Methods and systems for producing high purity gaseous chlorine dioxide
Methods and systems for producing high purity gaseous chlorine dioxide are provided. A solid chlorite reactant is contacted with an ozone-containing reactant gas, or a gas containing both ozone and a component that reacts with any hydroxide byproduct (such as carbon dioxide), to produce chlorine dioxide. The reaction can be monitored and controlled to ensure that excess chlorite reactant is provided and to prevent ozone from passing into the product gas.
1. A method of producing gaseous chlorine dioxide, the method comprising:
contacting a dry chlorite reactant with an ozone-containing gas; and
reacting the ozone in the ozone-containing gas with the dry chlorite reactant at a gas-solid interface between the ozone-containing gas and the dry chlorite reactant to produce the gaseous chlorine dioxide.
2. The method of claim 1 , wherein the dry chlorite reactant is sodium chlorite.
3. The method of claim 1 , wherein the ozone-containing gas includes ozone in an amount ranging from 10 ppm to 100,000 ppm.
4. The method of claim 1 , wherein the gaseous chlorine dioxide is at least 95 wt. % pure, not including any carrier gas.
5. The method of claim 1 , further comprising generating the ozone-containing gas by feeding an oxygen-containing gas into an ozone generator.
6. The method of claim 1 , further comprising dissolving the gaseous chlorine dioxide in a liquid media.
7. The method of claim 1 , further comprising combining the gaseous chlorine dioxide with a receiving stream of an industrial process.
8. The method of claim 1 , wherein the dry chlorite reactant is provided in a solid reactant media that also includes an inert component.
9. The method of claim 8 , wherein the solid reactant media is provided as pellets having an average particle size in the range of from 1 mm to 10 mm.
10. A system for producing gaseous chlorine dioxide, the system comprising:
an ozone generator that is configured to produce an ozone-enriched gas; and
a reactor that: (i) is coupled to the ozone generator and is configured to receive the ozone-enriched gas from the ozone generator, (ii) includes a dry chlorite reactant that is arranged to contact the ozone-enriched gas and react with ozone in the ozone-enriched gas at a gas-solid interface between the ozone-enriched gas and the dry chlorite reactant to produce the gaseous chlorine dioxide, and (iii) is configured to exhaust a gas product that includes the gaseous chlorine dioxide.
11. The system according to claim 10 , further comprising a monitor for determining the amount of ozone present in the gas product.
12. The system according to claim 10 , further comprising a vessel that receives the gas product, and wherein the vessel contains a liquid media that dissolves the gaseous chlorine dioxide.
13. The system according to claim 12 , further comprising a probe that measures the conductivity of the liquid media.
14. The system according to claim 13 , further comprising a controller that triggers an alarm when the conductivity of the liquid media exceeds a predetermined threshold value.
15. The system according to claim 10 , wherein:
the reactor comprises a container selected from at least one of a packed bed, a column, and a drum; and
the dry chlorite reactant is provided in a solid reactant media that is located in the container, the solid reactant media having a form selected from the group consisting of block form, granular form, pellets, powdered form, or combinations thereof.
16. The system according to claim 10 , further comprising a monitor for determining the amount of chlorine dioxide gas in the gas product.
17. The system according to claim 12 , further comprising a monitor for determining the amount of chlorine dioxide gas in the liquid media that dissolves the gaseous chlorine dioxide.
18. The method according claim 1 , wherein the reaction between the ozone and the dry chlorite reactant also produces an ozonide byproduct.