An inline buffer dilution system is provided that includes a first flow control valve fluidly connected to a supply of diluent liquid, second and third flow control valves fluidly connected to supplies of a first buffer and a second buffer, respectively, and a mixing pump fluidly connected to the first, second, and third flow control valves and configured to mix an amount of the diluent liquid, the first buffer, and the second buffer to produce a diluted buffer solution. The system further includes a backpressure control valve configured to generate a backpressure that promotes mixing within the mixing pump, and a controller configured to control the backpressure based on the amount of the diluent liquid, the first buffer, and the second buffer being mixed in the mixing pump, such that the mixing pump yields a minimum mixing threshold across a range of fluid flows.

An antimicrobial supply system employs a process water supply and incorporates a metallic ion supply connected to the process water supply to provide a high ion concentrate to an output. A dilution reservoir is connected to the metallic ion supply output and has an input from the process water supply. A pump is connected to an output of the reservoir. A manifold connected to the pump provides a dilute concentrate to at least one washing system and a recirculation loop to the dilution reservoir for enhanced mixing of the dilute concentrate. An electronics control module is connected to a first flow controller between the process water supply and the metallic ion supply and a second flow controller between the metallic ion supply and the reservoir for dilution control establishing a desired metallic ion concentration.

There is disclosed a capillary microfluidic circuit including a main channel communicating with a flow inducing element. The main channel has intermediary inlets. Reservoirs for containing one or more liquids prior to being drawn into the main channel. The reservoirs include a first reservoir and at least a second reservoir. Each of the reservoirs has an upstream end connectable to vents for filling the reservoirs with the one or more liquids and a downstream end. The downstream end of each of the reservoirs is connected to the intermediary inlets of the main channel A conduit is disposed between the first reservoir and the a least a second reservoir. The conduit links the downstream end of the first reservoir with the upstream end of the at least a second reservoir.

A gas solution manufacturing device 1 includes a gas supply line 2 configured to supply a gas as a raw material of a gas solution, a liquid supply line 3 configured to supply a liquid as a raw material of the gas solution, a gas solution production unit 4 configured to mix the gas and the liquid together to produce the gas solution, a gas-liquid separation unit 5 configured to perform gas-liquid separation of the produced gas solution into a supplied liquid to be supplied to a use point and a discharged gas to be discharged through an exhaust port, and a gas dissolving unit 6 provided in the liquid supply line 4 and configured to dissolve the discharged gas resulting from the gas-liquid separation in the liquid. The gas dissolving unit 6 is configured with a hollow fiber membrane configured with a gas permeable membrane.

A pressure washer includes a pump for pressurizing a primary fluid flow, the pump including a pump inlet for receiving fluid from a common fluid source and a pump outlet for supplying a pressurized primary fluid and a jet pump including a primary fluid inlet fluidly coupled to the pump outlet, a secondary fluid inlet configured to receive fluid from the common fluid source, and a fluid outlet. In a high pressure operating mode, all of the pressurized primary fluid flows through the jet pump and exits through the fluid outlet of the jet pump. In a high flow operating mode, all the pressurized primary fluid flows through the jet pump and entrains a secondary fluid supplied through the secondary fluid inlet from the common fluid source so that the secondary fluid also flows through the jet pump, resulting in a combined fluid flow of the primary fluid and the secondary fluid that exits through the fluid outlet of the jet pump.

A microfluidic system and method suitable for liquid mixing. The microfluidic system uses a pump (400) as the driving source, which draws at least two liquid samples that are to be mixed into the pump (400). Some air is drawn into the pump (400) as well. The system is also comprised of a mixing reservoir (203). The two liquids drawn into the pump (400) are pushed into the mixing reservoir (203). The air bubbles generated by the air have a stirring effect on the mixed liquid in the mixing reservoir (203). After the air bubbles burst, left at rest, and the air has risen to the top of the mixing reservoir (203), the mixed liquid is drawn back to the pump (400) and fed to the outlet (103) for subsequent detection steps. The addition of an antifoaming agent will prevent the accumulation of air bubbles during the mixing process. In the system, the valves (501, 502, 503, 504) and the sensors (601, 602, 603, 604) in the microfluidic channels (301, 302, 303, 304) will be used for the operation of the microfluidic system and for the precise control of the flow.

A distribution tube for a static mixer provides efficient mixing with improved performance over a wide range of flow rates. The distribution tube is positioned near an inlet side of the static mixer. An injected fluid is introduced into the static mixer via the distribution tube, which pre-mixes the injected fluid with a main fluid prior to further mixing by mixing elements of the static mixer.

A chemical injection unit consisting of one or more injection loops that uses a Venturi injector and motorized valve with a control system to isolate chemicals from water until operating conditions are suitable to carry the chemical and water mixture down the main flow pipe. The invention adjusts chemical injection rate to maintain desirable operational properties, including chemical injection rate, chemical concentration, or fluid viscosity. Accurate and real-time injection of chemicals is beneficial for safety as well as economics of the drilling operation in terms of reduced drilling time, efficient use of chemicals, and minimal variation in processing conditions.

A dilution apparatus (100) for diluting a fluidic sample in accordance with a specifiable dilution ratio, wherein the dilution apparatus (100) comprises a dilution fluid supply device (102) configured for supplying a dilution fluid at a first quantity per time, a transport fluid supply device (104) configured for supplying a transport fluid at a second quantity per time, a first fluid accommodation unit (106) configured for accommodating a first fluid volume, a second fluid accommodation unit (108) configured for accommodating a second fluid volume, and a control device (110, 112) configured for controlling the flow of the dilution fluid, the transport fluid and the fluidic sample so that in a first operation mode, the fluidic sample, being accommodated in the first fluid accommodation unit (106), is forced to flow to the second fluid accommodation unit (108) while being diluted by being mixed with dilution fluid, and in a second operation mode, the mixture of dilution fluid and fluidic sample, being accommodated in the second fluid accommodation unit (108), is forced to flow from the second fluid accommodation unit (108) to the first fluid accommodation unit (106) while being further diluted by being mixed with further dilution fluid.

An apparatus for processing a substrate includes a mixing nozzle having a mixing space that is shaped as an inverted cone, the mixing nozzle including a first inlet, a second inlet and an outlet installed at the mixing space; a first chemical supply unit connected to the first inlet; a second chemical supply unit connected to the second inlet; and a supply tank connected to the outlet, wherein the first chemical supply unit is configured to supply a first chemical solution to the mixing space through the first inlet, the second chemical supply unit is configured to supply a second chemical solution to the mixing space through the second inlet, and the supply tank is supplied with, through the outlet, a solution mixture that is formed of the first chemical solution and the second chemical solution after being mixed in the mixing space.