Device and method for purifying drinking water
In order to improve the lifespan of the semi-permeable membrane or the yield of the reverse osmosis system in the treatment of drinking water by means of reverse osmosis, the invention provides a device for treating drinking water with at least one reverse osmosis vessel which is divided into at least two chambers by at least one semi-permeable membrane, wherein a first chamber has an inlet for the water to be treated and an outlet for the concentrate, and the second chamber has an outlet for the treated water, wherein the device comprises at least one pressure vessel which is connected to the outlet for the treated water via a line, wherein the device is designed in such a way that, in an idle state, treated water flows out of the pressure vessel, through the semi-permeable membrane and into the first chamber.
1. A method for purifying drinking water, comprising:
conveying, during an extraction operation mode, drinking water to be purified through a semipermeable membrane ( 11 ) in reverse osmosis operation and separating the drinking water into permeate and concentrate;
allowing, during an extraction stop phase, the permeate to flow into a pressure tank ( 4 ), whereby a supply of permeate accumulates and is pressurized in the pressure tank ( 4 ); and
backflushing, during an idle operation state, pressurized permeate accumulated in the pressure tank through the semipermeable membrane ( 11 ) and thereby displacing the concentrate on a concentrate side of the semipermeable membrane and removing deposits that may be present on the concentrate side of the semipermeable membrane.
2. The method for purifying drinking water as claimed in claim 1 ,
wherein a pressure difference across the semipermeable membrane ( 11 ) for conveying the drinking water through the semipermeable membrane ( 11 ) is in a range between 0.05 bar and 1 bar.
3. The method for purifying drinking water as claimed in claim 1 ,
wherein, on the concentrate side of the semipermeable membrane ( 11 ), the drinking water has a conductivity of less than 100 μS/cm in the idle operation state after the backflushing.
4. The method for purifying drinking water as claimed in claim 1 ,
wherein a concentration gradient across the semipermeable membrane ( 11 ) between the concentrate side and a permeate side is minimized in the idle operation state, after backflushing.
5. The method as claimed in claim 1 ,
wherein the semipermeable membrane is exposed to chlorine or another disinfectant only during the extraction operation mode and
wherein the semipermeable membrane is not exposed to chlorine or another disinfectant during the idle operation state.
6. The method as claimed in claim 1 , wherein
only permeate is used for backflushing in the idle operation state.