Demineralization of milk and milk-derived products by electrodeionization

• US 6,033,700 A
• Filed: 10/08/1997
• Issued: 03/07/2000
• Est. Priority Date: 10/09/1996
• Status: Expired due to Fees

• Current Assignee: Nestec SA (Nestle SA)
• Original Assignee: Nestec SA (Nestle SA)
• Inventors: Berrocal, Rafael, Chaveron, Michel
• Primary Examiner(s): Mosher, Mary E.
• Assistant Examiner(s): SALIMI, ALI REZA
• Application Number:
  US08/946,848
• Time in Patent Office: 881 Days
• Field of Search: 426/239, 426/491, 426/583, 426/801, 426/495, 210/677, 210/663, 210/669, 210/681, 204/182.5, 204/182.4, 204/301, 204/252-257, 204/263
• US Class Current: 426/239
• CPC Class Codes: A23C 9/144 by electrical means, e.g. electrodialysis
• CPC Class Codes: A23C 9/146 by ion-exchange
• CPC Class Codes: B01D 61/48 having one or more compartments filled with ion-exchange material , e.g. electrodeionisation

Abstract

A liquid milk product, including a milk and a whey, but other than sweet whey, is demineralized by an electrodeionization process by passing the product to be demineralized through a resin bed of strong cationic exchange resin contained in an electrodeionization dilution compartment or through a resin bed of weak anionic and of cationic, particularly strong cationic, exchange resins in the compartment, and in the process, the pH of the wash solution present in the electrodionization cation and anion concentration compartments is maintained so that the solution present in each concentration compartment has a pH value less than 5.

Claims

1. In an electrodeionization process for demineralizing a substrate wherein a substrate comprising cations and anions is passed through an ion exchange resin bed contained in a dilution compartment between a cation-permeable membrane and an anion-permeable membrane, wherein an electric conductivity field produced from electrodes contained in electrode compartments directs cations from the dilution compartment via the cation-permeable membrane to a cation concentration compartment and directs anions from the dilution compartment via the anion-permeable membrane to an anion concentration compartment, wherein a wash solution is passed into and through the cation and anion concentration compartments for removing cations and anions from the concentration compartments and wherein a product from which cations and anions have been removed is collected from the dilution compartment, the improvements comprising:

passing a liquid material of milk origin through a dilution compartment resin bed which comprises strong cationic exchange resin beads and maintaining a pH of the wash solution so that the solution present in the cation and anion concentration compartments has a pH value of less than 5 and wherein the liquid material is not sweet whey and is selected from the group consisting of an acid whey and of a permeate selected from the group consisting of a permeate from microfiltration or ultrafiltration of skimmed milk, from ultrafiltration of acid whey and from microfiltration of sweet whey.

2. A process according to claim 1 wherein the resin bed consists essentially of the strong cationic exchange resin.

5. A process according to claim 1 or 3 wherein the wash solution is passed through concentration compartments which do not contain an ion exchange resin.

6. A process according to claim 1 or 3 further comprising passing the wash solution through a resin bed which is present in each concentration compartment and which comprises cationic and weak anionic exchange resin beads.

7. A process according to claim 6 wherein the cationic resin beads are strong cationic resin beads.

8. A process according to claim 1 or 3 further comprising passing the wash solution through a resin bed which is present in each concentration compartment and which comprises a strong cationic exchange resin to maintain the pH of the solution present in each compartment so that the solution present has a pH value less than 5.

9. A process according to claim 1 or 3 wherein the wash solution is acidic to maintain the pH value.

10. A process according to claim 9 wherein the wash solution comprises hydrochloric acid.

12. A process according to claim 6 wherein the resin beds are arranged in an arrangement selected from the group consisting of a mixed bed and a layered bed.

14. A process according to claim 6 wherein, by weight proportion of strong cationic exchange resin beads to weak anionic exchange resin beads, the resin beads are in amounts of from 30%-40% cationic resin to 70%-60% anionic resin.

16. A process according to claim 6 wherein the strong cationic exchange resin beads are in an H⁺ form and the weak anionic exchange resin beads are in an OH^- form.

17. A process according to claim 1 or 3 wherein the electrical conductivity is maintained at at least 5 mS.

18. A process according to claim 1 or 3 further comprising treating the sweet whey passed to the resin bed so that the sweet whey passed to the resin bed has a pH of from 7.5 to 8.

3. In a electrodeionization process for demineralizing a substrate wherein a substrate comprising cations and anions is passed through an ion exchange resin bed contained in a dilution compartment between a cation-permeable membrane and an anion-permeable membrane, wherein an electric field produced from electrodes contained in electrode compartments directs cations from the dilution compartment via the cation-permeable membrane to a cation concentration compartment and directs anions from the dilution compartment via the anion-permeable membrane to an anion concentration compartment, wherein a wash solution is passed into and through the cation and anion concentration compartments for removing cations and anions from the concentration compartments and wherein a product from which cations and anions have been removed is collected from the dilution compartment, the improvements comprising:

passing a liquid material selected from the group consisting of a milk and of a material of milk origin through a dilution compartment resin bed which comprises cationic exchange resin beads and weak anionic exchange resin beads and maintaining a pH of the wash solution so that the solution present in the cation and anion concentration compartments has a pH value of less than 5 and wherein the liquid material of milk origin is not sweet whey and is selected from the group consisting of an acid whey and of a permeate selected from the group consisting of a permeate from microfiltration or ultrafiltration of skimmed milk, from ultrafiltration of acid whey and from microfiltration of sweet whey.

4. A process according to claim 3 wherein the cationic exchange resin beads are strong cationic exchange resin beads.

11. A process according to claim 3 wherein the resin beds are arranged in an arrangement selected from the group consisting of a mixed bed and a layered bed.

13. A process according to claim 4 wherein, by weight proportion of strong cationic exchange resin beads to weak anionic exchange resin beads, the resin beads are in amounts of from 30%-40% cationic resin to 70%-60% anionic resin.

15. A process according to claim 4 wherein the strong cationic exchange resin beads are in an H⁺ form and the weak anionic exchange resin beads are in an OH^- form.

19. A process according to claim 3 wherein the liquid material is a milk and the milk is a concentrated skimmed milk.