Periodically operating a forward osmosis (FO) semi-permeable membrane element in reverse osmosis (RO), to yield product extraction on a feed side of the membrane, to flush out a concentration polarization (salt concentration of the feed side and dilution of draw solution on the draw side) across the membrane. Utilizing treated waste water to generate the flushing solution of low osmotic pressure, and gauge pressurizing the flushing solution to the gauge pressure of the draw solution to keep a constant gauge pressure of the solutions. FO process is interrupted every 5-20 minutes for a 10-60 seconds long flushing RO process, thereby increasing the FO throughput five fold and recovering power from the increased throughput, i.e. from the osmotic pressure of the brine.

The invention provides a process for purifying water containing soluble species capable of forming one or more sparingly soluble salts or minerals, said process comprising feeding a pressurized water stream into a treatment zone having one or more membranes disposed therein, passing said stream along said membrane(s) to recover a permeate and to withdraw a concentrate therefrom while periodically reversing the direction of the flow of said stream in said treatment zone, wherein the periodicity of the flow reversal is such that said one or more membranes are exposed to supersaturation conditions evolving in said water stream for a period of time which is less then the time required for said supersaturated water stream to precipitate one or more of said sparingly soluble salts and/or minerals therefrom.

The present application comprises symbiotic reverse osmosis train system for maximizing desalinated water recovery, meanwhile yielding high salinity brine suitable for osmotic power generation or commercial salt production; trains comprise series of number of cells operating in interrelated sequential pattern within a salinity field. Each cell forms a closed hydraulic brine loop having pumping means, power recovery means and shared semipermeable membranes between adjacent cells, defining the boundaries of flow path within a given cell, using applicant's technology for semipermeable Flat Sheet Membranes [FSM] or Hollow Fiber Membranes [HFM] intended for new and novel development in Hypersalinity processes and applications in desalination and osmotic power generation of brackish, seawater and brines of 15% salinity or more. Charging each cell in the train of plurality of cells with a formulated brine having a specified ionizable inorganic salt concentration and type, without permitting mixing of the given brines among the adjacent cells in the plurality of cells, allowing the train of multiple cells to achieve water recovery exceeding 85% with concentrated rejected brine of 28-30% salt content that is recoverable by evaporation/crystallization for commercial use. Highlighting, the first of its kind, a large scale Seashore Tower of flat Sheet membrane [FSM] for Induced Osmotic Desalination Plant of a capacity 28-56 million cubic meter per year (15 billion gallons per year) at a recovery rate of 85%, and rejected brine salinity of 28-30%, either used for sodium chloride salt recovery of 1-2 million metric tons per year, or to generate Induced Osmotic Power of 25-50 MW.

A novel filter media includes an array of raised features formed directly on the membrane surface, which create a feed channel. The predetermined configuration of features is dually optimized both for filtration in a first flow direction to maximize unobstructed fluid flow and prevent fouling. The same feature configuration is also optimized for enhancing/increasing turbulence and scouring of the membrane when the flow through the filter is reversed during a cleaning operation. The feature configuration can also be optimized to capture bubbles in reverse flow such that the captured bubbles can be oscillated to further scour the membrane and the features themselves (e.g., in their cavities, etc.).

A membrane filtration device includes a plurality of membrane separation units vertically disposed in multiple stages. The membrane separation unit has a primary side communicating with a backwash drainage system and a flushing-air supply system to receive supplied raw water and a secondary side communicating with a backwash-water supply system to collect permeate. The backwash-water supply system includes a backwash-water main pipe and a plurality of backwash-water branch pipes to feed the backwash water into the membrane separation units. The backwash drainage system includes a plurality of backwash-drainage branch pipes and a backwash-drainage main pipe connected in parallel to the backwash-drainage branch pipes. The flushing-air supply system includes an air main pipe for passing flushing air upward and a plurality of air branch pipes for feeding flushing air into the membrane separation units, the air branch pipes being connected in parallel to the air main pipe.

The present invention includes: a first sealing portion which has a first entry/exit selectively opened or closed by a first opening/closing valve and a second entry/exit selectively opened or closed by a second opening/closing valve and is configured to seal one end of a housing; a second sealing portion which has a third entry/exit selectively opened or closed by a third opening/closing valve and a fourth entry/exit selectively opened or closed by a fourth opening/closing valve, and is configured to seal the other end of the housing; and a controller which is configured to control the supply of raw water through any one of the first entry/exit and the second entry/exit or control the supply of raw water through any one of the third entry/exit and the fourth entry/exit.

A pump and valve arrangement (201), a dialysis system (10) comprising the pump and valve arrangement 201 and a method of operating a pump and valve arrangement (201). The pump and valve arrangement (201) has a dialyser having a semi-permeable membrane. The pump and valve arrangement (201) delivers dialysis fluid to and from the dialyser (12). The pump and valve arrangement (201) has a control system (450) configured to shuttle dialysis fluid between an inlet pump assembly and the dialyser (12) one or more times so as to agitate the surface of the semi-permeable membrane of the dialyser (12).

The present disclosure relates to a system (100) for reverse osmosis, RO, including a first membrane unit (10) and a first generator drive (G1). The first membrane unit (10) includes a first feed inlet (11), a first concentrate outlet (12), a first permeate outlet (13), and a first membrane (14). The first generator drive (G1) is fluidly connected to and disposed downstream of the first membrane unit (10). The first generator drive (G1) is configured for recuperating energy from a first fluid flow effluent from the first membrane unit (10) based on a first shaft speed of the first generator drive (G1) and for inducing oscillations of the first membrane (14) by modulating the first shaft speed to generate pressure pulses in the first fluid flow. The present disclosure further relates to a method of operating the system (100), a generator drive, and the use of a generator drive for inducing oscillations of one or more membranes in the system (100).

The present invention relates to a process for the purification of an aqueous hydrogen peroxide solution, comprising at least one treatment on a reverse osmosis membrane and at least one electrodeionization treatment. The invention also relates to a process for the preparation of an aqueous hydrogen peroxide solution, comprising at least one stage of synthesis of an aqueous hydrogen peroxide solution, at least one treatment on a reverse osmosis membrane and at least one electrodeionization treatment of said solution. The invention also relates to an aqueous hydrogen peroxide solution capable of being obtained by the purification process or the preparation process, as are defined above.