Process for removing mercury from flue gases

• US 20040013589A1
• Filed: 07/24/2002
• Published: 01/22/2004
• Est. Priority Date: 07/22/2002
• Status: Abandoned Application

• Current Assignee: Bayer AG
• Original Assignee: Bayer AG
• Inventors: Bonkhofer, Theodor-Gerhard, Mueller, Claus, Nolte, Michael, Beyer, Joachim, Fleth, Olaf, Standau, Ewa, Vosteen, Bernhard, Kanefke, Rico, Pohontsch, Andreas, Koeser, Heinz, Wieland, Andrea
• Application Number:
  US10/202,571
• Publication Number:
  US 20040013589A1
• Time in Patent Office: Days
• US Class Current: 423/210
• CPC Class Codes: B01D 53/64 Heavy metals or compounds thereof, e.g. mercury

Abstract

The invention describes a process for removing mercury from flue gases of high-temperature plants, in particular power stations and waste incineration plants in which a bromine compound is fed to the if appropriate multistage furnace and/or the flue gas in a plant section downstream of the furnace, the temperature during contact of the bromine compound with the flue gas being at least 500° C., preferably at least 800° C. The combustion is carried out in the presence of a sulphur compound, in particular sulphur dioxide. Subsequently to the furnace, the flue gas is subjected to an if appropriate multistage cleanup for removing mercury from the flue gas, which cleanup comprises a wet scrubber and/or a dry cleanup.

Claims

1. Process for removing mercury from flue gases of high-temperature plants, in particular from power stations and waste incineration plants, characterized in that

bromine and/or a bromine compound and/or a mixture of various bromine compounds is fed to the if appropriate multistage furnace and/or to the flue gas in a plant section downstream of the furnace, the temperature during the contact of the bromine compound with the flue gas being at least 500°

C., preferably at least 800°

C.,

the combustion taking place in the presence of a sulphur compound, in particular sulphur dioxide, with or without the addition of sulphur and/or a sulphur compound and/or of a mixture of various sulphur compounds,

and then the flue gas being subjected to an if appropriate multistage cleanup for removing mercury from the flue gas, which cleanup comprises a wet scrubber and/or a dry cleanup.

2. Process according to claim 1, characterized in that the bromine compound is an aqueous solution of hydrogen bromide and/or an alkali metal bromide, in particular sodium bromide, and/or an aqueous solution of alkali metal bromide.

3. Process according to one of claims 1 to 2, characterized in that the bromine compound and/or the mixture of bromine compounds are liquid and/or solid high-bromine wastes.

4. Process according to one of claims 1 to 3, characterized in that the bromine and/or the bromine compound and/or the mixture of bromine compounds is added to the combustion air and/or if appropriate a recycled substream, in particular the recycled flue gas and the recycled fly ash.

5. Process according to one of claims 1 to 4, characterized in that the mass ratio of bromine to mercury is in the range from 102 to 104.

6. Process according to one of claims 1 to 5, characterized in that the combustion is carried out additionally in the presence of chlorine and/or a chlorine compound and/or a mixture of various chlorine compounds and/or iodine and/or an iodine compound and/or a mixture of various iodine compounds.

7. Process according to one of claims 1 to 6, characterized in that the flue gas emission control system comprises a multistage wet flue gas scrubber having at least one strongly acidic scrubbing stage and/or at least one weakly acidic and/or akaline scrubbing stage.

8. Process according to one of claims 1 to 7, characterized in that the flue gas emission control system comprises at least one dry or semi-dry absorption-based emission control stage, in particular using electrostatic or filtering dust separators.

9. Process according to claim 8, characterized in that the fly ash loaded with mercury from any dust separators present is given a thermal secondary treatment to decrease mercury load, in particular in a rotary drum heated to temperatures of at least 200°

C.

10. Process according to one of claims 1 to 9, characterized in that the mercury content of the flue gas, in particular the content of metallic mercury, is measured continuously downstream of the flue gas emission control system and on the basis of the measured mercury content the amount of bromine fed and/or bromine compounds fed and any sulphur and/or sulphur compounds fed is controlled.