This reverse osmosis membrane processing method comprises adjusting processing-target water to a pH range of 4 to 8 and passing the water through a reverse osmosis membrane device. The reverse osmosis membrane processing method is characterized in that alkaline water having a pH of 9.5 or higher is brought into contact intermittently with the reverse osmosis membrane of the reverse osmosis membrane device. Raw water may be preprocessed with active carbon, or the like, to serve as the processing-target water. If the processing-target water has a pH of 9.5 or higher, this processing-target water may be used as the alkaline water.

This reverse osmosis membrane processing method comprises adjusting processing-target water to a pH range of 4 to 8 and passing the water through a reverse osmosis membrane device. The reverse osmosis membrane processing method is characterized in that alkaline water having a pH of 9.5 or higher is brought into contact intermittently with the reverse osmosis membrane of the reverse osmosis membrane device. Raw water may be preprocessed with active carbon, or the like, to serve as the processing-target water. If the processing-target water has a pH of 9.5 or higher, this processing-target water may be used as the alkaline water.

The present disclosure is directed to filtering technologies that combine elements of continuous and batch NF/RO based on the constraints of the end-user facility to achieve a target balance between, for instance, recovery and power consumption, and to reduce long term operating cost of a plant. A method for extending batch operation into a second induction period with antiscalant injection is also disclosed herein, with the second induction period allowing for yet higher water recovery.

The present disclosure is directed to filtering technologies that combine elements of continuous and batch NF/RO based on the constraints of the end-user facility to achieve a target balance between, for instance, recovery and power consumption, and to reduce long term operating cost of a plant. A method for extending batch operation into a second induction period with antiscalant injection is also disclosed herein, with the second induction period allowing for yet higher water recovery.

The invention provides novel remediants and methods for remediating all biological and synthetic fibers; and biological and synthetic membranes. The remediants comprise a chemically or biologically active or inactive material, in the form of particles which are on average less than the pore size of the selected fiber, or larger than the pore size of the selected membrane, and a polymeric elution supporter suspension which is interactive with an environmentally acceptable solvent. The elution support suspension mixture is capable of maintaining the particles in a persistent suspension which can permeate through the interwoven fiber layers and pores; or brush membrane surfaces and pores, due to it small or large size, thereby delivering the remediant to the desired fiber and membrane locations.

The invention provides novel remediants and methods for remediating all biological and synthetic fibers; and biological and synthetic membranes. The remediants comprise a chemically or biologically active or inactive material, in the form of particles which are on average less than the pore size of the selected fiber, or larger than the pore size of the selected membrane, and a polymeric elution supporter suspension which is interactive with an environmentally acceptable solvent. The elution support suspension mixture is capable of maintaining the particles in a persistent suspension which can permeate through the interwoven fiber layers and pores; or brush membrane surfaces and pores, due to it small or large size, thereby delivering the remediant to the desired fiber and membrane locations.

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).

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).

Processes and systems for filtering a liquid sample are provided. Batches of a liquid sample can be routed to two or more cycling tanks (e.g., first and second cycling tanks). Upon filling a first cycling tank, a first batch of the liquid sample can be routed to a filtration assembly by a continuous diafiltration process that includes routing produced retentate back to the first cycling tank or to a collection vessel. Upon filling a second cycling tank, a second batch of the liquid sample is routed to the filtration assembly by a continuous diafiltration process that includes routing produced retentate back to the second cycling tank or to the collection vessel. The filling and continuous diafiltration of batches of the liquid sample continues to alternate between the two or more cycling tanks until a total product volume is processed.

Processes and systems for filtering a liquid sample are provided. Batches of a liquid sample can be routed to two or more cycling tanks (e.g., first and second cycling tanks). Upon filling a first cycling tank, a first batch of the liquid sample can be routed to a filtration assembly by a continuous diafiltration process that includes routing produced retentate back to the first cycling tank or to a collection vessel. Upon filling a second cycling tank, a second batch of the liquid sample is routed to the filtration assembly by a continuous diafiltration process that includes routing produced retentate back to the second cycling tank or to the collection vessel. The filling and continuous diafiltration of batches of the liquid sample continues to alternate between the two or more cycling tanks until a total product volume is processed.