Apparatus and method for semi-permeable membrane cleaning in particular, applying series of pulsed water stroke, made simultaneously with osmosis backward flow causing superposed membrane directional shaking and fouling detachment. Pulsed water stroke provided by water stroke generator as several momentum sharp changes in gauge pressure and induce velocity pulse of residual brine flow. The pulsed water strokes ideally induce resonance in the membrane. Osmosis backward wash may be provided either by injection for predetermined injection time, additional solution selected in such way that net driving pressure becomes opposite to normal osmotic operation thereby providing a backward flow of permeate towards to the side opposite to normal operation mode, so as to lift said foulant, or by throttling permeate exiting from the permeate enclosure, until the net driving pressure value become equal to zero, during application of precise synchronized and opposing brine and permeate pressure strokes thereby providing a plurality of quick RO-FO-RO process changes. These procedures allow a membrane to be kept continuously clean and operate at higher recovery.

Apparatus and method for semi-permeable membrane cleaning in particular, applying series of pulsed water stroke, made simultaneously with osmosis backward flow causing superposed membrane directional shaking and fouling detachment. Pulsed water stroke provided by water stroke generator as several momentum sharp changes in gauge pressure and induce velocity pulse of residual brine flow. The pulsed water strokes ideally induce resonance in the membrane. Osmosis backward wash may be provided either by injection for predetermined injection time, additional solution selected in such way that net driving pressure becomes opposite to normal osmotic operation thereby providing a backward flow of permeate towards to the side opposite to normal operation mode, so as to lift said foulant, or by throttling permeate exiting from the permeate enclosure, until the net driving pressure value become equal to zero, during application of precise synchronized and opposing brine and permeate pressure strokes thereby providing a plurality of quick RO-FO-RO process changes. These procedures allow a membrane to be kept continuously clean and operate at higher recovery.

A purified water storage device includes a container including a cover, a bladder having a top secured to the cover and a bottom secured to a through hole of the container, a pipe for both venting and draining having an end connected to the bladder and communicating therewith, the pipe including a check valve, a water pipe having an end connected to the bottom of the bladder and communicating therewith, and a level sensor disposed externally of the container and having an end connected to the bottom of the bladder and communicating therewith. The watertight bladder is made of thermoplastic for medical or food purposes. The bladder can be replaced after a predetermined times of use rather than regular cleaning. Venting is carried out and overflow is prevented. The device has the same effect as an open container. Its material is safe and cleanness can be maintained.

A purified water storage device includes a container including a cover, a bladder having a top secured to the cover and a bottom secured to a through hole of the container, a pipe for both venting and draining having an end connected to the bladder and communicating therewith, the pipe including a check valve, a water pipe having an end connected to the bottom of the bladder and communicating therewith, and a level sensor disposed externally of the container and having an end connected to the bottom of the bladder and communicating therewith. The watertight bladder is made of thermoplastic for medical or food purposes. The bladder can be replaced after a predetermined times of use rather than regular cleaning. Venting is carried out and overflow is prevented. The device has the same effect as an open container. Its material is safe and cleanness can be maintained.

Provided is a drainage device and a system for controlling discharging of concentrated water in a water purification process. The device includes a valve cavity, a flowmeter, a transmission shaft and a control unit. The control unit is used for controlling a motion of the transmission shaft to adjust a liquid flow of the flowmeter in the valve cavity. The device inhibits an instantaneous impact of a liquid on the valve cavity to relieve vibration generated by the instantaneous impact; a special structural design is employed, which is favorable for controlling a flow of the concentrated water; moreover, the device is suitable for different pressure environments, achieves the objectives of small volume, controllable fitting area and small friction force; prevents leakage, and is easy to maintain and clean; and abnormal discharging of the concentrated water caused by water hammer and liquid impact in a water purification system is solved.

Provided is a drainage device and a system for controlling discharging of concentrated water in a water purification process. The device includes a valve cavity, a flowmeter, a transmission shaft and a control unit. The control unit is used for controlling a motion of the transmission shaft to adjust a liquid flow of the flowmeter in the valve cavity. The device inhibits an instantaneous impact of a liquid on the valve cavity to relieve vibration generated by the instantaneous impact; a special structural design is employed, which is favorable for controlling a flow of the concentrated water; moreover, the device is suitable for different pressure environments, achieves the objectives of small volume, controllable fitting area and small friction force; prevents leakage, and is easy to maintain and clean; and abnormal discharging of the concentrated water caused by water hammer and liquid impact in a water purification system is solved.

Pressure processing systems disclosed herein comprise rotating fluid flow paths. Transfer of angular momentum between the working fluid and the fluid flow path may be configured to increase pressure within the system and/or recover energy used to increase pressure within the system. Rotation of pressure processing systems may be configured to alter working fluid pressure within the pressure processing system. Filtration and/or chemical processes may be performed within a pressure processing portion of such systems. Working fluid may be introduced or recovered from the system at various radial positions.

Pressure processing systems disclosed herein comprise rotating fluid flow paths. Transfer of angular momentum between the working fluid and the fluid flow path may be configured to increase pressure within the system and/or recover energy used to increase pressure within the system. Rotation of pressure processing systems may be configured to alter working fluid pressure within the pressure processing system. Filtration and/or chemical processes may be performed within a pressure processing portion of such systems. Working fluid may be introduced or recovered from the system at various radial positions.

Pressure processing systems disclosed herein comprise rotating fluid flow paths. Transfer of angular momentum between the working fluid and the fluid flow path may be configured to increase pressure within the system and/or recover energy used to increase pressure within the system. Rotation of pressure processing systems may be configured to alter working fluid pressure within the pressure processing system. Filtration and/or chemical processes may be performed within a pressure processing portion of such systems. Working fluid may be introduced or recovered from the system at various radial positions.

Pressure processing systems disclosed herein comprise rotating fluid flow paths. Transfer of angular momentum between the working fluid and the fluid flow path may be configured to increase pressure within the system and/or recover energy used to increase pressure within the system. Rotation of pressure processing systems may be configured to alter working fluid pressure within the pressure processing system. Filtration and/or chemical processes may be performed within a pressure processing portion of such systems. Working fluid may be introduced or recovered from the system at various radial positions.