Apparatus for the treatment of liquids contaminated by foreign substances

• US 6,126,819 A
• Filed: 03/31/1998
• Issued: 10/03/2000
• Est. Priority Date: 03/13/1998
• Status: Expired due to Fees

• Current Assignee: Rochem Ultrafiltrations Systeme Gesellschaft Fur Abwasserreinigung mbH
• Original Assignee: Rochem Ro-Wasserbehandlung GmbH
• Inventors: Vossenkaul, Klaus, Rautenbach, Robert, Heine, Wilhelm
• Primary Examiner(s): Drodge, Joseph W.
• Application Number:
  US09/052,487
• Time in Patent Office: 917 Days
• Field of Search: 210/139, 210/321.6, 210/321.69, 210/321.78, 210/321.79, 210/321.8, 210/321.88, 210/321.89, 210/321.9, 210/321.72, 210/323.1, 210/323.2 , 210/340, 210/410, 210/412, 210/483, 210/486, 210/497.01, 210/637, 210/406, 210/416.1, 210/456, 210/500.23, 96/7-9
• US Class Current: 210/139
• CPC Class Codes: B01D 2313/025 Specific membrane holders
• CPC Class Codes: B01D 2313/08 Flow guidance means within the module or the apparatus
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 2321/2066 Pulsated flow
• CPC Class Codes: B01D 63/024 with a single potted end
• CPC Class Codes: B01D 63/043 with separate tube sheets
• CPC Class Codes: B01D 63/065 on the outer surface thereof
• CPC Class Codes: B01D 65/08 Prevention of membrane fouling or of concentration polarisation

Abstract

In an apparatus for the treatment of liquids including foreign substances, particularly municipal and commercial waste waters, comprising a membrane separating structure having membrane elements, an inlet for receiving the liquid to be separated and passing it past the membrane elements whereby a permeant portion of the liquid permeates through the membranes and a retent portion becomes enriched with the foreign substances, and outlets for discharging the permeant portion and the retent portion, the membrane elements are arranged so as to form together flow channels extending longitudinally through the apparatus and adapted to guide the liquid straight through the flow channels along the membrane elements.

Claims

1. An apparatus for the treatment of liquids including foreign substances, comprising a membrane separating structure having opposite axial ends and including a membrane support element and membrane elements mounted in said membrane support element, said membrane separating structure having an inlet at one axial end for receiving the liquid to be separated and passing it past said membrane elements whereby a permeant portion of said liquid permeates through the membranes of said membrane elements and a retent portion of said liquid is enriched with said foreign substances, an outlet for discharging said permeant portion, and another outlet at the opposite axial end for discharging said retent portion, said membrane elements being arranged so as to form together at least one flow channel extending longitudinally through said apparatus and said membrane support element having flow openings in alignment with said at least one flow channel and adapted to guide said liquid to be treated and said retent portion in a straight line through said flow openings and said flow channel past the membrane elements forming said flow channel and out of said apparatus, repectively.

2. An apparatus according to claim 1, wherein said flow channel has a polygonal cross-section.

3. An apparatus according to claim 2, wherein said flow channel is hexagonal in cross-section.

4. An apparatus according to claim 1, wherein said flow channel is essentially circular in cross-section.

5. An apparatus according to claim 1, wherein said membrane elements are pillow type or pocket type membranes.

6. An apparatus according to claim 1, wherein said membrane elements are hollow fiber membranes.

7. An apparatus according to claim 1, wherein said apparatus includes a housing in which said membrane elements are disposed.

8. An apparatus according to claim 7, wherein said membrane elements have permeant discharge openings and said membrane support element is a closure element which is removably supported in said housing and on which said membrane elements are supported by their discharge openings.

9. An apparatus according to claim 8, wherein said closure element includes a permeant discharge passage to which the permeant which leaves the membrane elements through their discharge openings is conducted for discharge through said permeant discharge passage.

10. An apparatus according to claim 8, wherein said closure element consists of a support part for supporting said membrane elements and an admission part connected to said support part for the admission of said liquid to be separated.

11. An apparatus according to claim 10, wherein said membrane elements are mounted in said support part by a basic mounting means consisting of a hard-elastic connecting structure and a soft-elastic connecting means providing for some movability of said membrane elements in the interior of said housing.

12. An apparatus according to claim 8, wherein said housing is provided at least at a liquid supply side with a connecting element sealing said housing and having at least one passage for the liquid to be separated.

13. An apparatus according to claim 12, wherein said connecting element includes at least one permeant outlet which is in communication with at least one permeant outlet formed in said closure element.

14. An apparatus according to claim 8, wherein said membrane elements are closed at free ends thereof remote from open ends thereof by which they are supported.

15. An apparatus according to claim 14, wherein said membrane elements are freely movable in said liquid at their free ends.

16. An apparatus according to claim 1, wherein said liquid to be separated is pumped through said apparatus in a semi-cross-flow process.

17. An apparatus according to claim 1, wherein means are provided for admitting air to said apparatus in a timed fashion.

18. An apparatus according to claim 1, wherein a plurality of said apparatus are included in a housing and are arranged in series, one after another.

19. An apparatus according to claim 1, wherein said membrane elements are operable with at least one of excess pressure upstream or said elements and vacuum downstream of said elements.