659 results about "Electrocoagulation" patented technology

An electrocoagulation process for removing organic and metal contaminants from a pressurized waste fluid is disclosed in which a clarified waste fluid is produced when the pressure is released.

A method for the removal of contaminants from a contaminated water stream, by pretreating the contaminated water stream to yield a pretreated water stream, wherein pretreating comprises passing the contaminated water stream to at least one electrocoagulation cell wherein coagulation of contaminants is promoted, yielding an electrocoagulated stream; and separating coagulated contaminants from the electrocoagulated stream.

An electrocoagulation reactor comprising a plurality of electrodes positioned parallel to each other and provided with a means of energizing each electrode; a fluid inlet for an inlet stream comprising contaminated water; a fluid outlet for an outlet stream comprising electrocoagulated products; a flow distributor system; and a gas distribution system for injecting a gas into the electrocoagulation reactor. An electrocoagulation system for treating a contaminated water stream, the system comprising at least one electrocoagulation reactor.

A compact portable modular wastewater treatment system which integrates several processing technologies to provide a substantially purified water source. A wastewater stream is sent through an initial filtration step. The filtered wastewater is then subjected to electrocoagulation and then further filtered. The resulting stream containing substantially only organics is then treated in an advanced oxidation process which can include passing an electrical current through the water during the oxidation process. The partially treated water is then passed through ion-exchange columns to polish ammonium and other contaminants. The ion-exchange columns are cycled through regeneration cycles to provide continuous ion-exchange medium. The ammonium rich brine solution used in regeneration is subjected to an ammonium destruct process and then reused in regenerating ion-exchange columns. The water can then be sent through a final disinfection oxidation process to destroy or inactivate pathogens and/or remove any remaining colorants or odor to provide a water source suitable for almost any use.

A stream of process liquid is treated while flowing through in a horizontally elongated chamber having an open top. Longitudinally elongated electrode blades are aligned with the longitudinal dimension of the chamber. An overhead disbursement chamber supplies a sweeping air stream over the open top of the chamber for removing foam and gas reaction by-products. The electrode blades are separated and held at a desired spacing by small portable guides located below and above the blades.

A system and method for treating and removing hydrocarbon and other contaminants in bilge and ballast water, utilizing a multiple progressive process that chemically and electrically treats-and removes contaminants. Wastewater, received by a sump, is transmitted to a holding tank and treated, over a period of time while-influent wastewater continues off loading. The wastewater is pumped to an oil/water separator tank that decants free-floating oil from the wastewater to an oil retention tank. The wastewater then undergoes an electrocoagulation process where emulsions are broken and compounds that further aid treatment are created. The treated water flows to a retention/separation tank where contaminant particles coalesce and separate. Water is decanted and transferred to a clean water holding tank through an ozone injection system and an activated carbon filter. Treated water is recirculated until it exits the system meeting discharge limits for organics and metals allowing release into the environment.

The present invention provides an electrocoagulation device for drinking water and wastewater treatment by electro-coagulation and electro-catalytic precipitation principles. The invented device comprises a number of electrolysis cells formed by round-shaped electrode plates through which the raw water and waste water passes. A low DC voltage of 5 to 15 volts is applied to the cells. In addition, an electrode surface activator unit is provided to eliminate or minimize the passivation of the electrode plates. All types of impurities, including suspended solids, sub-micron particles, dissolved matters, dissolved minerals (including heavy metals and colloidal compounds), oil, grease, organic compounds and algae are converted to flocculants, water and carbon dioxide by the device. Micro-organisms and bacteria (pathogens) will be effectively killed at up to 99.99%. The invented device is capable of continuous operation.

A waste water treatment system and process for treating waste water received in a batch tank. The waste water is discharged in a headwork screen for removing large solids in the water. The solids are into a sludge drying bin. The screened water is transferred into a top of an influent surge tank with an oil/water separator. The oil/water separator includes a plurality of coalescing plates for separating free oil from the waste water. Heavy solids in the surge tank are drained into the sludge drying bin. The waste water is now dropped into a containment pan. From the containment pan, the waste water is pumped into a water treatment tank. The water treatment tank includes two or more electrodes mounted in the top thereof. The electrodes are separated using insulating support spacers for providing proper electrode spacing and insulation between the electrodes. The electrodes are used for providing current to the waste water and separating the contaminates in the water by electrocoagulation. The treated water in the water treatment tank is discharged after a completion of a period of settling or dwell time into a clean water tank.

An electrocoagulation system for removing contaminants from waste effluents comprising an electrocoagulation reactor having charged and uncharged plates and allowing serial flow of water therethrough. The reactor is connected to a voltage source to charge some of the plates positive and some negative, with uncharged plates between the positive and negative plates. The system allows waste water to enter the reactor for coagulation therein, the waste water leaving the reactor to enter a defoam tank for agitation which allows trapped bubbles to rise to the surface of the tank as foam. From the defoam tank, waste water goes through a sludge thickener, to allow sludge to settle at the bottom thereof and waste water is drawn off from the sludge thickener to flow to a clarifier. The pump removes sludge forming at the bottom of clarifier to take it back to the sludge thickener. The sludge is drawn out the bottom of the sludge thickener for transport to a press where most of the water is removed therefrom. Water is drawn off the top of the clarifier for transport to a conventional sewer system, or for reuse.

Incision and closure surgical device designed to assist in operative surgery as a means of effecting and repairing skin wounds. A slide fastener is fitted to a self-adhesive sheet that is attached to the skin surface. The slider of the slide fastener contains a contact electrode for electrocoagulation fitted with a cutting edge. As the slide fastener is opened, the slider simultaneously effects the incision by means of the cutting edge of the electrode, severing both the flexible sheet and the skin beneath. For closing the incision, the stringer tapes of the slide fastener interlock by the action of the slider, thereby bringing both the edges of the flexible sheet and the wound beneath into apposition. As the slider is drawn forwards closing the stringer tapes, electrical energy is applied by the electrode at the union site of the wound edges, which have previously been brought into apposition by the mechanical action of the slide fastener, thus ensuring that the edges become adhered in full depth as a result of electrical coagulation.

The current invention provides a novel process for the treatment and reclamation of drilling frac flowback and produced wastewater from the drilling industry. The wastewater is delivered to the EMC/F System from a frac tank or other reservoir. The wastewater is pumped into the system and is treated sequentially by passing through a mechanical hydrocavitation unit, an electromagnetic unit, an electrocoagulation unit and/or a hydrocyclone and a flocculation-sedimentation tank. Polishing of the final effluent is accomplished by passing the water through a mixed media tank.

An in situ system used for treating an oil and gas well drilling fluid and treating water after a well is completed. The system includes a fluid treatment unit used in a reserve pit and a water treatment unit disposed next to the pit. The fluid treatment unit includes a floating electrocoagulation unit in the reserve pit for destabilizing contaminates in the fluid and dropping out stable precipitates. The clear treated fluid is then pumped, using a submersible pump, to the water treatment unit. The water treatment includes a number of components including a pre-filter, an activated carbon filter and a heat exchanger for first treating the fluid. The filtered and heated fluid is then piped into a reverse osmosis unit for removing salt and any remaining minerals found therein. From the reverse osmosis unit, approximately 70 to 80% of the filtered water is cleaned and piped to a clean water storage tank for reuse. Reject water from the reverse osmosis unit is transferred to a water pre-heater and a primary and secondary distillation unit for converting the heated water to steam. The steam is now piped to a condenser where the steam is cooled to distilled, clean water. The remaining clean water from the condenser is now transferred to the clean water storage tank.

A water treatment reactor adapted to simultaneously carry out electrocoagulation and advanced oxidation processes is disclosed, which includes an upright sealed tank having a metal body, or a metal mounted on an inner wall thereof, used as a cathode; a sacrificial electrode used as an anode, which is disposed in the tank and non-electrically connected to the cathode; a mixing device disposed in the bottom of the tank for enabling mixing of influent water and an air or oxygen-containing gas introduced into the tank; a gas-liquid separator which is in fluid communication with the tank at the top for expelling a gas from the tank without expelling water; and a direct current supply having a positive electrode electrically connected to the anode and a negative electrode electrically connected to the cathode.

A process for enhanced removal of impurities from water by an enhanced multi-step electrocoagulation process including electrocoagulation, solids separation, hardness removal, crystallization, and, optionally, reverse osmosis and evaporative purification. Embodiments of the invention may remove multiple impurities at substantial savings in time, energy, and chemical use. Zero liquid discharge options are also reported.

The invention relates to a method and a device for processing pharmaceutical wastewater by pulse electrocoagulation-MBR. The main process of the method is a pulse electrocoagulation-chemical oxidation-MBR process. The device sequentially comprises a regulating reservoir, an electrocoagulation reactor, a chemical oxidation pond, an anoxic pond and a membrane bioreactor, wherein the electrocoagulation reactor adopts a pulse power supply for power supply, overcomes the problem that a polar plate is susceptible to passivation, has the characteristics of low energy consumption and high process efficiency, and can remove a major part of pollutants in the wastewater; the chemical oxidation pond plays a role in strong oxidative decomposition and converts difficult-to-degrade substances into biodegradable minor molecule substances; and the anoxic pond and the membrane bioreactor form an A/O process, the membrane bioreactor can effectively degrade organic substances, ammonia nitrogen and other pollutants in the wastewater, the processed waster water is filtered by a membrane and the effluent can reach an industrial grade A level. The process has the advantages of impact load resistance, stable effluent quality and low investment cost.

Methods and systems are disclosed which provide for the purification of effluent from a septic system or natural water from rainwater or stormwater collection devices for the storage and reuse of water. The purified water may be supplied to water applications, such as a return conduit to a home for potable or graywater usage. The distillation unit may be powered by a local power independent of a municipal power grid and which may employ sustainable energy mechanisms. The distiller residue may undergo a volume reduction process, such as evaporation, coagulation, electrocoagulation or microfiltration. The purified water may be stored in a holding tank with sensors to monitor the water quality and water level within the tank. Alarms, release valves or relief valves may be activated in response to such monitoring.

A control assembly for an electrocoagulation cell (1) comprising a plurality of electrodes, a releasable connection means (6) between at least a selection of the electrodes and electrical connection means (9, 10, 9A, 10A) attached to the releasable connection means (6) which in use is connectable to a power supply (12). An electrocoagulation system comprising a plurality of electrodes (2), an electrolytic cell (1) having an internal chamber which contains the plurality of electrodes (2), and a power supply (12) connectable to a power source and also connectable to the electrodes said power supply having control means (14, 24) for providing a selected constant output current or selected constant output voltage whereby the electrolytic cell may process samples of varying characteristics.

A water treatment system using electrocoagulation is provided. One of the stages of the water treatment is subjecting the water to electrocoagulation so that colloidal solids can be reduced, emulsions broken, and hydrocarbons and complex organics removed, without the application of substantial chemical substances to the contaminated water or even the use of any chemical substances. An electrocoaguloaty apparatus can comprise: a tank having a first end and a second end; a plurality of electrolytic cells provided in the tank, each electrolytic cell having at least one anode electrode and at least one cathode electrode defining an anode/cathode electrode pair; and a voltage supply connected to each electrolytic cell to supply a voltage across each anode/cathode pair.

Subject matter of the invention is the procedure and plant for industrial wastewater and/or drinking water treatment by means of electrochemical methods and advanced oxidation processes. The preparatory phase of gravitational sedimentation is followed by main treatment consisting of electrocoagulation, electrooxidation and electroflotation through action of metal electrode sets made of inox, steel and aluminium respectively, with parallel disinfection/oxidation with ozone, UV irradiation and ultrasonic treatment, as well as recirculation in the electromagnetic field. At the end of the main treatment, the mixture of floccule and water is subject to coagulation/flocculation by electrochemically generated steel and aluminium floccule with slow infusion of ozone. The next phase is separation of sediment from clean water which is discharged through sand and activated charcoal filters for the purpose of removal of light floating floccule in the collection tank. If required, the water is subject to oxidation with simultaneous action of UV irradiation and ozone for the purpose of final destruction of organic matter and ammonia, and potential residues of microbiological contamination.

The invention discloses a treatment method of chemical nickel-plating wastewater. The method comprises the following steps: (1) treating nickel-plating wastewater with strongly basic anion-exchange resin so as to destabilize nickel complex; (2) adsorbing nickel ions contained in the nickel-plating wastewater with strongly acidic cation-exchange resin; (3) adding a strong oxidant in the nickel-plating wastewater so that hypophosphite, phosphite and macromolecular organic acid complexing agent which are contained in the wastewater are oxidized so as to form phosphate and organic micromolecules;(4) carrying out pulse electrocoagulation on the nickel-plating wastewater so that the phosphate forms iron phosphate to be precipitated and residual nickel ions are oxidized to form oxidized scale precipitate at the same time; and (5) regulating the wastewater to alkalinity so that iron ions in the wastewater are precipitated, successively adding a deironing agent and a flocculant to remove ferrous ions and suspended matters in the wastewater, and directly discharging supernate. According to the invention, the content of the nickel ions in the wastewater treated by the process is far less than 0.1ppm and meets a national primary standard, the recycle of nickel resources can be realized, and the economic benefits of wastewater treatment are improved.

A process to purify wastewater that comprises the steps of passing the wastewater through an electrocoagulation cell which comprises a plurality of reaction plates or electrodes (6) disposed within said cell and spaced apart from each other, whereby said wastewater is treated by passing an electric current through the wastewater to thereby produce purified water (8); re-using said purified water for cleaning or other purposes to produce wastewater; and recycling (3) the wastewater back to the electrocoagulation cell. The wastewater may be obtained public or household showers, sinks, basins, baths, washing machines, dishwashers, kitchens or car washes.

A method and apparatus for the high-pressure electrocoagulative treatment of aqueous and viscous fluids and sludge is provided. The apparatus includes a plate and frame design utilizing mechanical closure on a plurality of recessed, gasketed, non-electrically conductive electrocoagulation spacer plates that completely enclose and isolate all fluids, electrical contacts, and electrodes within the confines of the apparatus. The spacer plates include intergral supports that position and support said plates with enclosed electrodes on top of the side rails of the supporting frame of the apparatus allowing said plates to be separated for electrode replacement and maintenance and conversly closed, pressured and put into service. The apparatus includes a baffled influent and effluent chamber at both ends for the addition and flash mixing of chemical reagents and/or flocculants and to provide a means of fluid communication between fluid conduits and chambers formed within the apparatus.

A system for servicing a wellbore, comprising a water source, a first water stream from the water source comprising undissolved solids, dissolved organics and undissolved organics, the first water stream being introduced into a mobile electrocoagulation unit, a second water stream comprising coalesced undissolved solids, coalesced undissolved organics and dissolved organics, the second water stream being emitted from the electrocoagulation unit and introduced into a mobile separation unit, a third water stream comprising dissolved organics, the third water stream being emitted from the separation unit, an ozone stream emitted from a mobile ozone generator and added to the third water stream comprising dissolved organics to form an ozonated water stream comprising dissolved organics, the ozonated water stream comprising dissolved organics being introduced into a mobile ultraviolet irradiation unit, a fourth water stream substantially free of undissolved solids, facilely-oxidizable organics and active microorganisms, the fourth water stream being emitted from the ultraviolet irradiation unit, and a wellbore servicing fluid, wherein the wellbore servicing fluid is formed using the fourth water stream, the wellbore servicing fluid being placed in the wellbore.

This invention relates to a method of installation of an electrocoagulation (EC) system to remove contaminants from wastewater which includes the steps of: (i) measuring conductivity of the wastewater; (ii) from the result obtained in step (i) determining the number of electrically connected electrodes or unipolar electrodes required in the EC system for efficient removal of the contaminants, and (iii) from step (ii) assessing a range of current and/or voltage to be applied to an EC cell included in the EC system.