IP Library Granted Patent US 8,038,884
Granted Patent B2
US 8,038,884 · App. 11/884,564 · Granted Oct 18, 2011

Process to prepare chlorine-containing compounds

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Quick Facts
Patent No.
US 8,038,884
App. No.
11/884,564
Granted
Oct 18, 2011
Kind
B2
Abstract

The present invention relates to process to prepare a chlorine-containing compound using an aqueous salt solution containing at least 100 g/l of sodium chloride and a contaminating amount of polyvalent cations comprising the steps of (i) preparing an aqueous salt solution containing at least 100 g/l of sodium chloride and at least 0.01 ppm of polyvalent cations by dissolving a sodium chloride source in water, (ii) adding an effective amount of at least one positive retention enhancing component to the aqueous solution, (iii) subsequently subjecting the solution to a nanofiltration step, thereby separating the solution into a retentate which is enriched for polyvalent cations and a permeate which is the purified aqueous salt solution, (iv) reacting the chloride anions in the permeate to a chlorine-containing compound by an electrolysis step, and (v) recycling at least part of the retentate to dissolution step (i).

Claims (25)

1. A process to prepare chlorine or sodium chlorate using an aqueous salt solution containing at least 100 g/l of sodium chloride and a contaminating amount of polyvalent cations comprising the steps of

(i) preparing an aqueous salt solution containing at least 100 g/l of sodium chloride and at least 0.01 ppm of polyvalent cations by dissolving a sodium chloride source containing more than 25% by weight sodium chloride in water,

(ii) adding an effective amount of at least one positive retention enhancing component to the aqueous solution,

(iii) subsequently subjecting the solution to a nanofiltration step—using a nanofiltration membrane having a molecular weight cut-off of between 100 Da and 10,000 Dalton, thereby separating the solution into a retentate which is enriched for polyvalent cations and a permeate which is the purified aqueous salt solution,

(iv) reacting the chloride anions in the permeate to chlorine or sodium chlorate by an electrolysis step, and

(v) recycling at least part of the retentate to dissolution step (i).

2. The process according to claim 1 further comprising adjusting the concentration of sodium chloride to be at least 100 g/l in a step subsequent to or simultaneous with step (ii) of adding the positive retention enhancing component to the aqueous solution and before nanofiltration step (iii).

3. The process according to claim 1 wherein the aqueous solution comprises at least 300 g/l of sodium chloride.

4. The process according to claim 1 wherein the at least one positive retention enhancing component is selected from the group consisting of polycarboxylic acids; polyacrylates; polymaleic acids; oligopeptides; polypeptides; polymers bearing two or more ester groups or carboxyalkyl groups; sugars; ferrocyanide salts; quaternary ammonium salts; cyclodextrines; urea; polymers bearing amino groups; polymers bearing one or more alcohol groups; polymers bearing quaternary ammonium groups; polymers comprising nitrogen-containing aliphatic rings; sodium salts of polymers bearing anionic groups; chloride salts of polymers bearing cationic groups; surfactants from a natural source; lactic acid; phospholipids; a suspension of yeast cells; a suspension of algae; maleic anhydride homopolymer; amylase; protease; sodium citrate; citric acid; nonanoyloxybenzene sulphonate; polyepoxysuccinic acid; polyacrylamide; sodium ethylenediamine tetraacetate; ethylenediamine tetramethylene phosphonic acid; sulphonated polyoxyethylene ethers; fatty acids; orange juice; apple juice; and Fe(II) or Fe(III) iron complexes with one of the above-mentioned compounds.

5. The process according to claim 4 wherein the polymers bearing two or more ester groups or carboxyalkyl groups also bear a member of the group consisting of phosphate groups, phosphonate groups, phosphino groups, sulphate groups, sulphonate groups and combinations thereof; the sugars are selected from the group consisting of functionalized monosaccharides, unfunctionalized monosaccharides, functionalized disaccharides, unfunctionalized disaccharides, functionalized polysaccharides and unfunctionalized polysaccharides; and the natural source is disproportionated rosin acid soap.

6. The process according to claim 1 wherein the positive retention enhancing component is selected from the group consisting of (poly)carboxylic acids, phosphinocarboxylic acids, polyacrylic acids, polymaleic acids, glucose, sucrose, saccharose, and sodium gluconate.

7. The process according to claim 1 wherein the at least one positive retention enhancing component is added in an amount of at least 15 ppm.

8. The process according to claim 1 wherein the at least one positive retention enhancing component is added in an amount of less than 5,000 ppm.

9. The process according to claim 1 wherein the polyvalent ions comprise calcium, magnesium, strontium, iron, barium, and/or aluminium.

10. The process according to claim 9 wherein either calcium or magnesium is present in the aqueous solution in an amount of less than 2,000 ppm.

11. The process according to claim 9 wherein either calcium or magnesium is present in the aqueous solution in an amount of less than 1,400 ppm.

12. The process according to claim 1 wherein sulphate anions are present in the aqueous salt solution in an amount of less than 75,000 ppm.

13. The process according to claim 1 wherein the sodium chloride source is a natural salt source containing more than 75% by weight of NaCl.

14. The process according to claim 1 wherein the aqueous solution is a saturated sodium chloride solution.

15. The process according to claim 1 wherein the at least one positive retention enhancing component is added in an amount of at least 50 ppm.

16. The process according to claim 15 wherein the at least one positive retention enhancing component is added in an amount of less than 350 ppm.

17. The process according to claim 1 wherein the at least one positive retention enhancing component is added in an amount of less than 350 ppm.

18. The process according to claim 1 wherein sulphate anions are present in the aqueous salt solution in an amount of less than 8,000 ppm.

19. The process according to claim 1 wherein the sodium chloride source is a natural salt source containing more than 90% by weight of NaCl.

20. The process according to claim 1 wherein the polyvalent cations are calcium.

Assignments (4)
CHANGE OF NAME Recorded Sep 18, 2019
From: AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
To: NOURYON CHEMICALS INTERNATIONAL B.V.
Reel/Frame 050426/0671 →
SECURITY INTEREST Recorded Oct 1, 2018
From: STARFRUIT US MERGER SUB 1 LLC; STARFRUIT US MERGER SUB 2 LLC; AKZO NOBEL SURFACE CHEMISTRY LLC; AKZO NOBEL CHEMICALS B.V.; AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
To: WILMINGTON TRUST (LONDON) LIMITED, AS COLLATERAL AGENT
Reel/Frame 047231/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 13, 2017
From: AKZO NOBEL N.V.
To: AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
Reel/Frame 044427/0759 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 8, 2007
From: BARGEMAN, GERRALD; DEMMER, RENE LODEWIJK MARIA; TEN KATE, ANTOON; KUZMANOVIC, BORIS; VAN LARE, CORNELIS ELIZABETH JOHANNUS; MAYER, MATEO JOZEF JACQUES; SCHUTYSER, MAARTEN ANDRE IRENE; WESTERINK, JAN BAREND
To: AKZO NOBEL N. V.
Reel/Frame 020217/0478 →