Method of cleaning membranes

• US 8,956,464 B2
• Filed: 06/11/2010
• Issued: 02/17/2015
• Est. Priority Date: 06/11/2009
• Status: Active Grant

• Current Assignee: Evoqua Water Technologies LLC
• Original Assignee: Evoqua Water Technologies LLC
• Inventors: Zauner, Peter, Zha, Fufang
• Primary Examiner(s): Kornakov, Michael
• Assistant Examiner(s): WHATLEY, KATELYN B
• Application Number:
  US12/813,748
• Publication Number:
  US 20110056522A1
• Time in Patent Office: 1,712 Days
• Field of Search: 134/27, 134/28
• US Class Current: 134/27
• CPC Class Codes: B01D 2321/168 Use of other chemical agents
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration

Abstract

Methods for cleaning polymeric microfiltration or ultrafiltration membranes. The membrane may be contacted with a first cleaning solution including at least one oxidising agent. A second cleaning solution including at least one reducing agent may then be introduced to the membrane and first cleaning solution. The oxidising and reducing agents may undergo a neutralisation reaction to form an oxidation-neutral mixed cleaning solution. The membrane may be simultaneously cleaned during the neutralisation reaction.

Claims

1. A method for cleaning a porous polymeric membrane contained in a tank of a wastewater treatment plan including a membrane bioreactor, the method comprising:

introducing a first cleaning solution including a chlorine-based oxidizing agent selected from the group consisting of chlorine, hypochlorites, chlorites, chlorates, perchlorates, and chloramines to a tank containing the membrane;

contacting at least a portion of the membrane with the first cleaning solution for a first time period;

introducing a second cleaning solution including a reducing agent directly to the tank containing the membrane and the first cleaning solution after the first time period has elapsed, the second cleaning solution neutralizing an oxidizing residual of the first cleaning solution and forming an acid species from a reaction between the first cleaning solution and the second cleaning solution;

soaking at least a portion of the membrane with the acid species for a second time period; and

discharging a solution including the acid species from the tank after the second time period has elapsed;

adjusting the pH level of the discharged solution including the acid species;

introducing the discharged acid species into a head of the wastewater treatment plant; and

mixing the discharged acid species with an incoming wastewater flow into the wastewater treatment plant.

2. The method of claim 1, wherein the membrane is a hollow-fiber membrane.

3. The method of claim 1, wherein the oxidizing agent is selected from the group consisting of sodium hypochlorite and monochloramine.

4. The method of claim 1, wherein the reducing agent is selected to neutralize the oxidizing residual from the oxidizing agent.

5. The method of claim 4, wherein the reducing agent is selected from the group consisting of bisulphites, metabisulfites, sulphites, and thiosulfates.

6. The method of claim 5, wherein the reducing agent is selected from the group consisting of sodium metabisulfite, sodium thiosulphate, and sodium bisulfite.

7. The method of claim 1, wherein the second cleaning solution further includes an enhancing agent.

8. The method of claim 7, wherein the enhancing agent is a surfactant or a chelating agent selected from the group consisting of polycarboxylic acids and salts thereof.

9. The method of claim 7, wherein the enhancing agent is selected from the group consisting of citric acid, a salt thereof, ethylenediaminetetraacetic acid (EDTA), a salt thereof, oxalic acid, and a salt thereof.

10. The method of claim 7, wherein a concentration of the enhancing agent is between 0.01 wt % and 1.0 wt %.

11. The method of claim 10, wherein the concentration of the enhancing agent is 0.5 wt %.

12. The method of claim 1, wherein a concentration of the oxidizing agent in the first cleaning solution is between 0.01 wt % and 2 wt %.

13. The method of claim 12, wherein the concentration of the oxidizing agent in the first cleaning solution is approximately 0.1 wt %.

14. The method of claim 12, wherein a concentration of the reducing agent is between 0.01 wt % and 2 wt %.

15. The method of claim 14, wherein the concentration of the reducing agent is approximately 0.15 wt %.

16. The method of claim 1, wherein the first time period is at least about three hours, and wherein the second time period is at least about two hours.

17. The method of claim 1, wherein the membrane is cleaned at ambient temperature and pressure.

18. The method of claim 1, further comprising recirculating at least one of the first cleaning solution and the acid species in the tank.

19. The method of claim 1, further comprising filtering at least one of the first cleaning solution and the acid species through the membrane from an outside wall of the membrane to a lumen of the membrane.

20. The method of claim 1, further comprising soaking the membrane in the first cleaning solution.

21. The method of claim 1, further comprising air scouring the membrane while contacting the membrane with at least one of the first cleaning solution and the acid species.

22. The method of claim 1, wherein the second solution is introduced while backwashing the membrane.

23. The method of claim 1, wherein the first cleaning solution targets organic membrane foulants, and wherein the acid species targets inorganic membrane foulants.

24. A method of facilitating cleaning of a porous polymeric membrane in place, the porous polymeric membrane being contained in a tank of a wastewater treatment plant including a membrane bioreactor, the method comprising:

providing a first cleaning solution including at least one chlorine-based oxidizing agent selected from the group consisting of chlorine, hypochlorites, chlorites, chlorates, perchlorates, and chloramines and a second cleaning solution including at least one reducing agent; and

providing instructions to;

contact at least a portion of the membrane with the first cleaning solution in a membrane tank for a first time period to target organic membrane foulants;

introduce the second cleaning solution directly to the membrane tank including the first cleaning solution after the first time period has elapsed, a mixture of the first cleaning solution and the second cleaning solution forming an acid species from a reaction between the first cleaning solution and the second cleaning solution;

recirculate the acid species through the membrane; and

contact at least a portion of the membrane with the acid species for a second time period of at least about two hours to target inorganic membrane foulants;

discharge a solution including the acid species after the second time period has elapsed;

adjust a pH level of the discharged solution including the acid species;

introduce the acid species into a head of the wastewater treatment plant after the second time period has elapsed; and

mix the acid species with an incoming wastewater flow into the wastewater treatment plant.