A system and related methods for monitoring and dosing peroxycarboxylic acids, particularly peracetic acid, in food processing applications based upon the desired concentration of the processing solution. The peroxycarboxylic acid concentration measured, and additional peroxycarboxylic acid added to the processing solution if the measured concentration is below a threshold level of the desired concentration, or additional water being added to the processing solution if the measured concentration is above a threshold level of the desired concentration. The system and related methods can be utilized with either live stream or static water sources to keep the concentration of peroxycarboxylic acid at or near desired concentration levels, which results in less concentration variation than experienced with conventional flow-based or hand-mixed systems.

A system for mixing and mixing processes and structures are disclosed. In addition a nozzle used for mixing is disclosed.

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.

Provided are: a method of producing heated ozone water, the method capable of producing heated ozone water having an extremely high ozone concentration by suppressing a reduction in the ozone concentration in high-concentration heated ozone water; heated ozone water; and a semiconductor wafer-cleaning liquid using the heated ozone water. A method of producing heated ozone water obtained by dissolving ozone in pure water, the method being characterized by including: adjusting a pH of the pure water to 3 or less by adding acid to the pure water; to obtain an acid water, dissolving an ozone gas in the acid water; and heating the pure water, the acid water or the ozone water, to 60 C. or more.

A system for growing algae includes a pivot arm pivotally coupled to a pivot connection positioned in a pond containing water and algae, and a mixing device coupled to the pivot arm and extending into the pond to mix the water and the algae as the pivot arm rotates.

A chemistry dispensing assembly for a laundry appliance includes a reservoir that dispenses a laundry chemistry to a treatment chamber. A mixing channel is positioned below the reservoir that receives the laundry chemistry dispensed from the reservoir. A fluid assembly delivers a fluid carrier through a flow path that includes the mixing channel. The mixing channel is defined between an underside of the reservoir and an upper surface of the mixing channel.

Methods and related apparatus for providing a chemical intervention processing solution for use within processing tanks. Processing tanks can include side streams or ancillary systems for generating the chemical intervention processing solution that can then be introduced into the processing tanks. The antimicrobial agents will be added and mixed in the side stream to form the chemical intervention processing solution. Additional actions can be conducted on the processing solution within the side stream including any and or all of heating, pumping, sampling, measuring, testing and pH adjustment of the processing solution. The chemical intervention processing solution can also be provided by a venturi injector that combines processing water and an antimicrobial agent and/or an alkaline agent outside of the processing tank. The processing solution can be used for various food processing applications.

An automated machine is provided for mixing and dispensing liquid detergents remotely controlled by a control software connected to a server which updates product databases, which is executed, together with other software for dispensing and delivering liquid content and surfactant detergent with anionic and cationic tensio-active chemical compounds as the basis of its selected formulation of Genapol, sodium phenyl sulfonate and the sodium lauryl sulfonate with preservatives such as formaldehyde and bactericides such as glutaraldehyde in a mixture of concentrated detergent with water in a proportion between 30% and 40%; where said machine is manipulated with a touch screen that drives two types of injectors that send product, to make the liquid mixture, to a static mixer or to a dynamic mixer and said machine conducts said mixed liquid to a tank of finished product to be dispensed by a filling spout placed on the front of a container-shaped casing.

The invention discloses a faucet capable of discharging ozone water, which includes a faucet body; an ozone generator; a water-gas mixer which includes a water inlet and a water outlet respectively located at two ends, wherein the water-gas mixer is arranged on a water outlet pipeline of the faucet body through the water inlet and the water outlet, an inner diameter reducing portion is formed in the water-gas mixer, a gas inlet is arranged at a position of a side wall of the water-gas mixer corresponding to the inner diameter reducing portion, and the gas inlet is communicated with the ozone generator; and a sensor arranged on the faucet body and used to receive an inductive signal to switch on or switch off the ozone generator.

A bubble generating device is disclosed which includes: a bubble generator including a tubular body, a liquid introduction port, a gas introduction port, and a discharge port; and a gas supply unit including a gas supply port, a pressurized gas being supplied to the bubble generator through the gas supply port, wherein the flow passage of the bubble generator extends substantially along a same axis, a plurality of reduced diameter portions each having an inner diameter reduced are provided along a direction along which the liquid flows, and gas-liquid mixing portions are provided downstream of the respective reduced diameter portions in a contiguous manner, each of the gas-liquid mixing portions having an inner diameter larger than a minimum inner diameter of each of the plurality of reduced diameter portions, and the gas introduction port of the bubble generator is formed of a plurality of through holes.