Micronized CaCO3 slurry injection system for the remineralization of desalinated and fresh water

Patent metadata

Field	Value
Publication number	US-10046992-B2
Application number	US-201113812256-A
Country	US
Kind code	B2
Filing date	Aug 10, 2011
Priority date	Aug 13, 2010
Publication date	Aug 14, 2018
Grant date	Aug 14, 2018

Abstract

The present invention concerns a process for treating water and the use of calcium carbonate in such a process. In particular, the present invention is directed to a process for remineralization of water comprising the steps of providing feed water, and injecting gaseous carbon dioxide and a slurry into the feed water, wherein the slurry comprises micronized calcium carbonate.

First claim

The invention claimed is:

1. A process for remineralization of water comprising the steps of:
a) providing feed water in need of remineralization,
b) preparing a slurry comprising 0.05 to 40 wt.-% of micronized calcium carbonate based on the total weight of the slurry by mixing water and micronized calcium carbonate, wherein the micronized calcium carbonate has a particle size of 0.5 μm to 100 μm, the micronized calcium carbonate has a HCl insoluble content from 0.05 to 1.5 wt.-% based on the total weight of the micronized calcium carbonate, and the micronized calcium carbonate is ground calcium carbonate obtained from limestone, marble and/or chalk, calcium carbonate treated with a surface treatment agent, precipitated calcium carbonate, or any mixture thereof, and
c) injecting gaseous carbon dioxide and the slurry comprising micronized calcium carbonate into the feed water at controlled flow rates until the feed water has one or more of a desired alkalinity, conductivity, calcium concentration, pH, total dissolved solids and turbidity, and remineralized water is obtained.

2. The process of claim 1 , wherein the concentration of calcium carbonate in the slurry is from 1 to 25 wt.-%, based on the total weight of the slurry.

3. The process of claim 1 , wherein the concentration of calcium carbonate in the slurry is from 2 to 20 wt.-%, based on the total weight of the slurry.

4. The process of claim 1 , wherein the concentration of calcium carbonate in the slurry is from 3 to 15 wt.-%, based on the total weight of the slurry.

5. The process of claim 1 , wherein the calcium carbonate has a particle size from 0.5 to 50 nm.

6. The process of claim 1 , wherein the calcium carbonate has a particle size from 1 to 15 nm.

7. The process of claim 1 , wherein the calcium carbonate has a particle size from 2 to 10 nm.

8. The process of claim 1 , wherein the calcium carbonate has a particle size from 3 to 5 nm.

9. The process of claim 1 , wherein the micronized calcium carbonate has a HCl insoluble content from 0.1 to 0.6 wt.-%, based on the total weight of the micronized calcium carbonate.

10. The process of claim 1 , wherein the micronized calcium carbonate is a ground calcium carbonate obtained from limestone, marble and/or chalk.

11. The process of claim 1 , wherein the slurry further comprises magnesium, potassium, sodium, magnesium carbonate, calcium magnesium carbonate, dolomitic limestone, calcareous dolomite, dolomite, half-burnt dolomite, magnesium oxide, burnt dolomite, magnesium sulfate, potassium hydrogen carbonate, or sodium hydrogen carbonate.

12. The process of claim 1 , wherein the slurry is freshly prepared by mixing water and the calcium carbonate.

13. The process of claim 12 , wherein the time period between the preparation of the slurry and the injection of the slurry is less than 24 hours.

14. The process of claim 12 , wherein the time period between the preparation of the slurry and the injection of the slurry is less than 2 hours.

15. The process of claim 1 , wherein the obtained remineralized water has a calcium concentration as calcium carbonate from 15 to 200 mg/l.

16. The process of claim 1 , wherein the obtained remineralized water has a calcium concentration as calcium carbonate from 50 to 150 mg/l.

17. The process of claim 1 , wherein the obtained remineralized water has a calcium concentration as calcium carbonate from 100 to 125 mg/l.

18. The process of claim 1 , wherein the obtained remineralized water has a calcium concentration as calcium carbonate from 15 to 100 mg/l.

19. The process of claim 1 , wherein the obtained remineralized water has a calcium concentration as calcium carbonate from 20 to 80 mg/l.

20. The process of claim 1 , wherein the obtained remineralized water has a calcium concentration as calcium carbonate from 40 to 60 mg/l.

21. The process of claim 1 , wherein the slurry comprises further minerals containing magnesium and the obtained remineralized water has a magnesium concentration from 5 to 25 mg/l.

22. The process of claim 1 , wherein the remineralized water has a turbidity value of lower than 5.0 NTU.

23. The process of claim 1 , wherein the remineralized water has a turbidity value of lower than 1.0 NTU.

24. The process of claim 1 , wherein the remineralized water has a turbidity value of lower than 0.5 NTU.

25. The process of claim 1 , wherein the remineralized water has a turbidity value of lower than 0.3 NTU.

26. The process of claim 1 , wherein the remineralized water has one or more of a Langlier Saturation Index from −1 to 2, a Slit Density Index SDI 15 below 5, and a Membrane Fouling Index MFI 0.45 below 4.

27. The process of claim 1 , wherein the remineralized water has one or more of a Langlier Saturation Index from −0.5 to 0.5, a Slit Density Index SDI 15 below 4, and a Membrane Fouling Index MFI 0.45 below 2.5.

28. The process of claim 1 , wherein the remineralized water has one or more of a Langlier Saturation Index from −0.2 to 0.2, a Slit Density Index SDI 15 below 3, and a Membrane Fouling Index MFI 0.45 below 2.

29. The process of claim 1 , wherein the feed water is desalinated seawater, brackish water, brine, treated wastewater, natural water, ground water, surface water or rainfall.

30. The process of claim 1 , wherein the carbon dioxide is injected in a first step, and the slurry is injected subsequently in a second step, or wherein the slurry is injected in a first step and the carbon dioxide is injected subsequently in a second step, or wherein the carbon dioxide and the slurry are injected simultaneously.

31. The process of claim 1 , wherein carbon dioxide is injected in the water used for the slurry preparation.

32. The process according to claim 1 , wherein the remineralized water is blended with feed water.

33. The process according to claim 1 , wherein the process further comprises a particle removal step.

34. The process of claim 1 , wherein one or more of a alkalinity, conductivity, calcium concentration, pH, total dissolved solids and turbidity is measured and compared to a predetermined parameter value, and the amount of injected carbon dioxide and/or slurry is adjusted based on the difference between the measured and the predetermined parameter value.

35. The process of claim 34 , wherein the predetermined parameter value is a pH value, wherein the pH value is from 5.5 to 9.

36. The process of claim 34 , wherein the predetermined parameter value is a pH value, wherein the pH value is from 7 to 8.5.

Assignees

• Skovby Michael
• Poffet Martine
• Buri Matthias
• Blum Rene Vinzenz
• Omya Int Ag

Inventors

• Skovby Michael
• Poffet Martine
• Buri Matthias
• Blum René Vinzenz

Classifications

• C02F1/68 Primary

  by addition of specified substances, e.g. trace elements, for ameliorating potable water (medicinal water A61K) · CPC title

• C02F2209/003

  Downstream control, i.e. outlet monitoring, e.g. to check the treating agents, such as halogens or ozone, leaving the process · CPC title

• C02F2303/24

  Separation of coarse particles, e.g. by using sieves or screens · CPC title