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An oxygen fueled integrated pollutant removal and combustion system includes a combustion system and an integrated pollutant removal system. The combustion system includes a furnace having at least one burner that is configured to substantially prevent the introduction of air. An oxygen supply suppl

An oxygen fueled integrated pollutant removal and combustion system includes a combustion system and an integrated pollutant removal system. The combustion system includes a furnace having at least one burner that is configured to substantially prevent the introduction of air. An oxygen supply supplies oxygen at a predetermine purity greater than 21 percent and a carbon based fuel supply supplies a carbon based fuel. Oxygen and fuel are fed into the furnace in controlled proportion to each other and combustion is controlled to produce a flame temperature in excess of 3000 degrees F. and a flue gas stream containing CO2 and other gases. The flue gas stream is substantially void of non-fuel borne nitrogen containing combustion produced gaseous compounds. The integrated pollutant removal system includes at least one direct contact heat exchanger for bringing the flue gas into intimated contact with a cooling liquid to produce a pollutant-laden liquid stream and a stripped flue gas stream and at least one compressor for receiving and compressing the stripped flue gas stream.

대표청구항 ▼

1. An oxygen fueled integrated pollutant removal and combustion system comprising: an oxy-fuel combustion system for producing a flue gas containing CO2 and other gases and substantially void of non-fuel borne nitrogen containing combustion produced gaseous compounds; anda pollutant removal system f

1. An oxygen fueled integrated pollutant removal and combustion system comprising: an oxy-fuel combustion system for producing a flue gas containing CO2 and other gases and substantially void of non-fuel borne nitrogen containing combustion produced gaseous compounds; anda pollutant removal system for directly receiving flue gas from said oxy-fuel combustion system and consolidating removal of multiple pollutants from said flue gas in a single process, said pollutant removal system comprising:at least one direct contact heat exchanger for bringing said flue gas into intimated contact with a cooling liquid to produce a pollutant-laden liquid stream which includes soluble and entrained particulates and a stripped flue gas stream containing condensable and non-condensable vapors;a discharge for discharging said pollution laden stream;one or more compressors for receiving said stripped flue gas stream from said at least one direct contact heat exchanger and compressing said stripped flue gas stream defining a compressed flue gas stream;at least one heat exchanger for receiving the compressed flue gas stream from said at least one or more compressors, said one or more compressors and said at least one heat exchanger configured to separate condensable vapors from non-condensable vapors by way of cooling of said compressed flue gas stream in order to condense said CO2 and any other condensable vapors defining condensed vapors and non-condensable vapors;a discharge connected to said at least one heat exchanger for discharging said condensed vapors; anda filter connected to said at least one heat exchanger for filtering said non-condensable vapors before releasing the flue gas to the atmosphere. 2. The integrated combustion system in accordance with claim 1 wherein the cooling liquid is water. 3. The integrated combustion system in accordance with claim 1 including at least two compressors. 4. The integrated combustion system in accordance with claim 1 wherein the stripped flue gas stream is separated into non-condensable gases and condensable gases. 5. The integrated combustion system in accordance with claim 4 wherein the condensable gases are condensed into a substantially liquid state. 6. The integrated combustion system in accordance with claim 5 wherein the gases condensed into the substantially liquid state are sequestered. 7. The integrated combustion system in accordance with claim 6 wherein the gases condensed into the substantially liquid state are, in large part, CO2. 8. The integrated combustion system in accordance with claim 1 wherein the carbon based fuel is a solid fuel and wherein the stripped flue gas stream is recirculated, in part, to carry the carbon based fuel into the oxy-fuel combustor. 9. The integrated combustion system in accordance with claim 8 wherein the stripped flue gas stream is substantially CO2. 10. The integrated combustion system in accordance with claim 1 further including at least two heat exchangers and a plurality of compressors, wherein at least two of the heat exchangers are direct contact heat exchangers for intimately contacting cooling water with the flue gas stream and wherein at least one of said plurality of compressors is disposed between the heat exchangers for compressing the stripped flue gas, stream between the heat exchangers. 11. The integrated combustion system in accordance with claim 1 including at least two heat exchangers. 12. A combustion and integrated pollutant removal method comprising the steps of: initiating combustion in an oxy-fuel combustion system producing a flue gas stream containing CO2 and other gases and substantially void of non-fuel borne nitrogen containing combustion produced gaseous compounds; anddirecting the flue gas to a pollutant removal system which includes a direct contact heat exchanger in serial arrangement with a compressor;bringing the flue gas into intimated contact with a cooling liquid in the heat exchanger to produce a pollutant-laden liquid stream and a stripped flue gas stream;discharging said pollutant laden stream;feeding the stripper flue gas stream into at least one compressor and at least one heat exchanger configured to separate CO2 and other condensable vapors from non-condensable vapors in the stripped flue gas stream;discharging said CO2 and other condensable vapors;filtering said non-condensable vapors from said stripped flue gas stream; anddischarging said stripped flue gas stream to the atmosphere. 13. The method in accordance with claim 12 including the steps of cooling the stripped flue gas stream by compressing the cooled stripped flue gas stream. 14. The method in accordance with claim 13 including the step of sequestering the compressed cooled stripped flue gas stream. 15. The integrated combustion system in accordance with claim 1 wherein the at least one compressor is used in a gas compression stage to compress gasses and wherein said at least one compressor includes more than one compression stage. 16. The integrated combustion system in accordance with claim 1 wherein the heat exchanger is used in a gas-to-liquid condensation stage to produce a condensate stream and there is more than one condensation stage. 17. The integrated combustion system in accordance with claim 1 wherein the stripped flue gas is compressed and cooled to produce a liquid. 18. The integrated combustion system in accordance with claim 17 wherein the liquid produced is in large part CO2. 19. The integrated combustion system in accordance with claim 1 wherein the carbon based fuel is a solid fuel. 20. The integrated combustion system in accordance with claim 19 wherein the solid fuel is coal. 21. The integrated combustion system in accordance with claim 20 wherein part of the flue gas stream is recirculated, in part, to carry the carbon based fuel into the furnace.