Disclosed is a method of simultaneously processing fly ash and COPR, which can treat the fly ash and COPR harmlessly during the landfilling process through biochemical and engineering measures. The method includes: transferring the fly ash and COPR to the yard; laying an impervious layer inside the yard; laying a diversion material at a bottom of the yard; laying a mixture layer on the diversion material, where the mixture layer contains a biogas residue, a waste carbon source, ferrous sulfate, a nutritional additive, the waste incineration fly ash and COPR; placing an internal-electrolysis ceramsite layer on the mixture layer; injecting a carbon source solution from an upper portion of the yard and collecting a leachate to a collection device through the diversion material irregularly during the operation; and recirculating the leachate to a top of the yard for spray reinjection.

Asymmetric electrochemical cell apparatus, and methods of operating such apparatus to produce electrolyzed water.

The present invention relates to a process for purification of wastewater. In particular, the present invention pertains to an improved process for purification of wastewater by employing anolyte as an additive.

Disclosed is a method of simultaneously processing fly ash and COPR, which can treat the fly ash and COPR harmlessly during the landfilling process through biochemical and engineering measures. The method includes: transferring the fly ash and COPR to the yard; laying an impervious layer inside the yard; laying a diversion material at a bottom of the yard; laying a mixture layer on the diversion material, where the mixture layer contains a biogas residue, a waste carbon source, ferrous sulfate, a nutritional additive, the waste incineration fly ash and COPR; placing an internal-electrolysis ceramsite layer on the mixture layer; injecting a carbon source solution from an upper portion of the yard and collecting a leachate to a collection device through the diversion material irregularly during the operation; and recirculating the leachate to a top of the yard for spray reinjection.

A water treatment method includes a microbubble generating step (S101) of generating microbubbles in water to be treated containing at least calcium ions and producing water to be treated containing microbubbles, a water softening step (S102) of crystallizing calcium ions contained in the water to be treated containing the microbubbles as calcium carbonate and removing the calcium carbonate, and a reverse osmosis membrane treatment step (S103) of separating the water to be treated, from which the calcium carbonate has been removed, into reverse osmosis membrane treated water and reverse osmosis membrane concentrated water using a reverse osmosis membrane.

An ice maker capable of sterilizing bacteria contains: a body, a compressor, a condenser, a cooling fan, and a control box. The condenser is connected with a capillarity tube on which a filtration program is installed, and the capillarity tube is connected with an expansion valve which communicates with an evaporator, and an ice cavity that has a heater. A tilted channel is located below the ice cavity, and a storage tank is fixed on the tilted channel. The body includes an ice water tank and a water pump communicating with multiple spray nozzles. The ice water tank includes a control valve connected with an intake, an overflow outlet is defined on the ice water tank, and a generator for ozonated and hypochlorous acid water is mounted in the ice water tank. The ozonated and hypochlorous acid water generator includes a casing, two inflow holes, two outflow holes, multiple cathode plates, and multiple anode plates.

Disclosed is an electro-Fenton-like (EFL) platform wherein an electrochemically produced acidic environment supports heterogeneous Fenton-like reaction for high throughput water treatment. The platform enables treatment of contaminated water.

The invention concerns a subsea water processing system comprising an electrochemical unit that uses raw or treated seawater to generate high pH and low pH solutions that are used to clean at least one subsea process apparatus during a cleaning cycle by circulation through the at least one subsea process apparatus via acid or base flow lines connecting the electrochemical unit with the subsea process apparatus on-site.

Provided are hybrid electrochemical and membrane-based systems for removing silica from water stream to achieve ultra-pure water. The silica concentration of a feed water stream may dictate the most effective and economical variation of disclosed hybrid processes to use. For example, for a feed water stream having a silica concentration of 1-30 ppm, a hybrid system for treating the feed water includes an electrodialysis reversal unit, the electrodialysis reversal unit comprising an inlet stream and a product outlet stream; a reverse osmosis unit, the reverse osmosis unit comprising an inlet stream and a product outlet stream, wherein the inlet stream of the reverse osmosis unit comprises the product outlet stream of the electrodialysis reversal unit; and an electrodeionization unit, the electrodeionization unit comprising an inlet stream and a product outlet stream, wherein the inlet stream of the electrodeionization unit comprises the product outlet stream of the reverse osmosis unit.

A hydrogen gas dissolution apparatus 1 to comprises a hydrogen extracting pipe 8 for extracting hydrogen gas from a cathode chamber 40b, a water supply pipe 3 for supplying water for electrolysis, an opening pipe 81 for opening the cathode chamber 40b, a hydrogen gas dissolution module 6 connected to the hydrogen extracting pipe 8, a first open/close valve 91 installed on the above-said water supply pipe 3, a second open/close valve 93 provided on the opening pipe 81, and a control means 10 for controlling the electrolysis tank 7, the first open/close valve 91, and the second open/close valve 93. The control means 10 causes the water to flow for the first and second open/close valves 91 and then start the electrolysis after closing the first open/close valve 91 and the second open/close valve 93.