The embodiments disclose a method including processing and treating at least one water source supply for mixing with humic acid and fulvic acid, chopping and pulverizing at least one humate source, mixing the chopped and pulverized at least one humate source with the processed and treated at least one water source supply, processing the chopped and pulverized at least one humate source and the processed and treated at least one water source supply for separating, segregating, and suspending fulvic acid and humic acid molecules from the at least one humate source, storing the fulvic acid and humic acid molecules in a fresh quantity of the treated water source supply, adjusting the pH level of the stored fulvic acid and humic acid, and creating at least one or more beverage product for human consumption using the fulvic acid and humic acid molecule ingredients and other ingredients including vitamins, flavorings and additives.

Illustrative configurations of a pet hydration system and methods are disclosed. The pet hydration system includes a bowl section configured to temporarily store water therein. In one configuration, a hydrogen-generation assembly is positioned in the bowl section. The hydrogen-generation assembly generates and introduces hydrogen into the water temporarily stored in the bowl section. In other configurations, methods related to pet hydration are also disclosed.

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.

The present invention provides a multi-stage filter system suitable for the production of drinking water from a wide variety of contaminated water sources. The modular nature of the multi-stage filter system allows for the customization of filter combinations according to the remediation requirements. The multi-stage filter system comprises a coarse filter (S1); an ultrafiltration filter (S2); a graphene-based filter (S3); and a residual nanoparticle filter (S4). The graphene-based filter cartridge comprises few-layer graphene powder; a combination of few-layer graphene powder and pellets comprising a mixture of polyethersulfone, graphene oxide (GO), and dimethylformamide; a composite comprising chitosan, GO, sodium sulfate and ferric chloride; or a combination of few-layer graphene powder, granular activated carbon and a composite comprising chitosan, GO, sodium sulfate and ferric chloride.

Embodiments of the present disclosure relate generally to a method, apparatus and system for the evaporation of produced water and dirty water from oil and gas production and other dirty water sources. The evaporation system may consist of a portable pond embodied in an Above Ground Storage Tank (AST) system and a fluid projection system which maybe controlled and employ optimized operating conditions to maximize the evaporation of produced water under varying meteorological and chemical condition.

It is an object of the present invention to provide a solid drug that is very convenient to transport and store. In order to achieve the object, a drug according to the present invention is a solid drug that includes a radical generating catalyst and a radical generation source.

A facility-based domestic wastewater treatment system equipped with modified toilets and a hypochlorous acid machine, neutralizing coliform bacteria from bodily excretions at the source. The treated batch content in the toilet is flushed to a secondary process tank equipped with a grinding pump, hypochlorous acid dispensing nozzles and solenoid valves. Toilet and other facility utilities wastewater are treated and discharged to a filtration system to be separated. The filtration system is capable of separating bacteria and other particulates up to or equal to a fineness of 0.01 microns. Separate storage tanks are used to store recovered and reclaimed water in conjunction with a slurry waste collection tank for solid waste disposal. A facility-based wastewater reclamation system utilizing Reverse Osmosis process to remove unwanted contaminants and dissolved solids producing potable water, some of which is further processed with UV, and Ozone treatment to be used as drinking and cooking water.

A system and method for controlling the accelerated remediation of the water of an aquatic facility using at least one sanitizer sensor, a pH sensor, a temperature sensor and a chlorine dioxide sensor all interfaced with a programmable controller that is programmed to implement a remediation cycle and configured to calculate a Ct value of the water chemical feed system. The programmable controller activates a chemical feed system to supply an acid, an oxidizer and a chlorite ion donor to a conduit to form chlorine dioxide that is supplied to the water until a desire Ct value is reached.

A sequential batch reactor wastewater treatment system and method, a material combination for practicing the method, and a fertilizer co-product deriving therefrom. A pH lowering agent comprising an acid lowers the pH of wastewater. A first compound including chitin or chitosan comprises a filtering medium, a coagulant, and a flocculant, and a second compound comprises an adsorbent and a pH raising agent. Wastewater is mixed and aerated subsequent to introduction of each of the first and second compounds, and flocculation yields treated water and a sludge byproduct that may be dewatered and further processed to yield a useful fertilizer co-product. Within the first compound, diatomaceous earth operates as a filtering medium and bentonite clay acts as a coagulant and filtering medium. Within the second compound, activated carbon, calcium oxide (CaO), and caustic soda (NaOH) are operative to adsorb, disinfect, and raise the pH of the wastewater.

An automated produced water treatment system that injects ozone or an ozone-oxygen mixture upstream of produced water separators, with the dose rate changing dynamically as the produced water quality changes, as determined by continuous monitoring of the produced water quality by a plurality of sensors that detect water quality parameters in real time. The system may operate as a “slipstream” injection system, that draws a portion of produced water from the produced water pipeline and injects ozone or an ozone-oxygen mixture back into the pipeline with disrupting or slowing normal operations. Disinfectants or other additives may also be injected. The treatment system may be wholly or partially contained in mobile containers or trailers, for on-the-fly use in existing produced water treatment facilities.