초록 ▼

The objective of this invention is to develop a method to reclaim functional sites on a CO2 sorbent that have reacted with an acid gas (other than CO2) to form heat stable salts (HSS). HSS are a significant concern for dry sorbent based CO2 capture because over time the buildup of HSS will reduce th

The objective of this invention is to develop a method to reclaim functional sites on a CO2 sorbent that have reacted with an acid gas (other than CO2) to form heat stable salts (HSS). HSS are a significant concern for dry sorbent based CO2 capture because over time the buildup of HSS will reduce the overall functionality of the CO2 sorbent. A chemical treatment can remove the non-CO2 acid gas and reclaim functional sites that can then be used for further CO2 adsorption.

대표청구항 ▼

1. A method, comprising: receiving a gas stream, the gas stream comprising a target gas component and at least one acid gas, the at least one acid gas being different from the target gas component;contacting the gas stream with a sorbent to remove at least a portion of the target gas component to fo

1. A method, comprising: receiving a gas stream, the gas stream comprising a target gas component and at least one acid gas, the at least one acid gas being different from the target gas component;contacting the gas stream with a sorbent to remove at least a portion of the target gas component to form a purified gas stream and a loaded sorbent comprising the removed target gas component, the sorbent also removing and the loaded sorbent also comprising a portion of the at least one acid gas;removing at least most of the removed target gas component from the loaded sorbent to form a lean sorbent comprising at least most of the removed portion of the at least one acid gas and/or a salt thereof; andcontacting the lean sorbent with a regeneration solution to remove at least most of the removed portion of the at least one acid gas and/or a salt thereof and form for recycle to the gas stream contacting step the sorbent,wherein the target gas component is a carbon oxide, wherein the at least one acid gas is one or more of a sulfur oxide, a nitrogen oxide and hydrogen sulfide, wherein the sorbent is an amine-base sorbent, and wherein the regeneration solution has a pH of at least pH 10. 2. The method of claim 1, wherein the acid gas comprises SO2, wherein the target gas component is CO2, wherein the regeneration solution comprises a base, wherein at least most of the CO2 in the received gas stream is removed by the sorbent, wherein CO2 is removed from the loaded sorbent by one or more of a pressure swing, temperature swing, and combination thereof, and wherein the sorbent is in the form of a solid. 3. A method comprising: receiving a gas stream, the gas stream comprising a target gas component and at least one acid gas, the at least one acid gas being different from the target gas component;contacting the gas stream with a sorbent to remove at least a portion of the target gas component to form a purified gas stream and a loaded sorbent comprising the removed target gas component, the sorbent also removing and the loaded sorbet also comprising a portion of the at least one acid gas;removing at least most of the removed target gas component from the loaded sorbent to form a lean sorbent comprising at least most of the removed portion of the at least one acid gas and/or a salt thereof; andcontacting the lean sorbent with a regeneration solution to remove at least most of the removed portion of the at least one acid gas and/or a salt thereof and form for recycle to the gas stream contacting step the sorbent,wherein bonds between adjacent sorbent components and between the sorbent components and an adjacent sorbent substrate are stronger than bonds between the sorbent component and the target gas component and between the sorbent component and the at least one acid gas and/or salt thereof. 4. The method of claim 3, wherein the regeneration solution does not significantly impact the strengths of the bonds between the between adjacent sorbent components and between the sorbent components and an adjacent sorbent substrate. 5. The method of claim 4, wherein the regeneration solution comprises a base that is at least one of an alkali or alkaline earth metal carbonate, at least one of an alkali or alkaline earth metal hydroxide, an alkoxide, a metal oxide, ammonia, a metal amine, a carboxylate, a phosphine, an ether, a ketone, an alkene, and CH3−. 6. A method, comprising: receiving a gas stream, the gas stream comprising a target gas component and at least one acid gas, the at least one acid gas being different from the target gas component;contacting the gas stream with a sorbent to remove at least a portion of the target gas component to form a purified gas stream and a loaded sorbent comprising the removed target gas component, the sorbent also removing and the loaded sorbent also comprising a portion of the at least one acid gas;removing at least most of the removed target gas component from the loaded sorbent to form a lean sorbent comprising at least most of the removed portion of the at least one acid gas and/or a salt thereof;contacting the lean sorbent with a regeneration solution to remove at least most of the removed portion of the at least one acid gas and/or a salt thereof and form for recycle to the gas stream contacting step the sorbent; andafter contact of the lean sorbent with the regeneration solution, contacting the sorbent with a wash solution to remove any deposit on the sorbent after contact with the regeneration solution. 7. A system, comprising: a gas component separator configured to (a) receive a gas stream, the gas stream comprising a target gas component and at least one acid gas, the at least one acid gas being different from the target gas component, and (b) contact the gas stream with a sorbent to remove at least a portion of the target gas component and a portion of the at least one acid gas to form a purified gas stream and a loaded sorbent comprising the removed target gas and the removed acid gas;a sorbent regenerator configured to remove at least most of the removed target gas component from the loaded sorbent to form a lean sorbent comprising at least most of the removed acid gas and/or a salt thereof; anda regeneration vessel configured to contact the lean sorbent with a regeneration solution to remove at least most of the removed acid gas and/or a salt thereof and form for recycle to the gas component separator the sorbent,wherein the target gas component is a carbon oxide, wherein the at least one acid gas is one or more of a sulfur oxide, a nitrogen oxide and hydrogen sulfide, wherein the sorbent is an a mine-base sorbent, and wherein the regeneration solution has a pH of at least about pH 10. 8. The system of claim 7, wherein the acid gas comprises SO2, wherein the target gas component is CO2, wherein the regeneration solution comprises a base, wherein at least most of the CO2 in the received gas stream is removed by the sorbent, wherein in the sorbent regenerator CO2 is removed from the loaded sorbent by one or more of a pressure swing, temperature swing, and combination thereof, and wherein the sorbent is in the form of a solid. 9. The system of claim 8, wherein bonds between the between adjacent sorbent components and between the sorbent and an adjacent sorbent substrate are stronger than bonds between the sorbent and the target gas and between the sorbent and the at least one acid gas and/or salt thereof and wherein the regeneration solution does not significantly impact the strengths of the bonds between the between adjacent sorbent components and between the sorbent and the adjacent sorbent substrate. 10. The system of claim 9, wherein the regeneration vessel is further configured, after contact of the lean sorbent with the regeneration solution, to contact the sorbent with a wash solution to remove any deposit on the sorbent after contact with the regeneration solution. 11. A system, comprising: a gas component separator configured to (a) receive a gas stream, the gas stream comprising a target gas component and at least one acid gas, the at least one acid gas being different from the target gas component, and (b) contact the gas stream with a sorbent to remove at least a portion of the target gas component and a portion of the at least one acid gas to form a purified gas stream and a loaded sorbent comprising the removed target gas and the removed acid gas;a sorbent regenerator configured to remove at least most of the removed target gas component from the loaded sorbent to form a lean sorbent comprising at least most of the removed one acid gas and/or a salt thereof;a regeneration vessel configured to contact the lean sorbent with a regeneration solution to remove at least most of the removed acid gas and/or a salt thereof and form, for recycle to the gas component separator, the sorbent; anda controller comprising microprocessor readable and executable instructions stored on a non-transient and tangible computer readable medium that, when executed, determine a concentration of the target gas component and/or at least one acid gas in the received gas stream and/or purified gas stream and, when a determined relationship involving the determined concentration of the target gas component and/or at least one acid gas in the received gas stream and/or purified gas stream is deemed to exist, initiate regeneration of the loaded sorbent. 12. In a system to remove a target gas component from a gas stream, the gas stream comprising the target gas component and at least one acid gas and the at least one acid gas being different from the target gas component, by contacting the gas stream with a sorbent to remove at least a portion of the target gas component to form a purified gas stream and a target gas component loaded sorbent, the sorbent also removing a portion of the at least one acid gas, a tangible and non-transient computer readable medium comprising microprocessor readable and executable instructions that, when executed, perform operations comprising: determine a concentration of a target gas component and/or at least one acid gas in at least one of the gas stream and the purified gas stream and, when a determined relationship involving the determined concentration of the target gas component and/or at least one acid gas in the at least one of the gas stream and the purified gas stream is deemed to exist, cause the following sub-operations to be performed; removing at least most of the removed at least a portion of the target gas component from the loaded sorbent to form a lean sorbent, the lean sorbent comprising at least most of the removed portion of the at least one acid gas and/or a salt thereof; andcontacting the lean sorbent with a regeneration solution to remove at least most of the removed portion of the at least one acid gas and/or a salt thereof and form a fully treated sorbent for recycle. 13. The computer readable medium of claim 12, wherein the instructions, when executed, select between first and second operating modes of the system based on whether the determined relationship is deemed to exist, wherein in the first operating mode, the gas stream passes through a first gas component separator but not a second gas component separator, a first sorbent used by the first gas component separator is not regenerated, and a second sorbent used by the second gas component separator is undergoing regeneration and wherein in the second operating mode, the gas stream passes through the second gas component separator but not the first gas component separator, the second sorbent used by the second gas component separator is not regenerated, and the first sorbent used by the first gas component separator is undergoing regeneration. 14. The computer readable medium of claim 12, wherein the determined relationship estimates at least one of an in-use and unused sorption capacity of the sorbent. 15. The computer readable medium of claim 12, wherein the target gas component is a carbon oxide, wherein the at least one acid gas is one or more of a sulfur oxide, a nitrogen oxide and hydrogen sulfide, wherein the sorbent is an amine-base sorbent, and wherein the regeneration solution has a pH of at least about pH 10. 16. The computer readable medium of claim 15, wherein the acid gas comprises SO2, wherein the target gas component is CO2, wherein the regeneration solution comprises a base, wherein at least most of the CO2 in the received gas stream is removed by the sorbent, wherein in a sorbent regenerator CO2 is removed from the loaded sorbent by one or more of a pressure swing, temperature swing, and combination thereof, and wherein the sorbent is in the form of a solid. 17. The computer readable medium of claim 16, wherein bonds between the between adjacent sorbent components and between the sorbent component and an adjacent sorbent substrate are stronger than bonds between the sorbent component and the target gas component and between the sorbent component and the at least one acid gas and/or salt thereof and wherein the regeneration solution do not significantly impact the strengths of the bonds between the between adjacent sorbent components and between the sorbent component and an adjacent sorbent substrate. 18. The computer readable medium of claim 17, wherein the regeneration solution is contacted with the lean sorbent in a regeneration vessel, wherein the regeneration vessel is further configured, after contact of the lean sorbent with the regeneration solution, to contact the sorbent with a wash solution to remove any deposit on the sorbent after contact with the regeneration solution.