A method for controlling treatment of an industrial water system is disclosed. The method comprises the steps of providing an apparatus for controlling delivery of at least one treatment chemical, the apparatus comprising at least one sensor and an electronic input/output device carrying out a protocol; measuring a parameter of the industrial water system using the at least one sensor; relaying the measured parameter to the electronic device; adjusting the protocol based on the measured parameter; delivering a concentrated treatment chemical into a stream of the industrial water system according to the adjusted protocol, the concentrated treatment chemical comprising an active ingredient, the active ingredient traced as necessary, the active ingredient having a concentration; repeating the measuring, the adjusting, and the delivering; and optionally repeating the steps for n-number of parameters, n-number of active ingredients, and/or n-number of concentrated treatment chemicals.

A water softener system includes a brine tank, an ion-exchange resin and a softener control valve fluidly coupling the brine tank and the ion-exchange resin. The softener control valve has an inlet configured to receive a flow of feed-water and an outlet configured to deliver a flow of product water. A flow meter is configured to monitor a flow rate of water to or from the control valve, and a sensor is arranged upstream of the inlet of the softener control valve to measure a fluid property of the flow of feed-water. A controller is configured to calculate an available exchange capacity of the ion-exchange resin using flow rate data from the flow meter and a hardness value of the feed-water, which the controller calculates using a fluid property value from the sensor and a predetermined coefficient. The controller is also configured to initiate a regeneration of the ion-exchange resin using the brine tank and the softener control valve, and to update the predetermined coefficient based at least partially on the calculated available exchange capacity upon initiating the regeneration.

The disclosure relates to systems, devices, and methods for flow control in a reverse osmosis filtration system, such as within a medical device. The systems, devices, and methods can respond to changes in permeate flow rate and solute concentration by adjusting feed water and concentrate water rates. Multiple feedback loops adjust parameters to meet water flow rate and purity requirements.

The disclosure relates to systems, devices, and methods for flow control in a reverse osmosis filtration system, such as within a medical device. The systems, devices, and methods can respond to changes in permeate flow rate and solute concentration by adjusting feed water and concentrate water rates. Multiple feedback loops adjust parameters to meet water flow rate and purity requirements.

A water conditioning system of an electrodialysis reversal (EDR) water purifier includes a first source water inlet, a second source water inlet, an EDR film stack, a first conductive probe, a second conductive probe, a third conductive probe, a fourth conductive probe, a variable speed pump, a one-way valve, a clean water outlet, a waste water outlet, an electrode A, an electrode B, and a control system module. With the four conductive probes detecting conductivity of water flowing through four ports on two sides of the EDR film stack and by sending detected data to the control system module, the control system module adjusts voltages of the electrode A and electrode B accordingly to instantly increase or decrease removal efficiency of the EDR film stack. Thus, the conductivity of the discharged clean water and the quality of the clean water can be stabilized.

A water conditioning system of an electrodialysis reversal (EDR) water purifier includes a first source water inlet, a second source water inlet, an EDR film stack, a first conductive probe, a second conductive probe, a third conductive probe, a fourth conductive probe, a variable speed pump, a one-way valve, a clean water outlet, a waste water outlet, an electrode A, an electrode B, and a control system module. With the four conductive probes detecting conductivity of water flowing through four ports on two sides of the EDR film stack and by sending detected data to the control system module, the control system module adjusts voltages of the electrode A and electrode B accordingly to instantly increase or decrease removal efficiency of the EDR film stack. Thus, the conductivity of the discharged clean water and the quality of the clean water can be stabilized.

This invention uses multiple pairs of electrodes acting as electrical conductivity sensors that are secured at specific locations within spiral wound membrane elements and their interconnecting components of a reverse osmosis or nanofiltration pressure vessel. Each electrode pair might be attached to a wire cord to be inserted through and sealed against a vessel end cap into the permeate carrier tubes and interconnecting components of the membrane elements, or each electrode pair might be attached to a battery and a wireless transmitting device. Conductivity measurements from the sensors would be communicated to a microprocessor, which would evaluate each permeate conductivity measurement relative to other permeate conductivity measurements, as well as relative to derived or measured conductivities in the saline water in calculating a percent salt passage value specific to the location of each permeate sensor.

This invention uses multiple pairs of electrodes acting as electrical conductivity sensors that are secured at specific locations within spiral wound membrane elements and their interconnecting components of a reverse osmosis or nanofiltration pressure vessel. Each electrode pair might be attached to a wire cord to be inserted through and sealed against a vessel end cap into the permeate carrier tubes and interconnecting components of the membrane elements, or each electrode pair might be attached to a battery and a wireless transmitting device. Conductivity measurements from the sensors would be communicated to a microprocessor, which would evaluate each permeate conductivity measurement relative to other permeate conductivity measurements, as well as relative to derived or measured conductivities in the saline water in calculating a percent salt passage value specific to the location of each permeate sensor.

The present invention relates to a system and process for treating a feedwater wherein the system includes at least one RO or nanofiltration unit that receives a feed under high pressure and produces a concentrate that is directed to and held at low pressure in a concentrate accumulator. Generally the permeate or the inlet feedwater is maintained at a constant flow rate. Periodically the system is switched from a mode 1 or normal operating process to a mode 2 where the concentrate is drained from the concentrate accumulator. However, in mode 2, the feedwater is still directed into the system and through the RO or nanofiltration unit which produces the permeate and the concentrate.

A system and a method for reusing waste water from a Reverse Osmosis (RO) filtering process are described, said system including: a Reverse Osmosis (RO) filtration system, from which a flow of highly alkaline waste water results; two tanks intended to receive waste water and able to alternately determine the physical and chemical properties of waste water through sensors or, and perform homogenization, chlorination and chemical treatments of said waste water; an output line which comprises a pump and connects the tanks to a reservoir; and said reservoir being able to blend the water treated by the tanks with treated chlorinated drinking water, depending on the physical and chemical properties of these volumes of water; the chlorination and chemical treatment includes addition of a hypochlorite compound, which reaction releases chlorine in the waste water and causes evaporation of at least O.sub.2 and H.sub.2 gases, reducing the alkaline pH of said waste water.