RO system and method for disinfecting lines of the RO system

• US 9,254,358 B2
• Filed: 09/04/2012
• Issued: 02/09/2016
• Est. Priority Date: 07/26/2012
• Status: Active Grant

• Current Assignee: Vivonic GmbH (Fresenius SE & Co. KGaA)
• Original Assignee: Manfred Volker
• Inventors: Volker, Manfred
• Primary Examiner(s): Zalasky, Katherine
• Assistant Examiner(s): LEBRON, BENJAMIN L
• Application Number:
  US13/602,656
• Publication Number:
  US 20140027379A1
• Time in Patent Office: 1,253 Days
• US Class Current: 1/1
• CPC Class Codes: A61M 1/16 with membranes
• CPC Class Codes: A61M 1/1656 Apparatus for preparing dialysates
• CPC Class Codes: A61M 1/1672 using membrane filters, e.g. for sterilising the dialysate
• CPC Class Codes: A61M 1/168 Sterilisation or cleaning before or after use
• CPC Class Codes: A61M 1/1688 with recirculation of the sterilising fluid
• CPC Class Codes: A61M 1/169 using chemical substances
• CPC Class Codes: B01D 2311/06 Specific process operations in the permeate stream
• CPC Class Codes: B01D 2311/2512 to feed side
• CPC Class Codes: B01D 61/08 Apparatus therefor
• CPC Class Codes: B01D 61/10 Accessories; Auxiliary operations
• CPC Class Codes: B01D 61/243 Dialysis
• CPC Class Codes: B01D 61/58 Multistep processes
• CPC Class Codes: B01D 65/022 Membrane sterilisation
• CPC Class Codes: C02F 1/441 by reverse osmosis
• CPC Class Codes: C02F 1/4672 by electrooxydation
• CPC Class Codes: C02F 2103/026 Treating water for medical or cosmetic purposes
• CPC Class Codes: C02F 2209/04 Oxidation reduction potential [ORP]
• CPC Class Codes: C02F 2209/23 O3
• CPC Class Codes: C02F 2307/14 Treatment of water in water supply networks, e.g. to prevent bacterial growth

Abstract

A circulation pump and an electrochemical ozone generator are integrated into the permeate return line of an RO system, and the permeate return line is connected in flow direction behind the circulation pump and the ozone generator by a recirculation line to the permeate supply line, which can form a closed circuit where the ozonized permeate circulates until all organic contaminants have been killed or decomposed by the ozone in that part of the line system. Valves are integrated, respectively, into the recirculation line and the permeate return line downstream of the branch of the recirculation line. During normal operation of the RO system, the recirculation line valve is connected for feeding connected dialysis devices while the permeate return line valve is open, so excessive permeate that was not taken by the dialysis devices can flow into the supply tank. Alternatively, the permeate can be discharged into an outlet.

Claims

1. A reverse osmosis (RO) system comprising an RO filter module which is subdivided by a membrane into a primary chamber and a secondary chamber, comprising a raw-water supply line leading to a ventilated supply tank, a line with an integrated pump leading from the ventilated supply tank to the primary chamber,

a concentrate line leading away from the primary chamber, and a permeate supply line leading from the secondary chamber, with at least one dialysis device being connectable to the permeate supply line by way of a branch line or secondary ring line, and

an adjacent permeate return line downstream of the at least one dialysis device leading back to the ventilated supply tank,

wherein a circulation pump and an electrochemical ozone generator are integrated into the permeate return line,

wherein a recirculation line connects the permeate return line downstream of the circulation pump and the ozone generator to the permeate supply line, with a recirculation valve integrated into the recirculation line and a return shutoff valve integrated into the permeate return line at a location downstream of the recirculation line, and

wherein a permeate return-line section, terminating at one end in the permeate return line downstream of the valve arranged therein, and at an opposite end in the permeate supply line, the opposite end of the permeate return-line section branching off from the permeate supply line upstream of the termination of the recirculation line into the permeate supply line, and

wherein a pressure holding valve is arranged in the permeate return-line section, so that the RO system can continue to operate even during a disinfecting mode and produces permeate without interruption and either an entire permeate volume or a proportion of the permeate flows back to the ventilated supply tank.

2. The RO system according to claim 1, wherein

a further valve is integrated into the permeate supply line downstream of the recirculation line to the permeate supply line.

3. The RO system according to claim 2, wherein

between the termination of the recirculation line into the permeate supply line and the further valve a connection line branches off to the permeate return line into which a further pressure holding valve is integrated.

4. The RO system according to claim 1, wherein

an outflow line, which leads to an outlet and into which an outflow valve is integrated, branches off at an intersection of the connection line and the permeate return line or branches off between said outflow line and the valve thereof.

5. The RO system according to claim 1, wherein

the amount of the ozone produced by the ozone generator is controllable by a selected applied voltage and/or a selected current.

6. The RO system according to claim 1, wherein

a measuring chamber is positioned in the permeate supply line or the permeate return line for monitoring the ozone concentration and for controlling the ozone amount in the liquid by way of redox potential or ozone sensors.

7. A method for disinfecting lines of a reverse osmosis (RO) system, comprising the steps of:

providing, during a cleaning process of the RO system, permeate with ozone while observing a predetermined ozone concentration and circulating ozonized permeate in a permeate supply line, permeate return line, and recirculation line, while the RO system continues to operate and produces permeate without interruption and either an entire volume or at least a proportion of the permeate coming from a secondary chamber of a filter module flows to a supply tank without mixing with ozone-enriched permeate,

flushing, after a predetermined time, the ozonized permeate into an outlet or to the supply tank of the RO system,

effectively preventing the ozone-enriched permeate from entering the supply tank by providing a pressure holding valve in a permeate return-line section that extends between the permeate supply line and the permeate return line, the permeate return line extending to the supply tank, and by providing a return shutoff valve in the permeate return line downstream of the recirculation line.

8. The method according to claim 7, wherein

the ozonized permeate fed to the supply tank disinfects the supply tank and preferably the line leading to the filter module, the primary chamber of the filter module, and the concentrate return line.

9. The method according to claim 7, wherein

the ozonized permeate flows to a closed water inlet valve of a dialysis device and discharges through an associated outflow line with an open flushing valve, while a partial stream of permeate exits out of the secondary chamber and flows into the permeate supply line.