Chlorine dioxide generation method
A method generating chlorine dioxide is provided. The method uses sodium chlorite solution and diluted sulfuric acid to generate chlorine dioxide with a significantly higher rate of conversion of chlorite to chorine dioxide than has been previously reported with sulfuric acid/chlorite chlorine dioxide generation.
1. A two chemical conversion method for preparing chlorine dioxide, comprising:
reacting a 7.5-25 weight % aqueous sodium chlorite solution with a 20-50 weight % aqueous sulfuric acid as sole constituents in a reaction chamber sized to allow the aqueous sodium chlorite solution and the aqueous sulfuric acid to react for about 5 seconds to about 300 seconds to form a reaction mixture comprising chlorine dioxide in which 75% or more and 85% or less of chlorite ion in the sodium chlorite solution is converted to chlorine dioxide.
2. The method of claim 1 , further comprising:
diluting a concentrated sulfuric acid with water to 20% to 50% by weight and cooling the diluted aqueous sulfuric acid to remove heat of reaction and using the cooled 20 to 50% by weight aqueous sulfuric acid in the reacting step.
3. The method of claim 1 , wherein the aqueous sodium chlorite solution and the aqueous sulfuric acid are contacted for about 30 seconds to about 60 seconds.
4. The method of claim 1 , wherein a prolonged time of storage of the reaction mixture prior to diluting the reaction mixture with water does not result in a significant loss of the produced chlorine dioxide by reaction with water to form chlorate.
5. A method for generating chlorine dioxide, comprising:
introducing an aqueous sodium chlorite solution and an aqueous sulfuric acid separately into a reactor as sole constituents, and
reacting the aqueous sodium chlorite with the aqueous sulfuric acid to form a reaction mixture by converting 75% or more and 85% or less of chlorite ions to chlorine dioxide,
wherein the aqueous sodium chlorite solution has a concentration in the range of 7.5-25% by weight, and the aqueous sulfuric acid has a concentration in the range of 20-50% by weight.
6. The method of claim 5 , further comprising storing the reaction mixture in the reactor for about 1 to 15 minutes without a significant conversion of the chlorine dioxide to chlorate.
7. The method of claim 5 , wherein the reaction mixture is substantially chlorine and chlorite free.
8. The method of claim 5 , wherein the reactor has a discharge opening which communicates with a treatment stream, and the reaction mixture is not diluted until the reaction is complete.
9. The method of claim 5 , further comprising:
diluting a concentrated sulfuric acid to 20% to 50% by weight with water and cooling the diluted aqueous sulfuric acid to remove heat of reaction and using the cooled 20 to 50% by weight aqueous sulfuric acid in the reacting step.
10. The method of claim 1 , further comprising discharging the reaction mixture from the reactor via a discharge opening of the reactor to a treatment stream.
11. The method of claim 2 , wherein the concentrated sulfuric acid is diluted with water to approximately 50% by weight and cooled.
12. The method of claim 1 , wherein the aqueous sulfuric acid has a concentration of approximately 50% by weight.
13. The method of claim 1 , wherein the percent conversion of chlorite ion to chlorine dioxide is determined by four step iodometric titration.
14. A method for preparing chlorine dioxide, comprising:
reacting a 7.5-25 weight % aqueous sodium chlorite solution with a 20-50 weight % aqueous sulfuric acid solution as sole constituents in a reactor for 5 to 300 seconds to obtain a reaction mixture in which 81.5% or more and 85% or less of chlorite ion in the aqueous sodium chlorite solution is converted to chlorine dioxide.
15. The method of 14 , further comprising:
diluting a concentrated sulfuric acid to approximately 50% by weight aqueous sulfuric acid solution and cooling the aqueous sulfuric acid solution and using the resulting cooled, diluted sulfuric acid in the reacting step.
16. The method of 14 , further comprising storing the reaction mixture in the reactor for about 1 to 15 minutes without a significant conversion of the chlorine dioxide to chlorate.
17. The method of 14 , further comprising discharging the reaction mixture to a treatment stream via a discharge opening of the reactor.
18. The method of claim 14 , wherein at least 84% of the chlorite ion is converted to the chlorine dioxide in the reaction mixture.
19. The method of claim 15 , further comprising discharging the reaction mixture from the reactor via a discharge opening of the reactor to a treatment stream.