Water treatment process and water treatment system

Patent metadata

Field	Value
Publication number	US-9914653-B2
Application number	US-201514673114-A
Country	US
Kind code	B2
Filing date	Mar 30, 2015
Priority date	Jul 5, 2013
Publication date	Mar 13, 2018
Grant date	Mar 13, 2018

Abstract

In a water treatment system and a water treatment process, a scale inhibitor is supplied to water to be treated containing Ca ions, SO 4 ions, carbonate ions, and silica, and the water to be treated is adjusted to a pH at which silica is soluble. The pH-adjusted water containing the calcium scale inhibitor is separated in a first demineralizing section into concentrated and treated water. In a first crystallizing section, seed crystals of gypsum are supplied to the first concentrated water, whereby gypsum is crystallized and removed from the first concentrated water. Silica in the water to be treated is removed from the first concentrated water on the downstream side of the first crystallizing section. Calcium carbonate in the water to be treated is removed from the first concentrated water on the upstream side of the first demineralizing section or the downstream side of the first crystallizing section.

First claim

The invention claimed is:

1. A water treatment process comprising:
a first scale inhibitor supplying step of supplying a calcium scale inhibitor which is a scale inhibitor for inhibiting the deposition of a scale containing calcium to water containing Ca 2+ ions, SO 4 2− ions, carbonate ions and silica;
a first pH adjusting step of adjusting the water to a pH of 10 or more at which the silica is soluble in the water;
a first demineralizing step of separating the water into first concentrated water in which the Ca 2+ ions, the SO 4 2− ions, the carbonate ions and the silica are concentrated and treated water after the first scale inhibitor supplying step and the first pH adjusting step; and
a first crystallizing step of supplying seed crystals of gypsum to the first concentrated water so that gypsum is crystallized from the first concentrated water,
wherein the water treatment process further comprises, after the first crystallizing step:
a second scale inhibitor supplying step of supplying the calcium scale inhibitor and a silica scale inhibitor which is a scale inhibitor for inhibiting the deposition of the silica to the water;
a second demineralizing step of separating the water into second concentrated water in which the Ca 2+ ions, the SO 4 2− ions, the carbonate ions and the silica are concentrated and treated water after the second scale inhibitor supplying step; and
a second crystallizing step of supplying seed crystals of gypsum to the second concentrated water so that gypsum is crystallized from the second concentrated water.

2. The water treatment process according to claim 1 , comprising a second pH adjusting step of adjusting the second concentrated water to a pH 6.0 or less at which a scale inhibition function of the calcium scale inhibitor is reduced, thereby promoting the deposition of the gypsum in the second crystallizing step.

3. The water treatment process according to claim 1 , comprising, after the second crystallizing step, a downstream side demineralizing step of separating the second concentrated water into concentrated water and treated water, and recovering the separated treated water.

4. The water treatment process according to claim 2 , wherein, after the second crystallizing step, the second concentrated water after the adjustment of the pH in the second pH adjusting step is adjusted to a pH of 4.0 or more at which the calcium scale inhibitor exerts its function.

5. The water treatment process according to claim 1 , comprising a second pH adjusting step of adjusting the second concentrated water to a pH of 10 or more at which the silica is soluble in the second crystallizing step.

6. The water treatment process according to claim 1 , comprising a first upstream side precipitating step of precipitating at least calcium carbonate from the water so that the concentration of the calcium carbonate in the water is reduced, before the first scale inhibitor supplying step and the first pH adjusting step.

7. The water treatment process according to claim 6 , comprising a first deaerating step of removing CO 2 from the water before the first upstream side precipitating step or after the first upstream side precipitating step and before the first scale inhibitor supplying step and the first pH adjusting step.

8. The water treatment process according to claim 1 ,
wherein the water contains metal ions; and
wherein the process comprises a first precipitating step of precipitating at least one of calcium carbonate and a metal compound so that the concentration of at least one of the calcium carbonate and the metal ions is reduced from the first concentrated water, after the first crystallizing step.

9. The water treatment process according to claim 8 , wherein at least one of seed crystals of the silica and a precipitant for the silica is supplied to the first concentrated water in the first precipitating step.

10. The water treatment process according to claim 1 ,
wherein the water contains metal ions; and
wherein the process comprises a second precipitating step of precipitating at least one of calcium carbonate and a metal compound so that the concentration of at least one of the calcium carbonate and the metal ions is reduced from the second concentrated water, after the second crystallizing step.

11. The water treatment process according to claim 10 , wherein at least one of seed crystals of the silica and a precipitant for the silica is supplied to the second concentrated water in the second precipitating step.

12. The water treatment process according to claim 11 , wherein, when the water contains Mg 2+ ions, the amount of the precipitant for the silica to be supplied is adjusted according to the concentration of the Mg 2+ ions.

13. The water treatment process according to claim 9 , wherein, when the water contains Mg 2+ ions, the amount of the precipitant for the silica to be supplied is adjusted according to the concentration of the Mg 2+ ions.

14. The water treatment process according to claim 8 ,
wherein, when the water contains Mg 2+ ions, the first concentrated water in the first precipitating step is adjusted to a pH of 10 or more at which a magnesium compound is deposited so that the concentration of the Mg 2+ ions is reduced, and
wherein, after the first precipitating step, the first concentrated water is adjusted to a pH of less than 10 at which the magnesium compound is soluble.

15. The water treatment process according to claim 10 ,
wherein, when the water contains Mg 2+ ions, the second concentrated water in the second precipitating step is adjusted to a pH of 10 or more at which a magnesium compound is deposited so that the concentration of the Mg 2+ ions is reduced, and
wherein, after the second precipitating step, the second concentrated water is adjusted to a pH of less than 10 at which the magnesium compound is soluble.

16. The water treatment process according to claim 6 ,
wherein, when the water contains Mg 2+ ions, the water in the first upstream side precipitating step is adjusted to a pH of 10 or more at which a magnesium compound is deposited so that the concentration of the Mg 2+ ions is reduced, and
wherein, after the first upstream side precipitating step, the water is adjusted to a pH of less than 10 at which the magnesium compound is soluble.

17. The water treatment process according to claim 3 , wherein moisture is evaporated from the concentrated water in the downstream side demineralizing step, so that a solid in the concentrated water is recovered.

18. A water treatment system comprising:
a first scale inhibitor supplying section that supplies a calcium scale inhibitor which is a scale inhibitor for inhibiting the deposition of a scale containing calcium to water containing Ca 2+ ions, SO 4 2− ions, carbonate ions and silica;
a first pH adjusting section that supplies a pH adjuster to the water to adjust the pH of the water to be treated to 10 or more such that the silica is soluble in the water;
a first demineralizing section that is installed on a downstream side of the first scale inhibitor supplying section and the first pH adjusting section and separates the water into first concentrated water in which the Ca 2+ ions, the SO 4 2− ions, the carbonate ions and the silica are concentrated and treated water; and
a first crystallizing section including a first crystallizing tank that is installed on a downstream side of the first demineralizing section and crystallizes gypsum from the first concentrated water and a first seed crystal supplying section th

Assignees

• Mitsubishi Heavy Ind Ltd

Inventors

• Eda Masayuki
• Okino Susumu
• Yoshiyama Ryuji
• Sakurai Hideaki
• Ukai Nobuyuki
• Suzuki Hideo
• Nakashoji Hiroshi
• Yoshioka Shigeru

Classifications

• C02F2209/06

  pH · CPC title

• B01D65/08

  Prevention of membrane fouling or of concentration polarisation · CPC title

• C02F1/42

  by ion-exchange (ion-exchange in general B01J) · CPC title

• B01D61/025

  Reverse osmosis; Hyperfiltration · CPC title

• B01D61/04

  Feed pretreatment · CPC title