Enzymatic treatment of alginate to reduce membrane fouling for water or wastewater purification

• US 9,352,284 B2
• Filed: 07/19/2012
• Issued: 05/31/2016
• Est. Priority Date: 07/22/2011
• Status: Active Grant

• Current Assignee: Purdue Research Foundation (Purdue University)
• Original Assignee: Purdue Research Foundation (Purdue University)
• Inventors: Chen, Dong
• Primary Examiner(s): Menon, Krishnan S
• Application Number:
  US13/552,746
• Publication Number:
  US 20130037484A1
• Time in Patent Office: 1,412 Days
• Field of Search: 210/632, 210/636, 210/606, 210777-779, 435262-264
• US Class Current: 1/1
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/14 Use of concentrate
• CPC Class Codes: B01D 2321/166 Use of enzymatic agents
• CPC Class Codes: B01D 61/145 Ultrafiltration
• CPC Class Codes: B01D 61/147 Microfiltration
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: B01D 65/08 Prevention of membrane fouling or of concentration polarisation

Abstract

This disclosure examines using alginate lyase to catalytically degrade alginate in order to decrease affinity and fouling potential to membranes of 0.2 and 0.02 μm pore size, respectively within a process line of a filtration system. Enzymatically treated alginate caused less fouling on both ultrafiltration and microfiltration membranes than original alginate. Enzymatically treated alginate is predicted to cause less fouling on both membranes within the pH range of approximately 3.0 to approximately 10.0. Without the presence of calcium cation, alginate lyase reduced the foulant resistance by more than 82% for both membranes. In the presence of 1 mM calcium cation, alginate lyase reduced the foulant resistance by more than 55%. In addition, the foulant structure composed of enzymatically treated alginate was more readily removed by backwashing, suggesting reversible fouling. The advantages of using enzymatic technique to control membrane fouling include high efficiency and no damage to the membrane materials.

Claims

1. A method of reducing membrane fouling by organic substances in water treatment, the method comprising:

treating organic foulants by introducing alginate lyase to water containing alginate on a concentrate side of a membrane within a process line of a filtration system, wherein said introducing occurs at least 30 minutes prior to the water containing alginate and introduced alginate lyase contacting the filtration membrane.

2. The method of claim 1 wherein the alginate lyase is provided to water or wastewater in an amount effective to reduce membrane fouling.

3. The method of claim 2 wherein pH of the water containing alginate is within the range of approximately 3.0 to approximately 10.0 prior to said introducing.

4. The method of claim 2 wherein ionic strength of the water containing alginate is within the range of approximately 0.006 M to approximately 1.0 M prior to said introducing.

5. The method of claim 2 wherein the water containing alginate includes calcium cation, and wherein the concentration of calcium cation is within the range of approximately zero mM to approximately 10 mM.

6. The method of claim 1 wherein the alginate lyase is provided to water or wastewater in an amount effective to make fouling reversible with backwashing.

7. The method of claim 6 wherein the membrane is an ultrafiltration membrane.

8. The method of claim 7 where the ultrafiltration membrane has a pore size within the range of approximately 0.01 μ

m to approximately 0.1 μ

m pore size.

9. The method of claim 1 wherein the membrane is a ceramic membrane or a polymeric membrane.

10. The method of claim 1, comprising:

introducing alginate lyase into a backwashing solution used by the filtration system to backwash the membrane.

11. The method of claim 1 further comprising:

immobilizing the alginate lyase on the concentrate side of the membrane.

20. The method of claim 1, wherein said introducing alginate lyase occurs while the water containing alginate is being filtered.

21. The method of claim 1 wherein the membrane is selected from the group consisting of:

a microfiltration membrane, an ultrafiltration membrane, a nanofiltration membrane with a pore size within the range of approximately 0.0001 μ

m to approximately 0.01 μ

m, a reverse osmosis membrane, and a forward osmosis membrane.

22. The method of claim 1, wherein said introducing alginate lyase occurs on a feed side of a forward osmosis filtration process.

23. The method of claim 1, comprising

selecting the pore size of the membrane to be smaller than the molecular size of the alginate lyase;

and

retaining the alginate lyase on the concentrate side of the membrane, the molecular size of the alginate lyase being larger than the membrane pore size.

24. The method of claim 1, wherein said introducing occurs about 2 hours prior to the water with alginate and introduced alginate lyase contacting the filtration membrane.

12. A method of promoting reversible membrane fouling by alginate in water treatment, the method comprising:

filtering water containing alginate wherein a membrane is fouled by alginate during said filtering, and

treating organic foulants by

introducing alginate lyase to water containing alginate within a process line of a filtration system, wherein enzymatic reactions resulting from said introducing alginate lyase to water containing alginate begin at least 30 minutes prior to the water with introduced alginate lyase contacting the membrane or

introducing alginate lyase in the backwashing solution within a process line of a filtration system.

13. The method of claim 12 wherein the membrane is a microfiltration membrane with a pore size within the range of approximately 0.1 μ

m to approximately 1.0 μ

m.

14. The method of claim 12 wherein alginate concentration is within the range of approximately 1 mg L⁻

1 to approximately 1000 mg L<sup>−

1</sup> as measured by Chemical Oxygen Demand by Chromium (VI).

15. The method of claim 12 wherein alginate lyase concentration is any concentration up to approximately 20 mg L⁻

1.

16. The method of claim 12 wherein alginate lyase concentration is any concentration up to approximately 1 g L⁻

1.

17. The method of claim 12 wherein filtration is performed at ambient temperature and within the range of approximately zero kPa to approximately 20 MPa.

18. The method of claim 12 further comprising:

backwashing the membrane.

19. The method of claim 12, comprising decreasing the affinity and fouling potential of alginate to a membrane.

25. A method of reducing membrane fouling by alginate in water treatment, the method comprising:

introducing alginate lyase to water containing alginate within a process line of a filtration system, wherein enzymatic reactions resulting from said introducing alginate lyase to water containing alginate begin at least 30 minutes prior to the water containing alginate and introduced alginate lyase contacting a filtration membrane within said filtration system.