B01D2311/2684

Energy Efficient Reverse Osmosis Filtration
20250083107 · 2025-03-13 ·

The present disclosure provides a reverse osmosis filter elements for separating components of a fluid mixture. The filter elements comprise self-supporting membrane vanes comprising porous supporting strips and at least one reverse osmosis membrane layer laminated thereon. These filter elements have a permeate flow channel between the inner surface of the two porous supporting strips and an open feed water flow channel dispersed around the membrane vane. These filter elements can be used in new and existing filtration plants, such as desalination systems, and have a wide range of advantages over the spiral wound filter elements currently available.

SYSTEMS AND METHODS FOR WATER FILTRATION
20170028350 · 2017-02-02 · ·

A water filtration systems may comprise an under the sink RO water filtration system that is plumed into a building's water supply. For example; the water filtration systems may include an RO device at least partially installed underneath a sink, with the tap water connection plumbed directly to the sink cold water supply line, and a waste water drain line connected directly to the sink drain, such as the p-trap.

SYSTEMS AND METHODS FOR WATER FILTRATION
20170028351 · 2017-02-02 · ·

A water filtration systems may comprise an under the sink RO water filtration system that is plumed into a building's water supply. For example, the water filtration systems may include an RO device at least partially installed underneath a sink, with the tap water connection plumbed directly to the sink cold water supply line, and a waste water drain line connected directly to the sink drain, such as the p-trap.

SYSTEMS AND METHODS FOR WATER FILTRATION
20170029293 · 2017-02-02 · ·

A water filtration systems may comprise an under the sink RO water filtration system that is plumed into a building's water supply. For example, the water filtration systems may include an RO device at least partially installed underneath a sink, with the tap water connection plumbed directly to the sink cold water supply line, and a waste water drain line connected directly to the sink drain, such as the p-trap.

METAL COATED POLYMEMBRANE AND METHOD OF ELECTROFILTRATION AND ELECTROSORPTION USING A METAL COATED POLYMEMBRANE
20170007964 · 2017-01-12 ·

A metal coated polymer membrane, a method for the production thereof, an electrofiltration device or electrosorption device, and a method of electrofiltration and electrosorption using a metal coated polymer membrane. The polymer membrane is coated with metal using Atomic layer deposition (ALD).

Apparatus system and method to extract minerals and metals from water
12297136 · 2025-05-13 · ·

A new apparatus, system and method to purified produced water and removed valuable metals and minerals is described. The apparatus comprises a device for flowing produced water wellbore from a wellbore to the produced water purification apparatus; at least one device to remove heavy metals from the produced water; at least one brine removal device to remove brine from the produced water. The method comprises steps to use the apparatus and the system comprises a control panel that operates the at least one device for removing heavy metals and at least one sensor in a coordinated manner.

CHEMICAL FREE EXTRACTION OF LITHIUM FROM BRINE
20250230074 · 2025-07-17 · ·

The present invention relates to an integrated electrochemical lithium extraction process to directly produce lithium hydroxide from geothermal brine. The process integrates electrochemical silica removal, selective uptake and release of lithium using an intercalation material, and electro-driven generation of hydroxy (OH.sup.) ions.

Acidic treatment liquid processing apparatus, acidic treatment liquid processing method, surface treatment system, and surface treatment method

An acidic treatment liquid processing apparatus includes: a tank having an interior space; a diaphragm permeable to a metal cation and separating the interior space of the tank into a first chamber and a second chamber; a first electrode disposed in the first chamber; a second electrode disposed in the second chamber; a power supply configured to apply a voltage while using the first electrode as an anode and the second electrode as a cathode; a first liquid passing part configured to pass an acidic treatment liquid containing a dichromate ion and a metal cation into the first chamber; and a second liquid passing part configured to pass an acid aqueous solution into the second chamber.

Nitrogen-oxygen separation device
20250222397 · 2025-07-10 ·

A nitrogen-oxygen separation device includes a housing and a gas separation assembly. The housing comprises a front cover and a rear cover spaced apart to define a space. The gas separation assembly is disposed within the space and includes a front component positioned near the front cover, a rear component positioned near the rear cover, and an electrochemical assembly disposed between the front component and the rear component. The electrochemical assembly includes a cathode current collector, an anode current collector, and an electrolytic reaction membrane positioned between the cathode current collector and the anode current collector.

Method for recovering water and chemicals from plants for treating effluents from pulp and paper factories

Described herein is a process for upgrading effluent treatment plants for pulp and paper production processes, where salts are removed from the effluent for water reuse and chemical recovery. The process comprises a first dialysis system for salt removal, a second treatment system for recovery or re-concentration, and optionally a post-treatment of the re-concentrate preventing liquid discharges to the environment. In the first system, a reversible electrodialysis or reversible pulsed step is carried out, separating the salts from the effluent, which are sent to the second treatment system to concentrate the salts (re-concentrate) or transform them into useful chemicals for the same process (recovery). Chemical recovery is achieved by electrodialysis with bipolar membranes or metathesis, to reduce the re-concentrate stream, which cannot be reused in the same plant. Lastly, this stream may be treated by spray drying, crystallization or evaporation.