A water savings system and method for reducing the amount of water needed for adiabatic cooling including the use of a softener and a reverse osmosis device, in which tap water, softened if necessary, is delivered to a reverse osmosis device and softened water alone, reverse osmosis reject water, or softened water combined with reverse osmosis reject water is delivered to spray nozzles for cooling, and reverse osmosis pure water is stored and used periodically to flush the coils to inhibit and/or prevent corrosion from dissolved salts and other solids in the spray water.

Formation of CaSO.sub.4 and Fe.sub.2O.sub.3 containing deposits is reduced in a pressure oxidation autoclave and/or adjacent circuits during pressure oxidation of gold-containing ore. The gold-containing ore is combined with water to create an aqueous slurry that is heated and introduced into the autoclave. The method includes providing a scale inhibitor that is free of an organic polymer and includes an inorganic phosphate according to formula (I), (XPO.sub.3).sub.m, wherein X is Na, K, H, or combinations thereof, and m is at least about 6, an inorganic phosphate according to formula (II), Y.sub.n+2P.sub.nO.sub.3n+1, wherein Y is Na, K, H, an organic phosphonate; or combinations thereof, and n is at least about 6. The method includes the step of combining the scale inhibitor and at least one of the gold-containing ore, the water, and the aqueous slurry to reduce scale.

The invention provides a device with a steam function, wherein the device includes a water supply opening, a scale inhibitor dosing element, a flow control device, a heating unit, a scale collector element, and a water processing unit. Further, the flow control device provides a fluid including water to flow from the water supply opening via the heating unit to the water processing unit; the scale inhibitor dosing element provides a scale inhibitor to the water at a location in the heating unit and/or upstream of the heating unit; the heating unit includes heating the water in a heating mode and for converting the water into steam in a steam formation mode; and the scale collector element is arranged downstream of the heating unit and upstream of a flow restriction, wherein the scale collector element includes collecting scale particles from the fluid flowing through the scale collector element.

A method for electrolysis-ozone-corrosion inhibitor/electrolysis-ozone-hydrogen peroxide-corrosion inhibitor coupling treatment on toxic and refractory wastewater includes the following steps: adding toxic and refractory wastewater to be treated into a wastewater treatment reaction tank equipped with a plate anode and a plate cathode, and starting a direct current (DC) power supply connected to the plate anode and the plate cathode to treat the toxic and refractory wastewater at an appropriate current density under stirring, during which a corrosion inhibitor and hydrogen peroxide are added to the toxic and refractory wastewater to be treated and ozone is introduced into the toxic and refractory wastewater to be treated through an aeration device. The method can increase the production rate and production quantity of free radicals in a reaction system, effectively improve the treatment efficiency for toxic and refractory wastewater, and reduce the treatment cost.

Systems and methods for treatment of hard water are disclosed that relate to combining a scale reduction device with a water softener device. In an aspect, the water softener device is an ion exchange water softener device. The systems and methods can be used to provide treated water having the same or similar performance quality compared to water produced by ion exchange water softener devices alone, while using significantly less chemical regenerant.

This invention effectively suppresses the corrosion fatigue of a boiler evaporation tube that is associated with repeated stress attributed to the presence of a corrosive environment and scales. This method for suppressing corrosion fatigue of a boiler evaporation tube includes maintaining the dissolved oxygen concentration of the boiler water at 1.0 mg/L or less. Preferably deionized water is used for the boiler water and a scale dispersant is present in the boiler water.

A feeding head assembly and a chemical release system for eliminating scale conditions and maintaining a neutral pH in potable water is disclosed. The feeding head assembly may include a composite membrane system comprising at least one semi-permeable layer and at least one filter layer. A chemical release system may include a cartridge or vessel. The cartridge may include a hollow body with two opposing open ends. A time-release pouch may be located within the hollow body and holds a composition that mixes with potable water to eliminate scale conditions and maintain a neutral pH in the potable water. A feeding head assembly may be coupled within the hollow body between the time-release pouch and one open end of the hollow body.

A water savings system and method for reducing the amount of water needed for adiabatic cooling including the use of a softener and a reverse osmosis device, in which tap water, softened if necessary, is delivered to a reverse osmosis device and softened water alone, reverse osmosis reject water, or softened water combined with reverse osmosis reject water is delivered to spray nozzles for cooling, and reverse osmosis pure water is stored and used periodically to flush the coils to inhibit and/or prevent corrosion from dissolved salts and other solids in the spray water.

An anti-scale electrochemical apparatus comprises at least one ion exchange cell, each cell comprising a housing having a plurality of openings to receive and release a water stream, inner and outer electrodes in the housing, and a water-splitting membrane between the inner and outer electrodes to treat an influent water stream to form an effluent water stream. A controlled-release scale-inhibitor composite comprising a scale-inhibitor agent and a polymer, is provided in the housing or in the water flow pathway of the electrochemical apparatus. An anti-scale, water splitting ion exchange membrane was also fabricated.

A phosphorus-based calcification inhibitor (“inhibitor”) configured to prevent calcification of anaerobic granular sludge.