode, the reactor being provided with an electrolyte inlet and an electrolyte outlet, a central electrode arranged in the centre of the reactor, additional electrodes E.sub.x, with x an integer ranging from 1 to n, the additional electrodes E.sub.x being tubular and arranged around the central electrode.

A separator plate for an electrochemical system has two metal individual plates. The plates have passage openings for operating media and possibly coolant, and distribution structures. The distribution structures are formed in the metal individual plates and which each communicate with at least two of the passage openings. A peripherally extending sealing structure is formed in each of the metal individual plates at least peripherally around the electrochemically active region and at a distance therefrom and/or peripherally around at least one of the passage openings and at a distance from the edge thereof. The cross-section of the sealing structure has a bead roof, two bead flanks, and at least in some segments, two bead feet. At least in the region of the bead roof of the sealing structure at least in some segments, the sealing structure extends sinuously with at least two wave periods having convex and concave segments.

The invention essentially consists of proposing a novel reactor or fuel cell architecture having an active section of the catalytic material for methanation or reforming reaction integrated into the electrode which varies with the composition of the gases, as they are distributed in accordance with the electrochemistry on said electrode.

The invention essentially consists of proposing a novel reactor or fuel cell architecture having an active section of the catalytic material for methanation or reforming reaction integrated into the electrode which varies with the composition of the gases, as they are distributed in accordance with the electrochemistry on said electrode.

Bipolar electrochemistry (BPE) concepts are used to provide a single-step and controllable process for simultaneously exfoliating a graphite source and depositing both graphene oxide and reduced graphene oxide layers on conductive substrates. A bipolar electrochemical cell can be used for a three-in-one deposition and can include two wired pieces of graphite to monitor the amount of current that passes through the bipolar electrode.

Bipolar electrochemistry (BPE) concepts are used to provide a single-step and controllable process for simultaneously exfoliating a graphite source and depositing both graphene oxide and reduced graphene oxide layers on conductive substrates. A bipolar electrochemical cell can be used for a three-in-one deposition and can include two wired pieces of graphite to monitor the amount of current that passes through the bipolar electrode.

A chlorination electrolyser having a housing provided with an inlet and an outlet suitable for the circulation of brine; at least one pair of bipolar electrodes facing each other and positioned within said housing. Each bipolar electrode of the at least one pair has a valve metal substrate; an active coating comprising at least one layer of a catalytic composition comprising ruthenium and titanium disposed over the substrate; a top coating having at least one layer composed of oxides of tantalum, niobium, tin, or combinations thereof disposed over the active coating. A self-cleaning electrochlorination system having the an electrolyser, a method for its production, its use in normal and low salinity pools for hypochlorite mediated water disinfection and a method for hypochlorite-mediated water disinfection.

A chlorination electrolyser having a housing provided with an inlet and an outlet suitable for the circulation of brine; at least one pair of bipolar electrodes facing each other and positioned within said housing. Each bipolar electrode of the at least one pair has a valve metal substrate; an active coating comprising at least one layer of a catalytic composition comprising ruthenium and titanium disposed over the substrate; a top coating having at least one layer composed of oxides of tantalum, niobium, tin, or combinations thereof disposed over the active coating. A self-cleaning electrochlorination system having the an electrolyser, a method for its production, its use in normal and low salinity pools for hypochlorite mediated water disinfection and a method for hypochlorite-mediated water disinfection.