An example water purification system includes a forward osmosis module, a reverse osmosis module, a pump powered by an electric motor, and a pressure sensor. The forward osmosis module may receive a feed stream and a draw stream, and may produce an intermediate product stream. The intermediate product stream may be pressurized by a pump and provided to the reverse osmosis module. The reverse osmosis module may generate a product stream and return the draw stream to the forward osmosis module. The pressure sensor may monitor the pressure of the intermediate product stream, and the pressure may be used to determine the speed of the electric motor.

Disclosed in the present invention are a purification method and system of NMMO and a NMMO hydrate crystal obtained thereof. The purification method is suitable for purifying NMMO in a coagulating bath of a cellulose product, and by means of the method, almost all impurities including carbohydrate impurities can be removed from the NMMO solution of the coagulating bath of the cellulose product and a high-purity NMMO hydrate crystal is obtained. The purification method comprises the following steps: performing a cooling crystallization to the coagulating bath of the cellulose product between 20 C. and 78 C. to obtain NMMO hydrate crystals. According to the method for purifying and recovering NMMO in the coagulating bath of the cellulose product in the invention, ion-exchange resins are not needed, and acid and alkali are not needed for resin regeneration.

The invention concerns a process for producing gaseous dihydrogen and ammonium sulphate from an aqueous liquid effluent containing organic and inorganic materials or a mixture of aqueous liquid effluents,

said process comprising the following steps: nanofiltration of said aqueous liquid effluent or said mixture of aqueous liquid effluents so as to obtain a permeate; ammonia stripping of the permeate from said nanofiltration step in an ammonia stripping unit so as to obtain an ammonium sulphate; treatment by reverse osmosis of at least part of the permeate extracted from the ammonia stripping unit after said ammonia stripping step, so as to obtain an osmosed aqueous solution; electrolysis of at least part of said osmosis aqueous solution so as to decompose said part of said osmosis aqueous solution into at least gaseous dihydrogen.

The present invention discloses stable composite membranes comprising a porous support having one or more thin selective layers coated on a top surface thereof, whereas at least one of said thin selective layers comprises a crosslinked fluorinated silicone polymer, and further wherein the total thickness of said one or more thin selective layers ranges between 0.1 to 10 microns. The use of these membranes in the process of olive oil wastewater treatment and the valorization of polyphenol-rich by-products, are also disclosed.

A reverse osmosis unit for processing a feed solution is provided. The unit includes a pressure vessel includes an inlet end, an outlet end, and a vessel body extending between the inlet end and the outlet end. The reverse osmosis unit further includes a plurality of first membrane modules positioned within the pressure vessel. Each first membrane module of the plurality of first membrane modules has a first salt permeance value. At least one second membrane module is positioned within the pressure vessel and coupled in flow communication to the plurality of first membrane modules. The at least one second membrane module has a second salt permeance value that is different from the first salt permeance value.

A method of recovering a metal from a low-grade ore which is subjected to cyanide leaching to produce a PLS which contains a metal cyanide which is removed from the PLS by ultrafiltration and nano-filtration, and then acidified and sulphidised to produce a metal sulphide from which the metal is extracted, and hydrogen cyanide which is recycled to the cyanide leaching step.

Processing methods and systems are directed toward water filtration and/or purification techniques and/or energy recovery processes that may be used to generate usable water. Some embodiments can include at least one filtration and/or purification stage that processes water to a level of purity. Some embodiments can include recirculating water streams through a stage or another stage to achieve a desired level of purity. Some embodiments can include use of an energy recovery unit that may harvest energy from the water stream of the system and supply the harvested energy therefrom back into the system.

A fluid conditioning unit is provided that includes a housing, a cap, a cartridge device, and a filter cartridge. The cap is threadably secured to and unsecured from the housing by rotation about an axis of the housing. The cap forms a removable seal with the housing when secured thereto. The cartridge device is secured to the cap in a manner that restricts movement of the cartridge device with respect to the cap along the axis but allows rotation of the cartridge device with respect to the cap about the axis. The filter cartridge is removably secured to the cartridge device and is disposed in the housing along the axis.

A portable water conditioning system is provided that includes an incoming water inlet; a reverse osmosis stage in fluid communication with the incoming water inlet, the reverse osmosis stage having a permeate outlet and a concentrate outlet; a diversion device having a diversion valve, the diversion valve placing the concentrate outlet in fluid communication with a waste water outlet; a deionizing stage in fluid communication with a pure water outlet; a bypass valve configured to selectively place the permeate outlet in fluid communication with one or more of the waste water outlet, the deionizing stage, and the pure water outlet; and a controller configured to control the diversion device and the bypass valve to provide water at the pure water outlet of a desired condition.

A portable water conditioning system is provided that includes a water conditioner, a first sensor, a second sensor, and a controller. The water conditioner has a plurality of conditioning stages that condition water. The plurality of conditioning stages include, in a direction of flow of the water through the water conditioner, a reverse osmosis stage and a deionizing stage. The first sensor detects a first condition of the water before the reverse osmosis stage. The second sensor detects a second condition of the water after the reverse osmosis stage. The controller is in communication with the first and second sensors and determines a health status of the reverse osmosis stage based the first and second conditions. The first and second conditions each include a level of total dissolved solids of the water.