Installation for the preparation of a solution of calcium hydrogen carbonate suitable for the remineralization of water
US-2016130163-A1 · May 12, 2016 · US
US11130689B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11130689-B2 |
| Application number | US-201716068599-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 3, 2017 |
| Priority date | Feb 5, 2016 |
| Publication date | Sep 28, 2021 |
| Grant date | Sep 28, 2021 |
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The present invention relates to a process for the preparation of an aqueous solution comprising at least one earth alkali hydrogen carbonate, a process for the mineralization and/or stabilization of water as well as the use of the aqueous solution comprising at least one earth alkali hydrogen carbonate obtained by the process for the mineralization and/or stabilization of water.
Opening claim text (preview).
The invention claimed is: 1. A process for the preparation of an aqueous solution comprising at least one earth alkali hydrogen carbonate, comprising the steps of: a) providing water; b) providing at least one earth alkali carbonate-comprising material; c) providing CO 2 or an acid having a pK a -value <5; d) combining the water of step a) with the at least one earth alkali carbonate-comprising material of step b) and the CO 2 or acid of step c) in any order such as to obtain an aqueous suspension S 1 comprising at least one earth alkali hydrogen carbonate; e) filtering at least a part of the aqueous suspension S 1 obtained in step d) by passing the aqueous suspension S 1 through at least one submerged membrane module in order to obtain an aqueous solution S 2 comprising at least one earth alkali hydrogen carbonate, wherein the at least one submerged membrane module is located in a container; and wherein process steps d) and e) are carried out in the same container and air or process fluid is recirculated across at least a part of the surface of the at least one submerged membrane module. 2. The process according to claim 1 , wherein step d) comprises the steps of i1) combining the water of step a) with the CO 2 or acid of step c), and i2) combining the mixture of i1) with the at least one earth alkali carbonate-comprising material of step b); or ii1) combining the water of step a) with the at least one earth alkali carbonate-comprising material of step b), and ii2) combining the mixture of ii1) with the CO 2 or acid of step c). 3. The process according to claim 1 , wherein process steps d) and e) are carried out in a reactor tank. 4. The process according to claim 1 , wherein the at least one submerged membrane module has a pore size of <1 μm. 5. The process according to claim 1 , wherein air or process fluid is recirculated from the bottom to top direction of the at least one submerged membrane module and/or container. 6. The process according to claim 1 , wherein the container is sealed and air at the top of the container is used as the feed and reintroduced at the bottom of the container. 7. The process according to claim 1 , wherein the process comprises a further step f) of backwashing the at least one submerged membrane module with water, optionally CO 2 or an acid having a pK a -value <5 is added to the water. 8. The process according to claim 1 , wherein the at least one earth alkali carbonate-comprising material of step b) is selected from the group consisting of precipitated calcium carbonate, modified calcium carbonate, ground calcium carbonate and mixtures thereof. 9. The process according to claim 1 , wherein the at least one earth alkali carbonate-comprising material of step b) is ground calcium carbonate being selected from the group consisting of marble, limestone, chalk and mixtures thereof. 10. The process according to claim 1 , wherein the at least one earth alkali carbonate-comprising material of step b) is provided in dry form or in form of an aqueous suspension; and/or the at least one earth alkali hydrogen carbonate obtained in step d) comprises calcium hydrogen carbonate. 11. The process according to claim 1 , wherein the acid provided in step c) has a pK a -value <4 and/or the acid is selected from the group consisting of sulfuric acid, hydrochloric acid, nitric acid or citric acid and/or mixtures thereof. 12. The process according to claim 1 , wherein the aqueous solution S 2 comprising at least one earth alkali hydrogen carbonate obtained in step e) has an earth alkali concentration as earth alkali hydrogen carbonate in the range from 20 to 1 000 mg/l; and/or has a pH-value in the range from 6.1 to 8.9. 13. A process for the mineralization and/or stabilization of water, the process comprises the steps of (i) providing water to be mineralised, (ii) providing an aqueous solution comprising at least one earth alkali hydrogen carbonate obtained by the process as defined in claim 1 , (iii) combining the water to be mineralised of step (i) and the aqueous solution comprising at least one earth alkali hydrogen carbonate of step (ii) in order to obtain mineralised water. 14. The process according to claim 13 , comprising a further step (iv) of adding a base to the mineralised water of step (iii). 15. Use of an aqueous solution comprising at least one earth alkali hydrogen carbonate obtained by the process according to claim 1 for the mineralization and/or stabilization of water or as mineralized water. 16. The use according to claim 15 , wherein the water is desalinated or naturally soft water. 17. The process of claim 4 , wherein the pore size is <0.1 μm. 18. The process of claim 5 , wherein CO 2 or acid of step c) is added to the air or process fluid. 19. The process of claim 8 , wherein the at least one earth alkali carbonate comprising material in step b) is ground calcium carbonate. 20. The process of claim 10 , wherein the at least one earth alkali hydrogen carbonate obtained in step d) consists of calcium hydrogen carbonate.
Regeneration of sorbents, filters · CPC title
CO2 · CPC title
Seawater, e.g. for desalination · CPC title
by addition of specified substances, e.g. trace elements, for ameliorating potable water (medicinal water A61K) · CPC title
by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) · CPC title
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