Treatment system having spiral membrane element and method for operating the treatment system

• US 20030127388A1
• Filed: 12/16/2002
• Published: 07/10/2003
• Est. Priority Date: 12/17/2001
• Status: Abandoned Application

• Current Assignee: Nitto Denko Corporation
• Original Assignee: Nitto Denko Corporation
• Inventors: Yoshikawa, Hiroshi, Ando, Masaaki, Watanabe, Terutaka
• Application Number:
  US10/319,602
• Publication Number:
  US 20030127388A1
• Time in Patent Office: Days
• US Class Current: 210/636
• CPC Class Codes: B01D 2311/04 Specific process operations in the feed stream; Feed pretreatment
• CPC Class Codes: B01D 2311/12 Addition of chemical agents
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 61/025 Reverse osmosis; Hyperfiltration
• CPC Class Codes: B01D 61/04 Feed pretreatment
• CPC Class Codes: B01D 63/10 Spiral-wound membrane modules
• CPC Class Codes: B01D 63/101 Spiral winding
• CPC Class Codes: B01D 63/12 comprising multiple spiral-wound assemblies
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: B01D 69/10 Supported membranes; Membrane supports
• CPC Class Codes: B01D 69/1071 Woven, non-woven or net mesh
• CPC Class Codes: C02F 1/441 by reverse osmosis
• CPC Class Codes: C02F 2103/04 for obtaining ultra-pure water
• CPC Class Codes: C02F 2303/16 Regeneration of sorbents, filters

Abstract

At the time of back washing of a treatment system, filtrate 2 is reverse-osmosis-filtrated by a reverse osmosis membrane separation device 51 so as to be separated into permeate 3 and concentrate 4. The concentrate 4 obtained from the reverse osmosis membrane separation device 51 is supplied as washing water into a spiral membrane element 10 through pipes 21 and 21a. On this occasion, the concentrate 4 is pressurized by a supply pump 104, so that a separation membrane is back-washed under a back pressure higher than 0.05 MPa but not higher than 0.3 MPa.

Claims

1. A treatment system comprising:

a spiral membrane element including a porous hollow tube, and an envelope-like separation membrane wound on an outer circumferential surface of said porous hollow tube, said spiral membrane element capable of being back-washed under a back pressure higher than 0.05 MPa but not higher than 0.3 MPa;

a reverse osmosis membrane separation device provided on a downstream side of said spiral membrane element; and

a washing liquid supply system provided so that at least a part of permeated liquid or concentrated liquid obtained from said reverse osmosis membrane separation device at the time of filtration by said spiral membrane element is supplied as washing liquid to said spiral membrane element at the time of washing said spiral membrane element.

2. A treatment system according to claim 1, wherein said washing includes back washing, which is performed by said washing liquid supply system so that at least a part of said permeated liquid or concentrated liquid ejected from said reverse osmosis membrane separation device is supplied to said spiral membrane element under a pressure higher than 0.05 MPa but not higher than 0.3 MPa.

3. A treatment system according to claim 1, wherein said washing includes flushing washing, which is performed by said washing liquid supply system so that at least a part of said permeated liquid or concentrated liquid ejected from said reverse osmosis membrane separation device is supplied to said spiral membrane element at the time of filtration by said spiral membrane element.

4. A treatment system according to claim 1, wherein said washing liquid supply system is provided so that at least a part of said permeated liquid or concentrated liquid ejected from said reverse osmosis membrane separation device is supplied, together with chemicals, to said spiral membrane element.

5. A treatment system according to claim 1, wherein said concentrated liquid or permeated liquid ejected from said reverse osmosis membrane separation device has a residual pressure higher than 0.05 MPa but not higher than 0.3 MPa, so that said washing liquid supply system supplies at least a part of said concentrated liquid or permeated liquid to said spiral membrane element under said residual pressure at the time of said washing.

6. A treatment system according to claim 1, wherein:

a plurality of spiral membrane elements as defined in claim 1 are provided in parallel with one another, said spiral membrane elements being washed successively so that while one of said spiral membrane elements is washed, at least one of the other spiral membrane elements is operated for filtration; and

said washing liquid supply system is provided so that at least a part of permeated liquid or concentrated liquid obtained from said reverse osmosis membrane separation device at the time of filtration by the plurality of spiral membrane elements is supplied as washing liquid to each spiral membrane element at the time of washing said spiral membrane element.

7. A method of operating a treatment system including a spiral membrane element, and a reverse osmosis membrane separation device provided on a downstream side of said spiral membrane element, said spiral membrane element having a porous hollow tube, and an envelope-like separation membrane wound on an outer circumferential surface of said porous hollow tube, said spiral membrane element capable of being back-washed under a back pressure higher than 0.05 MPa but not higher than 0.3 MPa, said method comprising the step of:

supplying at least a part of permeated liquid or concentrated liquid obtained from said reverse osmosis membrane separation device at the time of filtration by said spiral membrane element, as washing liquid, to said spiral membrane element at the time of washing said spiral membrane element.

8. A method of operating a treatment system according to claim 7, wherein said washing includes back washing, which is performed so that at least a part of said permeated liquid or concentrated liquid ejected from said reverse osmosis membrane separation device is supplied to said spiral membrane element under a pressure higher than 0.05 MPa but not higher than 0.3 MPa.

9. A method of operating a treatment system according to claim 7, wherein said washing includes flushing washing, which is performed so that at least a part of said permeated liquid or concentrated liquid ejected from said reverse osmosis membrane separation device is supplied to said spiral membrane element at the time of filtration by said spiral membrane element.

10. A method of operating a treatment system according to claim 7, wherein at least a part of said permeated liquid or concentrated liquid ejected from said reverse osmosis membrane separation device is supplied, together with chemicals, to said spiral membrane element.

11. A method of operating a treatment system according to claim 7, wherein said concentrated liquid or permeated liquid ejected from said reverse osmosis membrane separation device has a residual pressure higher than 0.05 MPa but not higher than 0.3 MPa, so that at least apart of said concentrated liquid or permeated liquid is supplied to said spiral membrane element under said residual pressure at the time of said washing.

12. A method of operating a treatment system, wherein:

a plurality of spiral membrane elements as defined in claim 7 are provided in parallel with one another, said spiral membrane elements being washed successively so that while one of said spiral membrane elements is washed, at least one of the other spiral membrane elements is operated for filtration; and

at least a part of permeated liquid or concentrated liquid obtained from said reverse osmosis membrane separation device at the time of filtration by the plurality of spiral membrane elements is supplied as washing liquid to each spiral membrane element at the time of washing said spiral membrane element.