The present invention discloses an SWRO and MCDI coupled seawater desalination device system with energy recovery, including a pre-filtering unit, an SWRO treatment unit, an MCDI treatment unit, and a post-filtering unit. The SWRO treatment unit is coupled with the MCDI treatment unit. Seawater desalination is performed through a coupling complementary water passage and circuit design, while water quality is improved, and the continuity of water output from a water passage of the device is kept. By recovering the pressure potential energy of high-pressure brine in the SWRO treatment unit and electric energy released by desorption in the MCDI treatment unit, energy consumption is reduced.

A method for selectively removing micro-contaminants from sludge, the method includes a) providing sludge contaminated with micro-contaminants, and b) subjecting the sludge to a primary treatment step, thereby producing a first stream of primary sludge comprising a first part of micro-contaminants and a second stream of remaining sludge comprising a second part of micro-contaminants, c) subjecting the second stream of remaining sludge to a secondary treatment step, thereby producing biological sludge, wherein the first stream of primary sludge and the biological sludge are further subjected to separate treatment steps whose effects are coupled, so as to divert, capture and destroy the first part of micro-contaminants in the primary treatment step.

A method for decomposing and removing a pollutant includes: confining, in a small sealable container, a waste containing the pollutant to be processed and liquid for dilution together with gas containing oxygen or air; disposing the small sealable container in a processing chamber of a high-temperature and high-pressure processing device and keeping the small sealable container at an elevated temperature after the confining; and lowering a temperature in the processing chamber after the disposing. The disposing and the lowering are performed under a state where the small sealable container is pressurized from outside by increasing a pressure in the processing chamber.

Disclosed herein are apparatuses and methods for semi-permeable membrane cleaning. In particular, a pressure retarded osmosis (PRO) process redirects raw solution and fluid streams in such a way as to cause periodic changes of the process from PRO to reverse osmosis (RO) for lifting and detaching fouling. Further disclosed is applying, at least periodically, a pulsed-flow regime in the fluid stream, thereby causing increased shearing force for enhanced evacuation of the foulant. Additionally, a backward wash may be provided by injection, for a predetermined injection time, of additional solution selected in such way that net driving pressure becomes RO opposite to normal PRO operation, thereby providing a backward flow from a first side of the membrane to a second side of the membrane, so as to lift and evacuate foulant.

A method of a filtration uses a hollow fiber membrane module comprising a module case; and a hollow fiber membrane bundle comprising a plurality of hollow fiber membranes bundled together and being accommodated in the module case, respective ends of the hollow fiber membranes being bonded together by a potting material. The filtration is carried out in the hollow fiber membrane module under a pressure of 0.3 to 1.2 MPa. The hollow fiber membrane module satisfies a relationship: 0.5<R/L<5 when the pressure inside the hollow fiber membrane module is 1.0 MPa without the hollow fiber membrane module being restrained, and satisfies relationships: 0<R<0.25 and 0<L<0.06 during an operation in an operation condition, where R (%) represents a radial expansion ratio at a center portion in a longitudinal direction, and L (%) represents a longitudinal expansion ratio, of the hollow fiber membrane module.

Liquid solution concentration methods and related systems involving osmosis units and energy recovery are generally described. In some embodiments, an osmotic system has a pump, a first reverse osmosis unit, a second reverse osmosis unit, and one or more energy recovery devices. Various embodiments are directed to features such as balancing streams, recirculation streams, and/or valving that alone or in combination may afford improved energy efficiency and/or system performance. Some embodiments may improve performance of certain types of energy recovery devices in combination with osmosis units, such as isobaric or turbine energy recovery devices.

An apparatus for preparing and dispensing a flocculant solution to dewatering an aqueous process stream includes a mixing pump, a maturing tank, and a feeding unit. The mixing pump mixes the flocculant solution and builds up a pressure onto the flocculant solution. The maturing pressure tank is fluidly connected with the mixing pump, so that the pressurized diluted flocculant solution is led from the mixing pump into the maturing pressure tank and matured therein under pressure that is above atmosphere pressure.

Procedure for the thermal hydrolysis of organic matter in steady state, with a double steam explosion and total energy recovery, which consists, as a minimum, of the 1) feeding stage, stepped pressurization and sequential injection of low, medium and high pressure level steam; 2) first stage of hydrolysis by consecutive steam explosion operations with the production of medium pressure level steam and thermal reaction; 3) second stage of hydrolysis consisting of steam explosion and production of low pressure steam. An installation for the implementation of the process, which consists of comprising pumps for stepped pressurization, fluid-steam mixers, valves, mixers, decompression elements, tanks, piping and instrumentation and control systems.

The present disclosure relates to a treatment method of wastewater containing heterocyclic organics comprising the following steps: (1) adding a persulfate to the wastewater containing heterocyclic organics in a reaction vessel; (2) heating the reaction vessel to a reaction temperature in an inert atmosphere, then introducing an oxygen-containing gas until a reaction pressure is reached for reaction, and after the reaction is completed, cooling and filtering the reaction resultant to obtain a filtrate as a treated effluent and a filter residue; no catalyst is added to the reaction system. The treatment method provided by the present disclosure not only can significantly reduce the treatment temperature of the conventional wet oxidation, but also can control the amount of generated spherical polymer and the removal efficiency of organic pollutants by control of reaction conditions. Wastewater purification and organics recovery and reuse are achieved at the same time.

A water treatment device including a first hydrocyclone and a biocidal fluid injector is described. The first hydrocyclone has an internal space, a water inlet for supplying water into the internal space, a base outlet for discharging at least a part of the water, and an apex outlet. The biocidal fluid injector is configured to inject a biocidal fluid into the internal space for eliminating organisms present in the water. The biocidal fluid injector is positioned such that a pressure within the injected biocidal fluid is lower than a head pressure of the first hydrocyclone.