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Gas or Liquid Waste - High Levels of SOx or Cl2/HCl


Wastes are supplied to a disposal process in the form of either gas, liquid or solid, or a combination thereof. Configuration 2.1 illustrates a process to dispose of either a gas or liquid waste which produces flue gas containing excessive amounts of SOx or Cl2/HCl.

Configuration 2.1 a thermal oxidizer, quench section, two adiabatic absorbers and vent stack

Contact John Zink today to discuss your incineration needs.

The quench section cools the flue gas to its saturation temperature by directly contacting it with water; the adiabatic absorbers remove inorganic acids and chlorine. Water is used in the first absorber to remove a majority of the HCl from the flue gas. The residual HCl and virtually all the entering Cl2 leaves the absorber with the flue gas. A second absorber with caustic is used when either the Cl2 or HCl in the flue gas exiting the first absorber exceeds allowable levels. This occurs when excessive Cl2 is formed in the thermal oxidizer or when the first absorber is used to make acid.

 


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John Zink Company, LLC
11920 East Apache
Tulsa, OK 74116
United States of America
+1-918-234-1800

email: info@johnzink.com