초록 ▼

A method for producing steam while concurrently reducing emissions. The method includes combusting fuel and an oxidant stream having a high concentration of oxygen in a combustion zone having multiple combustion chambers and heat exchangers to produce a flue gas. The flue gas is subsequently cleaned

A method for producing steam while concurrently reducing emissions. The method includes combusting fuel and an oxidant stream having a high concentration of oxygen in a combustion zone having multiple combustion chambers and heat exchangers to produce a flue gas. The flue gas is subsequently cleaned in a dry flue gas cleaning chamber by contacting it with a dry adsorbent. In one embodiment, the method advantageously regenerates the dry adsorbent so that the dry adsorbent can be subsequently recycled back into the dry gas flue chamber.

대표청구항 ▼

1. A steam-generating oxy-boiler system comprising: an oxidant delivery system for providing an oxidant enriched gas stream having an oxygen content of 75 to 100% by volume;a first combustion chamber in fluid communication with the oxidant delivery system, wherein the first combustion chamber is ope

1. A steam-generating oxy-boiler system comprising: an oxidant delivery system for providing an oxidant enriched gas stream having an oxygen content of 75 to 100% by volume;a first combustion chamber in fluid communication with the oxidant delivery system, wherein the first combustion chamber is operable to combust a portion of a fuel stream in the presence of the oxidant enriched gas stream to generate a first product stream comprised of flue gas and non-combusted fuel;a first heat exchanger in fluid communication with the first combustion chamber, wherein the first heat exchanger is operable to remove heat from the first product stream such that the temperature of the first product stream is maintained within a desired range;a second combustion chamber in fluid communication with the first heat exchanger, wherein the second combustion chamber is operable to combust a portion of the non-combusted fuel of the first product stream to produce a second product stream, wherein the second product stream has a greater amount of flue gas as compared to the first product stream, wherein the first combustion chamber further comprises water circulating within walls of the first combustion chamber for regulating the temperature within the first combustion chamber, wherein the second combustion chamber further comprises water circulating within walls of the second combustion chamber for regulating the temperature within the second combustion chamber;a second heat exchanger in fluid communication with the second combustion chamber, wherein the second heat exchanger is operable to remove heat from the second product stream such that the temperature of the second product stream is maintained within a desired range;a flue gas cleaning chamber in fluid communication with the second heat exchanger, the flue gas cleaning chamber having an amount of a solid adsorbent contained therein that is operable to remove, via a chemical reaction, at least a portion of SOx from the second product stream and an amount of a reducing agent contained therein that is operable to remove, via a chemical reaction, at least a portion of NOx from the second product stream to produce a third product stream, the third product stream comprising a desulfurized and denitrified flue gas and spent adsorbent, the desulfurized and denitrified flue gas having reduced amounts of SOx and NOx as compared to the flue gas within the second product stream, wherein the solid adsorbent and the reducing agent are independently fed into the flue gas cleaning chamber;a precipitating unit in fluid communication with the flue gas cleaning chamber for removing the spent adsorbent from the desulfurized and denitrified flue gas to produce a spent adsorbent stream and a cleaned desulfurized and denitrified flue gas stream;an adsorbent storage tank in fluid communication with the precipitating unit for receiving the spent adsorbent stream;a discharge line in fluid communication with the precipitating unit for sending the cleaned desulfurized and denitrified flue gas stream to a CO2 recovery unit or to the atmosphere;a reducing gas feed line in fluid communication with the flue gas cleaning chamber for introducing reducing gas to the flue gas cleaning chamber;a regeneration unit in fluid communication with the adsorbent storage tank, the reducing gas feed line, and the flue gas cleaning chamber, the regeneration unit operable to regenerate a portion of the spent adsorbent stream by contacting the spent adsorbent stream with the reducing gas to produce regenerated adsorbent and spent reducing gas, wherein the regenerated adsorbent is then recycled back to the flue gas cleaning chamber; anda sulfur discharge line in fluid communication with the regeneration unit, the sulfur discharge line operable to introduce the spent reducing gas to a sulfur recovery unit,a third heat exchanger in fluid communication with the precipitating unit and the discharge line, the third heat exchanger operable to transfer heat energy from the flue gas stream to a target fluid prior to sending the cleaned flue gas stream to the CO2 recovery unit or to the atmosphere, wherein the target fluid is the water before circulating within the walls of the first combustion chamber and within the walls of the second combustion chamber;wherein the walls comprise membrane tubes and welded fins connecting the membrane tubes. 2. The system of claim 1, wherein the solid adsorbent has particle sizes in the range of 50 to 500 microns. 3. The system of claim 1, wherein the solid adsorbent is selected from the group consisting of MgO, CaO, and combinations thereof. 4. The system of claim 1, wherein the precipitating unit comprises a first precipitator, the first precipitator operable to remove all of the spent adsorbent from the desulfurized and denitrified flue gas. 5. The system of claim 1, wherein the first heat exchanger is further operable to receive the target fluid from the third heat exchanger and exchange heat between the first product stream and the target fluid such that the temperature of the first product stream is maintained within a desired range.