Process for the low-corrosion and low-emission co-incineration of highly halogenated wastes in waste incineration plants

• US 20030065236A1
• Filed: 06/26/2002
• Published: 04/03/2003
• Est. Priority Date: 06/29/2001
• Status: Abandoned Application

• Current Assignee: Bayer AG
• Original Assignee: Bayer AG
• Inventors: Krippner, Peter, Vosteen, Bernhard, Beyer, Joachim
• Application Number:
  US10/180,358
• Publication Number:
  US 20030065236A1
• Time in Patent Office: Days
• US Class Current: 588/208
• CPC Class Codes: F23G 2207/60 Additives supply
• CPC Class Codes: F23G 5/16 in a separate combustion chamber
• CPC Class Codes: F23G 5/50 Control or safety arrangements
• CPC Class Codes: F23J 15/04 using washing fluids scrubbers for removing solids only F23J15/022

Abstract

The invention relates to a process and an apparatus for the low-corrosion and low-emission co-incineration of highly halogenated wastes, in particular liquid waste, in waste incineration plants having at least one combustion chamber, a waste-heat boiler, a multistage flue gas scrubber comprising a single-stage or multistage acidic scrubber and an alkaline scrubber, in which sulfur or a corresponding sulfur carrier is added under control to the primary and/or secondary combustion chamber. The amount of sulfur is controlled substantially in proportion to the current halogen loading originating from the waste in the boiler flue gas.

Claims

1. A process for low-corrosion and low-emission co-incineration of highly halogenated liquid wastes comprising co-incinerating a highly halogenated liquid waste in a waste incineration plant having at least one combustion chamber, a waste-heat boiler, and a multistage flue gas scrubber comprising an acidic scrubber and alkaline scrubber, wherein sulfur or a sulfur carrier is added to the combustion chamber by controlled addition in an amount substantially in proportion to the halogen loading.

2. A process according to claim 1 wherein the amount of sulfur is added under control in proportion to the current loading of chlorine, bromine, or iodine in the waste.

3. A process according to claim 1 wherein the amount of sulfur is added in accordance with an operationally determined sulfur addition ramp that stipulates the residual SO₂ content in the dirty gas downstream of the boiler and upstream of the quench that is required at the current halogen loading for the high-halogen wastes.

4. A process according to claim 1 wherein a linear sulfur addition ramp is determined operationally in each case for high-halogen wastes by determining for at least one greater halogen loading in the waste the minimally required SO₂ content in the dirty boiler gas at which, in steady state operations, no free halogen or only an amount of free halogen below a set-point limiting value can be detected in the clean gas downstream of the flue gas scrubber.

5. A process according to claim 1 wherein the current flue gas-side halogen loading is continuously determined approximately as halide loading in the acidic flue gas scrubber effluent, determined as the product of halide concentration and effluent volumetric flow rate.

6. A process according to claim 1 wherein current flue gas-side halogen loading is continuously determined by measuring halogen and hydrogen halide species in the dirty boiler gas upstream of the quench and downstream of the boiler and the dry flue gas volumetric flow rate or a parameter proportional to the flue gas volumetric flow rate.

7. A process according to claim 1 wherein the amount of sulfur that corresponds to the halogen loading in the flue gas or the halide loading in the acidic scrubber effluent in accordance with the sulfur addition ramp is briefly elevated by 5 to 100% as soon as free halogen is measured in the clean gas downstream of the flue gas scrubber but still upstream of any following SCR catalyst bed.

8. A process according to claim 1 wherein the amount of sulfur that corresponds to the halogen loading in the flue gas or the halide loading in the acidic scrubber effluent in accordance with the sulfur addition ramp is briefly increased by 5 to 100% as soon as a rapid increase in halide concentration in the acidic scrubber effluent is measured.

9. A process according to claim 1 wherein the sulfur is added in the form of solid sulfur, liquid sulfur, or waste sulfuric acid.

10. A process according to claim 1 wherein solid sulfur is added in pelleted or granulated form via controllable metering elements.

11. A process according to claim 1 wherein solid sulfur is fed into the primary combustion chamber by pneumatic transport.

13. A process according to claim 1 wherein waste sulfuric acid is fed into the primary or secondary combustion chamber via an atomizer nozzle or corresponding jet assemblies.

14. A process according to claim 1 wherein for a periodically changing halogen loading in the flue gas that results from a timed feed of high-halogen individual packages, the sulfur and/or other sulfur carrier is added in an amount that is coupled to the timing of the feed and matched to the size of the packages with respect to height, timepoint, and time period.

15. A process according to claim 14 wherein the addition of sulfur and/or other sulfur carrier that is coupled to the timing of the feed and matched to the size of the packages with respect to height, timepoint, and time period, is carried out using automatically read-in individual bar codes for the heating value, type of halogen, and amount of halogen of the packages.

16. A process according to claim 1 wherein hypohalite reduction in the alkaline scrubber proceeds via the bisulfide that forms internally in the process from the residual SO₂ of the dirty boiler gas and at the same time or alone via an externally added reducing agent.

17. A process according to claim 3 wherein a sulfur addition ramp that is determined operationally for a pure chlorine-containing waste is also used for the combustion of halogen mixtures that, in addition to chlorine, comprise other halogens.

12. A process according to Clam 1 wherein waste sulfuric acid is added to the primary or secondary combustion chamber via controllable metering pumps.

18. A waste incineration plant having a combustion chamber, a waste-heat boiler, a multistage flue gas scrubber comprising an acidic scrubber and an alkaline scrubber, wherein the waste incineration plant has one or more control devices for the controlled addition of sulfur and/or other sulfur carriers into a primary or secondary combustion chamber.

19. A waste incineration plant according to claim 18 having one or more metering systems and one or more transport systems for the controlled addition of sulfur or other sulfur carriers into the primary or secondary combustion chamber.

20. A waste incineration plant according to claim 19 wherein the system for the controlled addition of sulfur or other sulfur carriers is a controllable transport system.

21. A waste incineration plant according to claim 20 wherein the system for the controlled addition of waste sulfuric acid is a controllable metering pump and the waste sulfuric acid is injected via a nozzle and/or a jet assembly into the primary or secondary combustion chamber.

22. A waste incineration plant according to claim 18 wherein at least one control device has a primary control circuit having set-point value control of the continuously measured residual SO₂ content in the dirty boiler gas upstream of the quench or, in a corresponding extended control circuit, has an additional feed-forward control in which the primary control circuit controls the sulfur addition according to a sulfur addition ramp in proportion to the current halogen loading in the flue gas or to the halide loading in the acidic effluent.

23. A waste incineration plant according to claim 19 wherein at least one control device has a primary control circuit having set-point value control of the SO₂ content in the flue gas upstream of the boiler calculated on-line or, in a corresponding extended control circuit, has additional feed-forward control in which the primary control circuit controls the sulfur addition on the basis of a continuous halogen-specific conversionary calculation via the speed of rotation of the metering system taking into account the transport characteristic of the metering system in proportion to the current halogen loading in the flue gas or to the halide loading in the acidic effluent.

24. A waste incineration plant according to claim 22 wherein the corresponding extended control circuit, at the start of Cl₂ breakthrough into the clean gas and/or in the event of a rapid increase in halide content in the acidic effluent, temporarily elevates the sulfur addition by feed-forward control.

25. A waste incineration plant according to claim 23 wherein the corresponding extended control circuit, at the start of Cl₂ breakthrough into the clean gas and/or in the event of a rapid increase in halide content in the acidic effluent, temporarily elevates the sulfur addition by feed-forward control.

26. A waste incineration plant according to claim 22 wherein the control circuit is a linear sulfur addition ramp that is determined operationally in each case for high-halogen wastes by determining for at least one greater halogen loading in the waste the minimally required SO₂ content in the dirty boiler gas at which, in steady state operations, no free halogen or only an amount of free halogen below a set-point limiting value can be detected in the clean gas downstream of the flue gas scrubber.

27. A waste incineration plant according to claim 22 wherein the current halogen loading is continuously determined approximately as halide loading in the acidic flue gas scrubber effluent, determined as the product of halide concentration and effluent volumetric flow rate.

28. A waste incineration plant according to claim 22 wherein the current halogen loading is continuously determined by measuring halogen and hydrogen halide species in the dirty boiler gas upstream of the quench and downstream of the boiler and the dry flue gas volumetric flow rate or a parameter proportional to the flue gas volumetric flow rate.