A water desalination system includes a first set of ultrafiltration membranes, a second set of ultrafiltration membranes, a first backwashing system configured to treat at least one of the first set of ultrafiltration membranes or the second set of ultrafiltration membranes with brine generated by a reverse osmosis process, and a second backwashing system configured to treat at least one of the first set of ultrafiltration membranes or the second set of ultrafiltration membranes with one or more chemicals and reverse osmosis permeate water.

A control method is provided for a filter system, which includes at least one filter element (2). The method includes continuously recording a total energy consumption (E.sub.G) during a filtration cycle (22) of the filter system. The total energy consumption (E.sub.G) includes at least of the energy consumption (E.sub.B) for a physical cleaning (24) and the energy consumption (E.sub.P) for the subsequent production cycle (23) up to a predefined, in particular current point in time. The method further includes computing a relative energy consumption (E.sub.rel) by way of division of the recorded total energy consumption (E.sub.G) by a net permeate volume (Q.sub.N) which has been produced during the filtration cycle (22) up to the predefined point in time and starting a physical cleaning (24) in dependence on the relative energy consumption or of a characteristic value derived from this.

An aeration amount control system includes a control device for determining a first target aeration amount as the target aeration amount, and after having determined the first target aeration amount, determining a second target aeration amount as the target aeration amount, wherein, if a first change amount of the transmembrane pressure difference of the separation membrane calculated by the measurement device for the aeration performed on the basis of the first target aeration amount by the aeration device is greater than a second change amount of the transmembrane pressure difference of the separation membrane calculated by the measurement device for the aeration performed on the basis of the second target aeration amount by the aeration device, the control device determines a value, smaller than the second target aeration amount, as a third target aeration amount.

The present invention relates to a device (1) for the treatment of biological material (2) comprising a concentration circuit (3) having at least one concentration filter (20), at least one supply conduit (30) of the biological material (2), and a concentration section (40) interposed between separation filter (10) and concentration filter (20) and defining an inner volume configured to accommodate a fraction of interest (2a) of the biological material (2). A discharge conduit (50) is connected to the second access (22) of the concentration filter (20) downstream of the concentration section (40), and an infusion line (60) is connected to the concentration circuit (3). The concentrated fraction of interest (2a) of biological material (2) may be withdrawn from a collection channel (70) or by removing the entire concentration section (40) from the rest of the circuit.

Sterilization is achieved while the filtration performance of membranes is maintained. In a hollow fiber membrane module 1, a hollow fiber membrane bundle 3 is accommodated in a module case 5. In the hollow fiber membrane module 1, both ends of the hollow fiber membrane bundle 3 are integrated with the module case 5 by a potting material. A storage liquid is contained in 90% or more of the pores of the hollow fiber membrane bundle 3. Space inside the module case 5 is filled with a gas free of viable bacteria and the storage liquid.

Provided is a method for washing a hollow fiber membrane module which comprises a hollow fiber membrane for filtering raw water containing a suspended component, said method comprising, in the following order, a first washing step for removing a suspended component that is accumulated on the hollow fiber membrane and a second washing step for carrying out an air scrubbing process in which gas is caused to pass through at least to the raw water side of the hollow fiber membrane, wherein, out of water that existed in the hollow fiber membrane module before washing, water in an amount corresponding to not less than 50 vol % of the capacity of the hollow fiber membrane module is removed in the first washing step.

A separation recovery system for separating and recovering an object to be separated includes a metal porous membrane which has a first principal surface and a second principal surface facing the first principal surface and has a plurality of through-holes extending between the first principal surface and the second principal surface, a supply device which supplies a first fluid containing the object to be separated from the first principal surface of the metal porous membrane toward the second principal surface, and a backwash device which supplies a second fluid containing a plurality of particles larger than a size of the plurality of through-holes of the metal porous membrane in a direction from the second principal surface of the metal porous membrane toward the first principal surface.

Algae harvesting and cultivating systems and methods for producing high concentrations of algae product with minimal energy. In an embodiment, a dead-end filtration system and method includes at least one tank and a plurality hollow fiber membranes positioned in the at least one tank. An algae medium is pulled through the hollow fiber membranes such that a retentate and a permeate are produced.

A filtration apparatus (10) for treating a fluid comprises a vessel (12), a first partition plate (18) dividing the vessel into first and second chambers (22, 26) and defining a through hole (40), and a filtration module (30) located within the second chamber (26) and including a body section (32) defining an outer diameter which is greater than the diameter of the through hole (40) in the first partition plate (18). The apparatus (10) further comprises a reducing connector (36) having a first end secured to the body section (32) of the filtration module (30) and a second end sealed relative to the through hole (40) in the first partition plate (18) to permit communication between the filtration module (30) and the first chamber (22). In a disclosed embodiment the apparatus (10) includes a second partition plate (20) such that the vessel is divided into first, second and third chambers (22, 24, 26), wherein the filtration module (30) is mounted between the partition plates (18, 20).

A method of air scouring an immersed membrane is described in this specification. The method comprising a step of adjusting one or more aeration parameters: between successive permeation, back pulse or relaxation cycles; during a permeation cycle; or, between a permeation cycle and a backpulse or relaxation cycle.