System for operation of multiple membrane filtration assemblies

• US 6,214,231 B1
• Filed: 08/27/1999
• Issued: 04/10/2001
• Est. Priority Date: 08/27/1999
• Status: Expired due to Term

• Current Assignee: Zenon Technology Partnership
• Original Assignee: Zenon Environmental Incorporated
• Inventors: Janson, Arnold Frederic, Low, Steven Ian, Cote, Pierre Lucien, Pedersen, Steven Kristian
• Primary Examiner(s): Drodge, Joseph W.
• Application Number:
  US09/384,638
• Time in Patent Office: 592 Days
• Field of Search: 210/90, 210/321.69, 210/321.79, 210/321.8, 210/321.88, 210/321.89, 210/333.01, 210/340, 210/341, 210/636, 210/650, 210/741, 210/637, 210/791, 264/451
• US Class Current: 210/636
• CPC Class Codes: B01D 2313/125 Discharge manifolds
• CPC Class Codes: B01D 2313/54 Modularity of membrane module elements
• CPC Class Codes: B01D 2315/06 Submerged-type; Immersion type
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/16 Use of chemical agents
• CPC Class Codes: B01D 2321/2066 Pulsated flow
• CPC Class Codes: B01D 61/146 comprising multiple ultrafiltration steps
• CPC Class Codes: B01D 61/149 Multistep processes comprising different kinds of membrane processes selected from ultrafiltration or microfiltration
• CPC Class Codes: B01D 61/18 Apparatus therefor
• CPC Class Codes: B01D 61/22 Controlling or regulating
• CPC Class Codes: B01D 63/043 with separate tube sheets
• CPC Class Codes: B01D 63/046 in separate housings
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: B01D 65/102 Detection of leaks in membranes
• CPC Class Codes: C02F 1/444 by ultrafiltration or microfiltration

Abstract

Limitation of the number of cassettes in an assembly currently used for the production of permeate is obviated by grouping plural cassettes into racks one or more of which may be isolated while permeate production from the remaining racks is uninterrupted. Ancillary functions such as back-pulsing, chemical cleaning and testing for defects in membranes (“integrity testing”) in one or more racks may proceed while production of permeate continues. The number of racks in a bank is determined by the period of the overall filtration cycle, typically 15 min, in which filtration period the ancillary period is a minor portion, typically 30 sec. The racks make it possible to use automatic on/off valves which open and close quicker than larger ones. The resulting saving in time, energy, and equipment costs, which when back-pulsing with permeate is surprisingly economical, is even greater when a chemical cleaning solution is to be used. In addition, the saving in cost of equipment and avoiding the wear and tear of pumps which are intermittently stopped and started, produces unexpected economic benefits. For even greater savings in operating costs, a bank of cassettes, or a bank of racks may be operated with a “gravity flow” system.

Claims

1. In a large plant comprising a bank of multiple cassettes for filtering a contaminated substrate, immersed in said substrate, and in open fluid communication with each other, each cassette comprising a multiplicity of membrane modules connected for operation in parallel in the cassette, a method comprising,

connecting said multiple cassettes having a total of at least 100 modules, for operation in parallel in said bank without selectively isolating any module thereof;

isolating at least one cassette in said bank for a predetermined period of time sufficient to execute an ancillary operation with said cassette; and

,

continuously withdrawing permeate from said bank and from said cassettes left unisolated.

2. The method of claim 1 wherein each said module has a membrane area of at least 10 m²and comprises fibers greater than 0.5 meter long;

and, providing one automatic cassette valve on a manifold in each cassette to control withdrawal of permeate from modules in each cassette, and to control flow of back-pulsing fluid into modules in each cassette, respectively.

3. The method of claim 2 including isolating from 6 percent to 50 percent of the cassettes in said bank to provide at least one isolated cassette;

and, said ancillary operation comprises flowing a back-pulsing fluid through said isolated cassette.

4. The method of claim 3 wherein said back-pulsing fluid is selected from the group consisting of permeate, air and a mixture thereof.

5. The method of claim 2 wherein said ancillary operation includes flowing a chemical cleaning fluid through modules in from 1-2 cassettes while remaining cassettes remain in a permeate production mode.

6. The method of claim 2 wherein said ancillary operation includes pressurizing said modules in an isolated cassette with a pressurizing gas while substantially all remaining cassettes remain in a permeate production mode.

7. The method of claim 6 comprising measuring pressure decay to determine whether a membrane is defective.

8. The method of claim 2 comprising,

connecting said cassette manifolds to a vacuum generating means;

exerting a sufficient vacuum in said cassette manifold to withdraw permeate therein, said manifolds each having an automatic valve to shut off flow of said permeate when said modules in said cassette are to be back-pulsed;

discharging permeate into a wet well;

isolating at least one cassette in said bank for a predetermined period of time sufficient to execute an ancillary operation with said cassette;

providing means to back-pulse said modules with back-pulsing fluid; and

,

discharging permeate from said wet well.

9. The method of claim 8 wherein, once started, flow of permeate from said bank of cassettes is self-regulating.

10. In a large plant a bank comprising a bank of racks for filtering a contaminated substrate, immersed in said substrate, and in open fluid commuication with each other, each rack comprising a multiplicity of membrane modules connected for operation in parallel in cassettes, a method comprising,

connecting multiple cassettes having a total of at least 100 modules, for operation in parallel in respective racks without selectively isolating any module in said cassettes, and without selectively isolating any cassettes in said racks;

connecting multiple racks for operation in parallel in said bank of racks;

isolating at least one rack in said bank for a predetermined period of time sufficient to execute an ancillary operation with said rack; and

,

continuously withdrawing permeate from said bank and said racks left unisolated.

11. The method of claim 10 wherein each said module has a membrane area of at least 10 m² and comprises fibers greater than 0.5 meter long;

and,

including connecting said multiple cassettes to cassette manifolds and

connecting said cassette manifolds to rack manifolds

connecting said rack manifolds to a main manifold; and

,

providing one automatic rack valve on each rack manifold to control withdrawal of permeate from cassettes in each rack, and to control flow of back-pulsing fluid into cassettes in each rack, respectively.

12. The method of claim 11 including isolating from 6 percent to 50 percent of the racks in said bank to provide at least one isolated rack;

and,

said ancillary operation comprises flowing a back-pulsing fluid through said isolated rack.

13. The method of claim 12 wherein said back-pulsing fluid is selected from the group consisting of permeate, air and a mixture thereof.

14. The method of claim 11 wherein said ancillary operation includes flowing a chemical cleaning fluid through membrane modules in from 1-2 racks while remaining racks remain in a permeate production mode.

15. The method of claim 11 wherein said ancillary operation includes pressurizing said isolated rack with a pressurizing gas while remaining racks remain in a permeate production mode.

16. The method of claim 15 comprising measuring pressure decay to determine whether a membrane is defective.

17. The method of claim 11 comprising,

connecting said rack manifolds to a vacuum generating means;

exerting a sufficient vacuum in said cassette rack manifold to withdraw permeate therein, said rack manifolds each having an automatic valve to shut off flow of said permeate when said modules in said rack are to be back-pulsed;

discharging permeate into a wet well;

isolating at least one rack in said bank of racks for a predetermined period of time sufficient to execute an ancillary operation with said rack;

providing means to back-pulse said modules with back-pulsing fluid; and

,

discharging permeate from said wet well.

18. The method of claim 17 wherein, once started, flow of permeate from said bank of racks is self-regulating.

19. A large filtration plant comprising a bank of multiple cassettes for the production of permeate flowing immersed in a reservoir of substrate to be filtered, comprising,

said bank including a total of at least 100 modules of fibers, said modules connected in open fluid communication for operation in parallel in cassettes;

said multiple cassettes being connected in open fluid communication with a cassette manifold and each other, and connected for operation in parallel in said bank;

multiple, automatically actuated on/off valves including two cassette valves to selectively control flow of fluid through said cassette manifold; and

,

means to selectively open and close said automatically actuated on/off valves to isolate a cassette so as to continuously withdraw permeate from said bank.

20. The filtration plant of claim 19 including,

vacuum generating means to exert a sufficient vacuum in said cassette manifold to generate flow of permeate into said modules, and,

a wet well in which permeate is collected.

21. The filtration plant of claim 19 wherein,

said multiple cassettes are connected in open fluid communication with each other, and also with a rack manifold, for operation in parallel in a bank or racks comprising at least two racks;

multiple, automatically actuated on/off valves include two rack valves to selectively control flow of fluid through said rack manifold; and

,

means to selectively open and close said automatically actuated on/off valves to isolate a rack.

22. The filtration plant of claim 21 including,

vacuum generating means to exert a sufficient vacuum to generate flow of permeate into said modules;

and,

a wet well in which permeate is collected.