Calcium removal method

Patent metadata

Field	Value
Publication number	US-9242875-B2
Application number	US-201113703879-A
Country	US
Kind code	B2
Filing date	May 11, 2011
Priority date	Jun 21, 2010
Publication date	Jan 26, 2016
Grant date	Jan 26, 2016

Abstract

In accordance with the present invention, there is provided a calcium removal method capable of reducing operation cost. A solution L 2 containing potassium or/and sodium, and calcium is passed through an ion-exchange resin 35 to separate the solution into a solution containing potassium or/and the sodium, and a solution containing calcium. Operation cost can remarkably be decreased since potassium carbonate is not required to remove calcium as before. Timing for changing a calcium-containing water L 3 and a salt water L 4 discharged from the ion-exchange resin can be performed based on at least one measurement result selected from the group consisting of: a calcium or chlorine concentration; electrical conductivity; and pH of a fluid which is discharged from said ion-exchange resin. The solution may be a filtrate L 1 that is obtained by washing a chlorine bypass dust D generated in a cement burning process, or a leachate W of a final disposal site 50.

First claim

The invention claimed is:

1. A method of removing calcium from a solution containing potassium or/and sodium, and calcium using water and an ion-exchange resin to separate said solution containing potassium or/and sodium, and calcium into a solution containing potassium or/and the sodium and a solution containing calcium, wherein the method comprises the steps of:
(a) providing an amphoteric ion-exchange resin filled up with said water;
(b) introducing the solution containing potassium or/and sodium, and calcium into the amphoteric ion-exchange resin;
(c) introducing said water for regenerating the amphoteric ion-exchange resin;
(d) discharging the solution containing potassium or/and sodium from the amphoteric ion-exchange resin;
(e) discharging the solution containing calcium from the amphoteric ion-exchange resin separate from the discharging in step (d) so as to separate the solution containing potassium or/and sodium from the solution containing calcium; and
(f) repeating steps (b) to (e).

2. The calcium removal method as claimed in claim 1 , wherein said solution containing potassium or/and sodium, and calcium is a filtrate obtained by washing chlorine bypass dust generated in a cement burning process.

3. The calcium removal method as claimed in claim 2 , further comprising a step of adjusting an amount of the filtrate supplied to the amphoteric ion-exchange resin and an amount of said water supplied to said amphoteric ion-exchange resin to equalize an amount of separated calcium-containing water to the amount of the supplied filtrate.

4. The calcium removal method as claimed in claim 3 , wherein at least one step selected from the group consisting of:
adjustment of the amount of the filtrate supplied to the amphoteric ion-exchange resin;
adjustment of the amount of said water supplied to the amphoteric ion-exchange resin; and
control of timing for separately collecting the solution containing sodium and/or potassium and the calcium-containing water from the amphoteric ion-exchange resin is performed based on at least one measurement result, and wherein said at least one measurement is selected from the group consisting of:
a calcium or chlorine concentration;
electrical conductivity; and
pH of a fluid which is discharged from the amphoteric ion-exchange resin.

5. The calcium removal method as claimed in claim 2 , further comprising a step of adjusting an amount of the filtrate supplied to the amphoteric ion-exchange resin and an amount of said water supplied to said amphoteric ion-exchange resin to increase an amount of separated calcium-containing water than the amount of the supplied filtrate.

6. The calcium removal method as claimed in claim 5 , wherein at least one step selected from the group consisting of:
adjustment of the amount of the filtrate supplied to the amphoteric ion-exchange resin;
adjustment of the amount of said water supplied to the amphoteric ion-exchange resin; and
control of timing for separately collecting the solution containing sodium and/or potassium and the calcium-containing water from the amphoteric ion-exchange resin is performed based on at least one measurement result, and wherein said at least one measurement is selected from the group consisting of:
a calcium or chlorine concentration;
electrical conductivity; and
pH of a fluid which is discharged from the amphoteric ion-exchange resin.

7. The calcium removal method as claimed in claim 1 , wherein said solution is a leachate of a final disposal site.

8. A method for providing calcium containing water comprising the steps of:
(a) obtaining a solution containing potassium or/and sodium, and calcium, wherein said solution is one of a filtrate obtained by washing chlorine bypass dust generated in a cement burning process and a leachate solution obtained from a final disposal site;
(b) supplying a regeneration water that consists essentially of pure water;
(c) providing an amphoteric ion-exchange resin;
(d) introducing the solution containing potassium or/and sodium, and calcium into the ion-exchange resin;
(e) introducing the regeneration water into the ion exchange resin to regenerate the ion-exchange resin;
(f) separately collecting a solution containing sodium and/or potassium and the calcium-containing water from the ion exchange resin during the step of introducing the regeneration water; and
(g) directing the calcium-containing water collected in step (f) to step (a) to wash chlorine bypass dust or to the final disposal site to produce the leachate solution.

9. The calcium removal method as claimed in claim 8 , wherein said solution containing potassium or/and sodium, and calcium is said filtrate obtained by washing chlorine bypass dust generated in a cement burning process.

10. The calcium removal method as claimed in claim 9 , further comprising a step of adjusting an amount of the filtrate supplied to the ion-exchange resin and an amount of a regeneration water supplied to said ion-exchange resin to equalize an amount of separated calcium-containing water to an amount of the supplied filtrate.

11. The calcium removal method as claimed in claim 10 , wherein at least one step selected from the group consisting of adjustment of an amount of a filtrate supplied to the ion-exchange resin, adjustment of an amount of the regeneration water supplied to the ion-exchange resin, and control of timing for separately collecting the solution containing sodium and/or potassium and the calcium-containing water from the ion-exchange resin is performed based on at least one measurement result, and wherein said at least one measurement is selected from the group consisting of a calcium or chlorine concentration, electrical conductivity, and pH of a fluid which is discharged from the ion-exchange resin.

12. The calcium removal method as claimed in claim 9 , further comprising a step of adjusting an amount of the filtrate supplied to the ion-exchange resin and an amount of the regeneration water supplied to said ion-exchange resin to increase an amount of collected calcium-containing water relative to an amount of the supplied filtrate.

13. The calcium removal method as claimed in claim 12 , wherein at least one step selected from the group consisting of adjustment of an amount of the filtrate supplied to the ion-exchange resin, adjustment of an amount of the regeneration water supplied to the ion-exchange resin, and control of timing for separately collecting the solution containing sodium and/or potassium and the calcium-containing water from the ion-exchange resin is performed based on at least one measurement result, and wherein said at least one measurement is selected from the group consisting of a calcium or chlorine concentration, electrical conductivity, and pH of a fluid which is discharged from the ion-exchange resin.

14. The calcium removal method as claimed in claim 8 , wherein said solution is said leachate of a final disposal site.

Assignees

• Tamura Noritoshi
• Suzuki Takayuki
• Otani Hirokazu
• Taiheiyo Cement Corp

Inventors

• Tamura Noritoshi
• Suzuki Takayuki
• Otani Hirokazu

Classifications

• C04B7/60

  Methods for eliminating alkali metals or compounds thereof {, e.g. from the raw materials or during the burning process; methods for eliminating other harmful components (avoiding environmental pollution C04B7/364)} · CPC title

• C02F2209/29

  Chlorine compounds · CPC title

• C02F2209/05

  Conductivity or salinity · CPC title

• B01J47/15

  for obtaining a solution having a fixed pH · CPC title

• C02F1/5245

  using basic salts, e.g. of aluminium and iron · CPC title