Process for the production of chlorine dioxide
View Patent ↗Process for the continuous production of chlorine dioxide comprising generating chlorine dioxide in an aqueous reaction medium in a reaction vessel ( 1 ) maintained at sub-atmospheric pressure, bringing gaseous chlorine dioxide from said reaction vessel to an absorption tower ( 7 ) and contacting it therein with a flow of water to form an aqueous solution containing chlorine dioxide, bringing said aqueous solution containing chlorine dioxide to a stripper ( 12 ), blowing a gas through said aqueous solution of chlorine dioxide in the stripper to strip off from 10 to 100% of the chlorine dioxide entering the stripper and form a gaseous chlorine dioxide product.
1. A process for the continuous production of chlorine dioxide comprising
generating chlorine dioxide in an acidic aqueous reaction medium in a reaction vessel maintained at sub-atmospheric pressure,
bringing gaseous chlorine dioxide from said reaction vessel to an absorption tower and contacting it therein with a flow of water to form an aqueous solution containing chlorine dioxide,
bringing said aqueous solution containing chlorine dioxide from the absorption tower to a stripper, and increasing the pH of the aqueous solution containing chlorine dioxide leaving the absorption tower to is from about 6.5 to about 7.8,
blowing a gas through said aqueous solution of chlorine dioxide in the stripper to strip off from 10 to 100% of the chlorine dioxide entering the stripper and form a gaseous chlorine dioxide product obtained from the stripper with a partial pressure of from 0.5 to 20 kPa.
2. The process as claimed in claim 1 , wherein the chlorine dioxide is generated by reducing chlorate ions by means of a chemical reducing agent.
3. The process as claimed in claim 2 , wherein said chemical reducing agent is at least one of methanol or hydrogen peroxide.
4. The process as claimed in claim 1 , wherein from 40 to 95% of the chlorine dioxide entering the stripper is stripped off.
5. The process as claimed in claim 1 , wherein from 85 to 95% of the chlorine dioxide entering the stripper is stripped off.
6. The process as claimed in claim 1 , wherein said reaction medium is maintained at an absolute pressure from about 8 to about 80 kPa.
7. The process as claimed in claim 1 , wherein said reaction medium is maintained at its boiling point at the prevailing pressure.
8. The process as claimed in claim 1 , wherein the temperature of the aqueous solution containing chlorine dioxide is from about 0 to about 35° C.
9. The process as claimed in claim 1 , wherein a total yield of chlorine dioxide leaving the stripper is about 96% or more with respect to added chlorate ions.
10. The process as claimed in claim 1 , wherein said gaseous chlorine dioxide product is maintained at an total absolute pressure from about 10 kPa to about 2 MPa.
11. The process as claimed in claim 1 , wherein said gaseous chlorine dioxide product is maintained at a total absolute pressure from about 105 kPa to about 1 MPa.
12. The process as claimed in claim 1 , wherein the aqueous solution from the stripper containing remaining chlorine dioxide is at least partly recirculated to said absorption tower, or to said reaction vessel.
13. The process as claimed in claim 1 , wherein the gas blown through the aqueous solution of chlorine dioxide in the stripper is an inert gas.
14. The process as claimed in claim 13 , wherein said inert gas is air.
15. The process as claimed in claim 3 , wherein the chemical reducing agent is hydrogen peroxide which is fed to the aqueous reaction medium in an amount from about 0.5 to about 2 moles per mole of fed alkali metal chlorate.
16. The process as claimed in claim 3 , wherein the chemical reducing agent is methanol which is fed to the aqueous reaction medium in an amount from about 0.2 to about 1 moles per mole of fed alkali metal chlorate.
17. The process as claimed in claim 1 , wherein the aqueous solution in the absorption tower is acidified.
18. A process for the continuous production of chlorine dioxide comprising
generating chlorine dioxide in an acidic aqueous reaction medium in a reaction vessel maintained at sub-atmospheric pressure,
bringing gaseous chlorine dioxide from said reaction vessel to an absorption tower and contacting it therein with a flow of water to form an aqueous solution containing chlorine dioxide,
bringing said aqueous solution containing chlorine dioxide from the absorption tower to a stripper, and increasing the pH of the aqueous solution containing chlorine dioxide leaving the absorption tower to is from about 6.5 to about 7.8,
blowing a gas through said aqueous solution of chlorine dioxide in the stripper to strip off from 10 to 100% of the chlorine dioxide entering the stripper and form a gaseous chlorine dioxide product obtained from the stripper with a partial pressure of from 0.5 to 20 kPa, wherein the gaseous chlorine dioxide product has a content of elemental chlorine less than 1 wt %.