A skin cleaning device includes a body, the body is provided with a water storage tank, the water storage tank includes a clean water tank and a waste water tank, the body is provided with an electrolytic device, the water inlet of the electrolytic device is connected with the clean water tank, the water outlet of the electrolytic device is connected with a suction nozzle capable of contacting with the skin, the suction nozzle is also connected with a pump body, and the water outlet end of the pump body is connected with the waste water tank. The device can immediately generate hydrogen rich water with high efficiency and avoid wasting waiting time for electrolysis.

A water purification electrolytic generator apparatus provides clean drinking water to users. An electrolyte is added to water/other liquid exposed to the electrolytic generator apparatus in order to create an environment suitable for the apparatus to function . Residing in a housing of the apparatus is an enclosed first electrode (cathode) printed on a printed circuit board, a second electrode (anode), and a membrane separating the cathode and anode/printed circuit board. A control circuit including the printed circuit board electrically connects the anode and cathode to a power source, which is located external to the interior of the container. The incorporation of the printed circuit board reduces costs and improves portability so that the water purification system can provide drinkable water to users in different circumstances. A system including the apparatus may further include a container housing the electrolytic generator apparatus, a lid, and a stand. A filter is positioned in the container to filter water poured into the container.

A multifunctional membraneless boiled water electrolysis machine comprises a container (21) for containing raw water, and a water electrolysis apparatus. The water electrolysis apparatus is mounted outside the container (21) for containing raw water and comprises an electrolysis power supply (9), an electrolysis water tank (10) and an electrolysis electrode assembly (18) located in the electrolysis water tank. A water outlet at a bottom of the container for containing the raw water is connected with a water pump (24) through a pipeline. The water pump (24) is connected with a water inlet (15) of the electrolysis water tank (10) through the pipeline. The raw water in the container can flow into the electrolysis electrode assembly (18) from the water inlet (15) of the electrolysis water tank (10) after being heated or boiled by a heater (16). The water is electrolyzed through the gaps between the electrodes of different polarities in the electrolysis electrode assembly (18). The electrolyzed water flows from a water outlet (28) of the electrolysis water tank (10) to satisfy needs of people for the electrolyzed water of different water temperatures.

A microbial fuel cell system includes a supply-drain compartment having a supply port and a drain port of an electrolytic solution. The microbial fuel cell system further includes one or more power generation cassettes provided in the supply-drain compartment and each including a microbial fuel cell including: a positive electrode including a first water-repellent layer in contact with a gas phase and a gas diffusion layer attached to the first water-repellent layer; and a negative electrode holding anaerobic microorganisms. The microbial fuel cell system includes one or more purifying cassettes provided in the supply-drain compartment and each including a second water-repellent layer in contact with the gas phase. The power generation cassettes are arranged on the upstream side in a direction in which the electrolytic solution flows from the supply port toward the drain port, and the purifying cassettes are arranged on the downstream side of the power generation cassettes.

Methods of treating a fluid mixture include performing a first treatment on the mixture with electrochemically produced ions to separate an aqueous phase and a hydrophobic phase and performing a second electrochemical treatment on the separated aqueous phase to thereby remove aqueous contaminants from the aqueous phase wherein substantially laminar flow of fluid occurs between electrodes in the second electrochemical treatment.

A water treatment system includes a water inlet that intakes water to be treated, a high voltage (HV) electrode having a porous metal surface area in a range of between 0.1 cm.sup.2 and 5 cm.sup.2 in fluid communication with the water, such that the water flows through the porous metal surface area of the HV electrode, a ground electrode disposed across a gap from the HV electrode, in fluid communication with the water, a high voltage power supply electrically connected to the HV electrode for generating spark plasma or pulsed electric fields having a rise time equal to or less than 60 nanoseconds (ns) and an amplitude greater than or equal to 30 kV/cm across the gap, thereby producing treated water, and a water outlet that discharges the treated water.

A carbon fiber filter includes a center filter body and carbon fiber yarn wound around the center filter body. The center filter body is hollow and includes a water outlet. A surface of the center filter body is provided with at least one inverted triangular groove. A plurality of through holes are arranged in the groove. The through holes and the water outlet are in communication with a hollow inner cavity of the center filter body. The carbon fiber yarn is wound in the groove with a constant force to form a filter layer.

An apparatus for manufacturing hydrogen containing water is disclosed. An aspect of the present disclosure may provide an apparatus for manufacturing hydrogen containing water, comprising: housing having first receiving space formed therein; cylinder coupled to the housing to form second receiving space; connecting passage penetrating the housing to interconnect the first receiving space and the second receiving space; ion exchange membrane closing the connecting passage; electrolysis part comprising an anode and a cathode, the anode being disposed in the first receiving space and the cathode being disposed in the second receiving space; exhaust pipe penetrating the housing to interconnect the first receiving space and an external space; and first waterproof membrane closing the exhaust pipe and inhibiting water from being discharged while allowing gas to be discharged.

A water treatment apparatus includes: a plurality of plate-shaped ground electrodes; a high-voltage electrode unit having counter electrode portions opposing the ground electrodes, support portions supporting the counter electrode portions, and a voltage receiving portion for receiving a high voltage; a water supply unit for supplying to-be-treated water to between the ground electrodes from above, insulating members each having a lower end portion fixed to a support structure fixing lower end portions of the ground electrodes, and an upper end portion connected to the voltage receiving portion of the high-voltage electrode unit. The lower ends of the support portions of the high-voltage electrode unit are held in a space between the ground electrodes, and a portion where each insulating member and the high-voltage electrode unit are connected to each other is located above the water supply unit, so that electric leak due to the to-be-treated water is inhibited.

A system and associated method for producing an HOCl solution and an NaOH solution includes a generator operable for producing the HOCl and NaOH solutions utilizing electricity and a mixture of water and brine in an electrolysis cell. The generator includes a mechanical fixed flow restrictor (FFR) operable for controlling at least one of a pH of the HOCl solution and a free available chlorine (FAC) of the HOCl solution. The FFR includes an insert having a longitudinal fluid passageway. The length of the insert and the diameter of the fluid passageway are selected to control the pH of the HOCl solution and/or the FAC of the HOCl solution. The FFR is interchangeable so that the pH of the HOCl solution and/or the FAC of the HOCl solution can be precisely controlled.