Oxidation system and method for cleaning waste combustion flue gas
View Patent ↗Methods and systems for the removal of SO2 from waste combustion flue gas are described herein. One such system for removing SO 2 from waste combustion flue gas containing SO 2 uses a semi-dry desulfurization system for contacting the flue gas with a solvent moistened absorption material. Thereafter, a recirculated water quench is used for contacting the flue gas with recirculated water at a relatively low pH, followed by a condenser used for contacting the flue gas with a water spray. Additionally, a NaOH supply for supplying NaOH to the condenser and an oxidizing catalyst supply for supplying an oxidizing catalyst to the condenser, are likewise used to produce cleaned flue gas for release to the atmosphere.
1. A method for removing SO 2 from waste combustion flue gas containing SO 2 comprising:
flowing the flue gas through a desulfurization system for contact with a solvent moistened absorption material;
flowing the flue gas through a recirculated water quench for contact with recirculated water at a relatively low pH; and
flowing the flue gas through a condenser for contact with a water spray, NaOH and an oxidizing catalyst to produce cleaned flue gas for release to the atmosphere.
2. A method for removing SO 2 from waste combustion flue gas containing SO 2 comprising:
flowing the flue gas through a combination wet desulfurization system and quench for contact with an absorption material slurry and recirculated water at a relatively low pH; and
flowing the flue gas through a combination wet desulfurization system and condenser for contact with a water spray, NaOH and an oxidizing catalyst to produce cleaned flue gas for release to the atmosphere.
3. A method for removing SO 2 from waste combustion flue gas containing SO 2 comprising:
flowing the flue gas through a combination wet desulfurization system and condenser for contact with a recirculated water spray, NaOH and an oxidizing catalyst to produce cleaned flue gas for release to the atmosphere.
4. The method of claim 1 , 2 or 3 , further comprising:
providing air, oxygen or an oxygen enriched gas to the quench, combined wet desulfurization system and quench, condenser, combined wet desulfurization system and condenser or a combination thereof to promote oxidation therein.
5. The method of claim 1 , 2 or 3 , wherein said oxidizing catalyst is FeSO 4 .
6. The method of claim 1 , 2 or 3 , wherein said oxidizing catalyst is 0.0001 to 0.200 mM of FeSO 4 .
7. The method of claim 1 , 2 or 3 , wherein said pH in said condenser is 5.0 to 7.5.
8. A system for removing SO 2 from waste combustion flue gas containing SO 2 comprising:
a semi-dry desulfurization system for contacting the flue gas with a solvent moistened absorption material;
a recirculated water quench for contacting the flue gas with recirculated water at a relatively low pH;
a condenser for contacting the flue gas with a water spray;
an NaOH supply supplying NaOH to the condenser; and
an oxidizing catalyst supply supplying oxidizing catalyst to the condenser to produce cleaned flue gas for release to the atmosphere.
9. A system for removing SO 2 from waste combustion flue gas containing SO 2 comprising:
a combination wet desulfurization system and quench for contacting the flue gas with an absorption material slurry and recirculated water at a relatively low pH;
a combination wet desulfurization system and condenser for contacting the flue gas with a water spray;
a NaOH supply for supplying NaOH to the combination wet desulfurization system and condenser for contacting the flue gas and water spray; and
an oxidizing catalyst supply for supplying oxidizing catalyst to the combination wet desulfurization system and condenser for contacting the flue gas and water spray to produce cleaned flue gas for release to the atmosphere.
10. A system for removing SO 2 from waste combustion flue gas containing SO 2 comprising:
a combination wet desulfurization system and condenser for contacting the flue gas with a recirculated water spray;
a NaOH supply for supplying NaOH to the combination wet desulfurization system and condenser for contacting the flue gas; and
an oxidizing catalyst supply for supplying oxidizing catalyst to the combination wet desulfurization system and condenser for contacting the flue gas to produce cleaned flue gas for release to the atmosphere.
11. The system of claim 8 , 9 or 10 , further comprising:
an oxygen supply source to provide air, oxygen, or an oxygen enriched gas to the system to promote oxidation therein.
12. The system of claim 8 , 9 or 10 , wherein said oxidizing catalyst is FeSO 4 .
13. The system of claim 8 , 9 or 10 , wherein said oxidizing catalyst is 0.0001 to 0.200 mM of FeSO 4 .
14. The system of claim 8 , 9 or 10 wherein said pH in said condenser or combined wet desulfurization system and condenser is 5.0 to 7.5.
15. The system of claim 8 , 9 or 10 , wherein heat from said condenser or combined wet desulfurization system and condenser is used in a district heating system.