Integrated flue gas processing system

Claim 2

An integrated system for processing hot flue gas by removal of both particulate material such as flyash and gaseous contaminants such as sulfur dioxide from flue gas comprising a scrubbing tower, means for feeding hot flue gas to the tower for upward flow therein, means for spraying alkali slurry into the flue gas to react with sulfur dioxide therein, electrostatic precipitation means connected to the tower located downstream of the alkali spraying means for precipitating flyash from the scrubbed flue gas, the electrostatic precipitation means comprising discharge electrode means and collection electrode means, the discharge electrode means and collection electrode means together defining a channel for the passage of flue gas therebetween, the collection electrode means having a surface on which the particulate material is precipitated, means spaced from the collection electrode means for defining a chamber is proximity thereto, means for circulating air in the chamber over the collection electrode means to heat the air and to remove heat from the flue gas passing through the channel between the discharge electrode means and collection electrode means and duct means for conducting the heated air to mixing means in communication with the duct means and located within the flue gas processing system for mixing the heated air with one or more gas streams in the system to utilize the heat removed from the flue gas within the processing system to contribute to heating of the gas stream with which the heated air is mixed.

Claim 3

The integrated system for processing flue gas as claimed in claim 1 wherein the heat exchanging medium in the chamber cools the collection electrode means surfaces sufficiently to condense water vapor present in the scrubbed flue gas thereon to flush the collection electrode surfaces of particles precipitated thereon.

Claim 4

The integrated system for processing hot flue gas as claimed in claim 1 wherein the mixing means comprises means for mixing the heated air with the cleaned flue gas stream exiting from the wet electrostatic precipitator for reheating it.

Claim 5

The integrated system for processing hot flue gas as claimed in claim 1 wherein the mixing means comprises means for mixing the heated air with combustion air fed to a boiler from which the flue gas emanates for preheating it.

Claim 6

The integrated system for processing hot flue gas as claimed in claim 4 further comprising means for further heating the mixed heated air and combustion air and means for conducting a portion of the thus heated mixed air stream to means for mixing with the cleaned flue gas stream exiting from the wet electrostatic precipitator for reheating it.

Claim 7

The integrated system for processing flue gas as claimed in claim 1 wherein the collection electrode means comprises collection tubes having a length (L) and an inner diameter (D) and the discharge electrode means comprises an electrode mast of electrically conducting material having a diameter of from 0.25 to 0.40 D, and a helical screw flight around the electrode mast, the screw flight being made of an electrically conducting material having an outer diameter (d) of from 0.33 to 0.67 D, and a substantially symmetrically curved outer discharge edge in cross section.

Claim 8

The integrated system for processing flue gas as claimed in claim 6 wherein the helix of the discharge electrode is spaced at a distance greater than D-d/2 from each end of the collector tube.

Claim 9

The integrated system for processing flue gas as claimed in claim 6 wherein the pitch of the discharge electrode helical screw flight is from D-d/2 to D-d, and the overall length (1) of the helical screw flight is from one screw revolution to L-(D-d).

Claim 10

The integrated system for processing flue gas as claimed in claim 8 further comprising means for providing a high strength electric field between the collection electrode means and the discharge electrode means; whereby a substantially symmetrical, high density current flow between the discharge electrode and the collection tube is created when high voltage is applied to the discharge electrode.

Claim 11

The integrated system for processing flue gas as claimed in claim 6, 7, 8 or 9 wherein the heat exchanging medium in the chamber cools the collection surfaces sufficiently to condense water vapor present in the scrubbed flue gas thereon to flush the collection tube surfaces of particles precipitated thereon.

Claim 12

An integrated system for removing sulfur dioxide and flyash from hot flue gas comprising a scrubbing tower, a low pressure-drop venturi scrubber quencher located upstream of the scrubbing tower, means for feeding hot flue gas to the venturi scrubber quencher, means for introducing aqueous slurry to the venturi scrubber quencher to saturate the flue gas with water vapor and remove coarse flyash particles from the flue gas, duct means for connecting the venturi scrubber quencher to the scrubber tower and conducting the flue gas from the venturi scrubber quencher to the tower for upward flow therein, spray means located within the tower for spraying alkali slurry into the flue gas to absorb and react with the sulfur dioxide therein, means located within the tower for collecting and recirculating slurry containing absorbed sulfur dioxide to the spray means to increase the residence time for the reaction of alkali and sulfur dioxide, discharge means connected to the tower for removing slurry containing reaction products of alkali and sulfur dioxide and precipitated flyash from the tower, means connected to the discharge means for dewatering the slurry so removed to obtain a waste product, interface tray means located in the tower downstream of the alkali slurry spray means, means for spraying the interface tray means with an unreactive aqueous solution, a wet electrostatic precipitator located downstream of the tower and connected thereto by flue gas directing means for electrostatically removing flyash and entrained slurry droplets from the scrubbed flue gas, the wet electrostatic precipitator comprising a cross flow heat exchanger having collection electrode tubes through which the flue gas passes, the tubes being arranged between tube sheets, means for causing ambient air to flow across the outside of the tubes to remove heat from the flue gas and heat the flowing ambient air to cool the tube walls to cause condensation on the tube wall surfaces, and duct means connected to the heat exchanger to conduct the heated flowing ambient air means to mixing means for mixing at least part of the heated air with combustion air for the boiler furnace, the flue gas of which is being processed, to preheat the combustion air, boiler combustion air preheater means for preheating the combustion air mixed with the heated air, means for passing the mixed air stream through the preheater means, means located downstream of the preheater means to separate and conduct a portion of the further preheated mixed air stream to means for mixing with the cleaned flue gas stream leaving the wet electrostatic precipitator to reheat it.

Claim 13

An integrated system for removing sulfur dioxide and flyash from hot flue gas comprising a scrubbing tower, a low pressure-drop venturi scrubber quencher located upstream of the scrubbing tower, means for feeding hot flue gas to the venturi scrubber quencher, means for introducing aqueous slurry to the venturi scrubber quencher to saturate the flue gas with water vapor and remove coarse flyash particles from the flue gas, duct means for connecting the venturi scrubber quencher to the scrubber tower and conducting the flue gas from the venturi scrubber quencher to the tower for upward flow therein, spray means located within the tower for spraying alkali slurry into the flue gas to absorb and react with the sulfur dioxide therein, means located within the tower for collecting and recirculating slurry containing absorbed sulfur dioxide to the spray means to increase the residence time for the reaction of alkali and sulfur dioxide, discharge means connected to the tower for removing slurry containing reaction products of alkali and sulfur dioxide and precipitated flyash from the tower, means connected to the discharge means for dewatering the slurry so removed to obtain a waste product, interface tray means located in the tower downstream of the alkali slurry spray means, means for spraying the interface tray means with an unreactive aqueous solution, a wet electrostatic precipitator located downstream of the tower and connected thereto by flue gas directing means for electrostatically removing flyash and entrained slurry droplets from the scrubbed flue gas, the wet electrostatic precipitator comprising a cross flow heat exchanger having collection electrode tubes through which the flue gas passes, the tubes being arranged between tube sheets, means for causing ambient air to flow across the outside of the tubes to remove heat from the flue gas and heat the flowing ambient air to cool the tube walls to cause condensation on the tube wall surfaces, and duct means connected to the heat exchanger to conduct the heated flowing ambient air means to mixing means for mixing at least part of the heated air with combustion air for the boiler furnace, the flue gas of which is being processed, to preheat the combustion air, boiler combustion air preheater means for preheating the combustion air mixed with the heated air, means for passing the mixed air stream through the preheater means, means located downstream of the preheater means to separate and conduct a portion of the further preheated mixed air stream to means for mixing with the cleaned flue gas stream leaving the wet electrostatic precipitator to reheat it.

Claim 14

An integrated system for removing sulfur dioxide and flyash from flue gas as claimed in claim 11 wherein the cross-sectional area of the scrubbing tower and the wet electrostatic precipitator through which the flue gas flows are approximately the same.

Claim 15

An integrated system for removing sulfur dioxide and flyash from flue gas as claimed in claim 11 wherein the wet electrostatic precipitator comprises a discharge electrode having a helical discharge surface and effective large diameter high velocity characteristics producing a totally symmetric electrostatic field.