Abstract:
A method of converting biological material into energy resources includes transmitting biological material to a pulsed electric field (PEF) station, and applying a PEF to the biological material within a treatment zone in the PEF station to generate treated biological material. The method also includes transmitting the treated biological material to a biogenerator, and processing the treated biological material in the biogenerator to produce an energy resource. A converter may carry out this process, and may include the PEF station and the biogenerator.
Abstract:
The treatment of effluents in which a flow of the effluents is subjected to a pulsed electric field that modifies physicochemical and biologic characteristics of the medium, this modification being used during a solid/liquid separation operation, of the settlement or membrane filtration type. The solid/liquid separation operation and the application of a pulsed electric field are operations carried out at different locations along the effluent flow. The pulsed electric field has voltage value, current value, pulse repetition frequency, and voltage front shape characteristics chosen such that the required effluent treatment can be achieved as a function of the locations at which these membrane filtration operations are carried out and a pulsed electric field is applied.
Abstract:
An apparatus to treat an influent solution comprising ions to obtain a selectable ion concentration in an effluent solution. The apparatus comprises an electrochemical cell comprising a housing comprising first and second electrodes. A water-splitting ion exchange membrane is between the first and second electrodes, the membrane comprising ananion exchange surface facing the first electrode, and an cation exchange surface facing the second electrode, or vice versa. The housing also has an influent solution inlet and an effluent solution outlet with a solution channel that allows influent solution to flow past both the anion and cation exchange surfaces of the water-splitting ion exchange membrane to form the effluent solution. A variable voltage supply is capable of maintaining the first and second electrodes at a plurality of different voltages during an ion exchange stage.
Abstract:
Methods and systems for treating a waste stream in a waste treatment system involve performing a unit process of the waste treatment system by contacting 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. At least a portion of the oxyhydrogen-rich gas can be conveyed for a second use in the waste treatment system, such as a source of combustible fuel for incineration or power generation, for example.
Abstract:
Methods and systems for treating a waste stream in a waste treatment system involve performing a unit process of the waste treatment system by contacting the waste stream with oxyhydrogen-rich gas generated on-site by an oxyhydrogen gas generator that implements water dissociation technology. In a preferred embodiment, 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 conditioning, stabilization, thickening, and dewatering, among others. At least a portion of the oxyhydrogen-rich gas can be conveyed for a second use in the waste treatment system, such as a source of combustible fuel for incineration or power generation, for example.
Abstract:
The MPULSE 3000 System (fig C) sends a controlled high frequency (between 3125 and 4250 Times per second), a positive and negative low voltage Impulse between the stainless steel anode and cathode (see Fig B) to create a consistently changing electric Field. The Frequency, Voltage and Amperage are microchip controlled by the conductivity of the water. The MPULSE 3000 System (Fig C) controls the amount of the impulses (between 3125 and 4250 Times per second) utilized in the water to ensure the change from Calcium Bi-Carbonate to Calcium Carbonate and into the non-adherent Crystals (Aragonite). The formed Impulse (110 microsecond positive/32 microsecond break/110 microsecond negative/32 microsecond break), Voltage (16v) and Amperage (70 mA) are precisely calculated to insure that the stainless steel Anode and Cathode (see Fig B) in the water are complete stabilized and will not corrode.
Abstract:
The treatment of effluents in which a flow of the effluents is subjected to a pulsed electric field that modifies physicochemical and biologic characteristics of the medium, this modification being used during a solid/liquid separation operation, of the settlement or membrane filtration type. The solid/liquid separation operation and the application of a pulsed electric field are operations carried out at different locations along the effluent flow. The pulsed electric field has voltage value, current value, pulse repetition frequency, and voltage front shape characteristics chosen such that the required effluent treatment can be achieved as a function of the locations at which these membrane filtration operations are carried out and a pulsed electric field is applied.
Abstract:
Various kinds of wastewater and water such as methane fermentation digestion liquids, domestic wastewater, sewage, service water, culture pond water, wastewater defined by an active sludge law and wastewater from food industries are decomposed, cleaned and treated with a high efficiency with oxygen radicals, hydroxyl radicals and diphenyl para picrihydoral radicals, and injurious materials are decomposed, cleaned and treated by oxidizing and reducing functions. An apparatus for cleaning dissolved organic matters and a trace amount of injurious materials consisting of a anode which is formed or welded by coating clay or glass with a material prepared by mixing 2 to 15% by weight of a transition metal with 1 to 10% of an oxidized transition metal and sintering the glass within a range from 800 to 1500° C. as a glaze or coating a surface of a metal is with a mixture of anatase type titanium oxide, tin oxide, ruthenium oxide and fine particles of platinum as a glaze and sintering the glaze once again at a temperature of 580 to 980° C.
Abstract:
Methods and systems for treating a waste stream in a waste treatment system involve performing a unit process of the waste treatment system by contacting the waste stream with oxyhydrogen-rich gas generated on-site by an oxyhydrogen gas generator that implements water dissociation technology. In a preferred embodiment, 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 conditioning, stabilization, thickening, and dewatering, among others. At least a portion of the oxyhydrogen-rich gas can be conveyed for a second use in the waste treatment system, such as a source of combustible fuel for incineration or power generation, for example.
Abstract:
The invention aims to achieve effective recovery of metals from process solutions and effluents by means of pulsating cathode currents, preferably with coupled anodic processes. To precipitate metals by means of direct current in electrolysis cells which are undivided or are divided by separators, the pulsating cathode currents are generated by the anodes being divided into stationary strips past which the undivided cathode surface is guided. The current pulses formed on the cathode surface as a result can be varied in form and frequency by the arrangement of the anode strips and by current diaphragms. An apparatus with rotating cylinder cathodes and concentrically arranged anode pockets, the side walls of which function as current diaphragms and flow breakers, is preferred. Not only does the invention allow efficient recovery of metals, but also it allows coupling to various anode processes, e.g. for regeneration of peroxide sulfates and for breaking down inorganic or organic pollutants by oxidation.