Abstract: An apparatus for electrochemical treatment of wastewater has at least one electrolysis cell through which the wastewater to be treated is guided. The electrolysis cell has a multitude of electrode assemblies that have electrodes arranged such that the wastewater to be treated is guided through holes in the electrodes. At least one of the electrode assemblies has three electrodes arranged such that the wastewater to be treated is guided through all the electrodes.

Abstract: Methods and systems for reducing a redox active contaminant in a waste stream in a waste treatment system involve performing a unit process of the waste treatment system by contacting redox active contaminant in the waste stream with oxyhydrogen-rich gas generated on-site by an oxyhydrogen gas generator that implements water dissociation technology. The oxyhydrogen gas generator involves applying a pulsed electrical signal to a series of closely spaced electrodes that are submerged in the waste stream to produce oxyhydrogen-rich gas from a water component of the waste stream. Operation of the oxyhydrogen gas generator in the waste stream may accomplish one or more unit processes for waste treatment, such as oxidation, stripping, floatation, disinfection, conditioning, stabilization, thickening, and dewatering, among others.

Abstract: A chemical-free and no-microbe method for pre-treating a broad range of waste waters is presented. The said method involves electrocoagulation (EC) operated in synchronization with electrolytic ozone (EO3). In the combinatory method, each technique not only applies its own treatments, they also create synergistic effects from real-time reactions among the reagents generated by electrolysis. Two refractory waste waters, seawater and tannery effluent, are tested by the combinatory method, EC+EO3, to assess the viability of the said method. Without adjustment, each of the said waste waters is remedied by EC+EO3 from its raw state to a clean condition more effectively and more economically than that can be delivered by the respective prevailing processes of pretreatment for each of the said waste waters.

Abstract: An anode device for an electro-f locculation cell, is provided comprising a bed of metal granules (1c) through which raw water is flown from the bottom to the top, is loosely provided in a cell box (3) out of insulating material on an electrically conducting electrode (1) plate provided with insulating material nozzles (Da1-Dc1) and serving as current feeding means to the metal granules (1c), further comprising non-conducting, hydraulic tube connections (6a-6c) which are provided from the insulating material nozzles (Da1-Dc1) to outlet sockets of the tubular manifold (7) for raw water, and at least two gas injectors (9) for the supply of driving a gas which are protruding into the tubular manifold (7) and are connected to a gas supply device (8), wherein fluid connections for the driving gas and the raw water are provided from the outlet sockets (7a1-7c1) of the tubular manifold (7) through to the non-conducting tube connections and the insulating material nozzles to the metal granules (Ic) provided within th

Abstract: The present invention provides a high volume, foul-resistant electrolytic process for treating contaminated water comprising at least one upflow electroflocculation cell consisting of (i) a lower (or “bottom”) electrode (3) in form of a porous, non-fluidized bed of loose iron or aluminium granules kept in periodic motion by pulsed gas injections and (ii) an upper (or “top”) vibrating electrode (4) made of an iron or aluminium grid mesh or ribmesh. A voltage potential between the upper (4) and lower (3) electrode causes ions to be released from the moving electrodes. These ions oxydise and/or render insoluble contaminants in the ascending flow of wastewater and create easy filterable insoluble contaminants resulting in substantially cleansed water. Such moving electrodes electroflocculation cells are useful at municipal water works and commercial and industrial applications were large amounts of raw water have to be processed.

Abstract: An apparatus and a method for electrochemical modification of liquid streams using at least one anode and cathode assemblies arranged to contain liquid electrolytes anolyte and catholyte, a plurality of electrically conducting anode and cathode particulates forming anode and cathode particulate beds, and current feeder and current collector devices in contact with the particulate bed, where the anode particulates and cathode particulates are in motion substantially independent of bulk electrolytes flow.

Abstract: A nanoporous insulating oxide deionization device, method of manufacture and method of use thereof for deionizing a water supply (such as a hard water supply), for desalinating a salt water supply, and for treating a bacteria-containing water supply. The device contains two composite electrodes each constructed from a conductive backing electrode and a composite oxide layer being an insulating oxide or a non-insulating oxide and an intermediate porous layer. The composite layer being substantially free of mixed oxidation states and nanoporous and having a median pore diameter of 0.5-500 nanometers and average surface area of 300-600 m2/g. The composite layer made from a stable sol-gel suspension containing particles of the insulating oxide, the median primary particle diameter being 1-50 nanometers.

Abstract: A method for electrochemical modification of liquid streams employing an electrolytic cell which utilizes an oxidation site defined by an anode, an anode compartment comprising liquid electrolyte anolyte where oxidation is effected, a cathode compartment comprising liquid electrolyte catholyte where reduction is effected, a cathode comprising conducting cathode particulates forming a cathode particulates bed and a current feeder device in at least intermittent contact with said cathode particulates where the cathode particulates are in motion and the particulates motion is substantially independent of bulk electrolyte flow, a separator which confines the cathode particulates to the cathode compartment, constrains electrolyte flow through the cathode particulates bed and permits ionic conduction of current between the anode and cathode, a cathode particulates conveyance system that manipulates cathode particulates motion.

Abstract: The present invention provides a high volume, foul-resistant electrolytic process for treating contaminated water comprising at least one upflow electroflocculation cell consisting of (i) a lower (or “bottom”) electrode (3) in form of a porous, non-fluidized bed of loose iron or aluminium granules kept in periodic motion by pulsed gas injections and (ii) an upper (or “top”) vibrating electrode (4) made of an iron or aluminium grid mesh or ribmesh. A voltage potential between the upper (4) and lower (3) electrode causes ions to be released from the moving electrodes. These ions oxydise and/or render insoluble contaminants in the ascending flow of wastewater and create easy filterable insoluble contaminants resulting in substantially cleansed water. Such moving electrodes electroflocculation cells are useful at municipal water works and commercial and industrial applications were large amounts of raw water have to be processed.

Abstract: An electrochemical process, for removing or modifying ions in solution, incorporates an electrolytic cell comprising a bipolar bed of conductive and non-conductive cell particulate material spaced between two electrodes across which an electrical voltage is applied causing the removal or modification of the ions. A certain minimum of non-conductive particulates in the bed is required to prevent the bed from shunting. The solution contains anions or cations or both, which are to be destroyed, transformed to other species, plated onto the electrode or otherwise modified. The bed acts as a bipolar electrode because it contains both positively and negatively charged sites so that the cations migrate to the negatively charged sites and the anions to the positively charged sites to undergo electrochemical reactions. The electric current in the cell can flow in either direction to achieve the same result so an alternating current is as effective as a direct current.

Abstract: A method for separating contaminants from a aqueous source containing contaminants. In one embodiment, the method involves the use of a high powdered oxidant dissolved within the aqueous system. The gas is dissolved within a reservoir in the aqueous solution and the pressure within the reservoir is controllable. This allows maximum contact of the oxidizing dissolved gas with the contaminant material. Once oxidized, the outlet of the reservoir is adapted to permit hydraulic cavitation. The net effect of the cavitation is to induce a foam formation which foam transports a floc into a separate phase from the aqueous solution. In this manner, the process is effectively a dissolved oxidizing gas mass transfer process. In another embodiment, the process may be augmented by electrocoagulation. This involves the use of an electric cell which is disposed within the reservoir containing the oxidant material.

Abstract: A method and apparatus for purifying aqueous effluent streams to reduce chemical oxygen demand thereof, where the method comprises direct oxidation of water-soluble organic material in an electrochemical cell that incorporates stainless steel electrodes, whose stability and lifetime are enhanced by inclusion of circulating metal chips.

Abstract: A method and apparatus for purifying aqueous effluent streams to reduce chemical oxygen demand thereof, where the method comprises direct oxidation of water-soluble organic material in an electrochemical cell that incorporates stainless steel electrodes, whose stability and lifetime are enhanced by inclusion of circulating metal chips.

Abstract: A method of reducing scale formation in an aqueous solution using an electrolysis apparatus which has, in an electrolysis chamber, at least two electrodes and a bipolar electrode between the two electrodes includes feeding an aqueous solution to the electrolysis chamber, applying either a DC potential to the two electrodes so that one electrode is an anode and the other electrode is a cathode and reversing the polarity of the electrodes at intervals so that the composition of the aqueous solution remains essentially unchanged, or applying an AC potential to the two electrodes, producing, after the aqueous solution has passed through the electrolysis chamber, a treated aqueous solution having a significantly reduced tendency to form scale.

Abstract: A system for treating dissolved halogenated organic compounds in groundwater that relies upon electrolytically-generated hydrogen to chemically reduce the halogenated compounds in the presence of a suitable catalyst. A direct current is placed across at least a pair, or an array, of electrodes which are housed within groundwater wells so that hydrogen is generated at the cathode and oxygen at the anode. A pump is located within the well housing in which the cathode(s) is(are) located and draws in groundwater where it is hydrogenated via electrolysis, passes through a well-bore treatment unit, and then transported to the anode well(s) for reinjection into the ground. The well-bore treatment involves a permeable cylinder located in the well bore and containing a packed bed of catalyst material that facilitates the reductive dehalogenation of the halogenated organic compounds by hydrogen into environmentally benign species such as ethane and methane.

Abstract: In a water purification system for purifying raw water with a first d.c. voltage is applied between a conductive adsorber portion (20) and a primary electrode (27) in the raw water, a second d.c. voltage higher than the first d.c. voltage is applied in place of the first d.c. voltage at intervals between the adsorber portion and the primary electrode to accelerate generation of chlorine from the raw water. The primary electrode is opposite to the adsorber portion with a particular space left therebetween. It is preferable that the adsorber portion is provided with a supplementary electrode (29) which is opposite to the primary electrode so that the particular space is left therebetween.

Abstract: A water treating apparatus for treating water, includes: an oil drop separator for separating oil drops from water to be treated which has an electrode in which an anode is made of amphoteric metal, a power source for supplying an electric power to the electrode, a treating tank for housing the electrode and the water, a water inlet through which the water is led to the treating tank, and a water outlet through which the treated water is exhausted from the treating tank; and a three-dimensional fixed bed type electrolytic tank for treating the water which has been treated by the oil drop separator which has a fixed bed type electrode, a power source for supplying an electric power in which a polarity is reversed periodically, to the fixed bed type electrode, a treating tank for housing the fixed bed type electrode and the water, a water inlet through which the water is led to the treating tank, and a water outlet through which the treated water is exhausted from the treating tank.

Abstract: Method for recovering etchant from etching waste liquid 11 containing iron chloride is disclosed, wherein iron powder is mixed with iron chloride waste solution containing metal ions having a lesser ionization tendency than iron ion in an mixing vessel so as to cause a reaction between the iron powder and the metal ions and remove the precipitated metal from the iron chloride waste solution.

Abstract: An electrically regeneratable electrochemical cell (30) for capacitive deionization and electrochemical purification and regeneration of electrodes includes two end plates (31, 32), one at each end of the cell (30). Two end electrodes (35, 36) are arranged one at each end of the cell (30), adjacent to the end plates (31, 32). An insulator layer (33) is interposed between each end plate (31, 32) and the adjacent end electrode (35, 36). Each end electrode (35, 36) includes a single sheet (44) of conductive material having a high specific surface area and sorption capacity. In one embodiment, the sheet (44) of conductive material is formed of carbon aerogel composite. The cell (30) further includes a plurality of generally identical double-sided intermediate electrodes (37-43) that are equidistally separated from each other, between the two end electrodes (35, 36).

Abstract: Applying electrical energy to a microorganism through a liquid, gas or solid having electrical energy causes an increase in an electric charge in excess of the limit of intracellular and extracellular electrostatic capacity possessed by the microorganism, which results in an irreversible change in the microorganism cells and/or explosively destroys the border membrane of the microorganism cells.

Abstract: Treatment of halogenated hydrocarbon contaminants in groundwater is accomplished by passing the water through a bed of granular iron (43). An electrical circuit (47) is promoted for providing electrons for reducing the contaminant. The circuit may be made using a DC supply, by configuring an electrolytic circuit, or by providing a layer of a second metal such as zinc placed next to the iron bed, thereby creating a galvenic circuit.

Abstract: The present invention relates to an electrolysis cell for percolating a solution in order to perform a chemical reaction, such as the cathodic reduction of a metal cation.This cell includes for example a bed of cathodically biased particles 31, a plurality of counter-electrodes 33, located at the periphery of the bed of particles and anodically biased and an additional counter-electrode 38, anodically biased and located at the center of the bed.This arrangement allows to modify the electrode potential inside the bed, in order to avoid the unwanted electrochemical reactions.

Abstract: A method for treating water with an electrolytic cell including an anode, a cathode, and a three-dimensional carbon electrode provided between the anode and the cathode, the method comprising the steps of supplying the water having an electric resistivity of not less than 10 M.OMEGA..multidot.cm into the electrolytic cell; applying an electric current to the anode and the cathode so as to polarize the electrodes for sterilizing the water, wherein a first distance between the electrode and the anode and a second distance between the electrode and the cathode are not more than 1.0 mm.

Abstract: A water dispenser including a water tank for storing water supplied from a water bottle; an electrolytic cell including an anode, a cathode, and a three-dimensional carbon electrode provided between the anode and the cathode, the electrolytic cell being provided downstream of the water tank; a water outlet valve provided downstream of the electrolytic cell; and a power supply for applying an electric current to the anode so as to polarize the electrode for sterilizing the water.

Abstract: Waste water is purified by passing through a vessel in which small particles of insoluble cathodes interact with anodes to form galvanic couples. During this process, chemical reduction of ions of heavy metals in the water occurs by ions and hydroxides formed during electrochemical dissolution of anodes. The hydroxides are an excellent coagulating agent which absorbs impurities contained in the water. Pressurized air can saturate the waste water simultaneously with passing through the vessel with anodes in order to produce process floatation using hydroxides as coagulant. The temperature of the waste water can be increased in order to intensity the process of treatment.

Abstract: A waste solution containing electroactive species, e.g., metal ions, can be remediated to very low levels of contaminant by an electrolysis method including the steps of introducing an electrolyte containing an electroactive species into an electrolytic cell having a cathode and an anode, producing a flow of the electrolyte past at least one of the electrodes at an electrolyte flow rate, and passing an electric current through the solution between the anode and the cathode whereby the electroactive species undergoes an electrochemical reaction at one of the electrodes at an electrochemical reaction rate, using an electric current pulsed at a frequency of 0.5 to 1000 Hertz and a duty cycle of not greater than 50%, and adjusting the electrolyte flow rate for the pulsed current electrolysis such that the electrochemical reaction rate for pulsed current electrolysis is greater than the electrochemical reaction rate for direct current electrolysis.

Abstract: A process for purifying streams which contain organic and/or inorganic impurities is disclosed. The stream to be treated is introduced into a water-containing reaction zone which includes a packed bed of activated carbon to which an electrochemical potential is applied and to which ozone or hydrogen is fed at the same time. The cell further uses a contact electrode placed in the packed bed for supplying or removing an electrical current, and a counterelectrode disposed in a reaction vessel. The counterelectrode is electrically insulated from the packed bed of activated carbon. The cell further includes an inlet for feeding in liquid to be treated, an inlet for feeding ozone or hydrogen gas, and an outlet for discharging treated liquid and a further outlet for discharging waste gas.

Abstract: Apparatus and method for removing contaminants from an aqueous medium. The apparatus includes a fluidized bed of metallic particles through which the medium is flowed and through which an electric current is applied by electrodes for agglomerating contaminants in the medium. In order to allow the electrodes to be non-consumable so that they do not require frequent replacement, the particles are consumable.