Exhaust gas treatment system for an ammonia-containing exhaust gas
A method and exhaust gas treatment system for treating an ammonia-containing exhaust gas, for example a livestock house exhaust gas. The exhaust gas treatment system comprises a plurality of sorbent beds comprising a copper-doped small-pore zeolite, a valve system configured to establish independently for each sorbent bed fluid communication in a first or second configuration, wherein in the first configuration a flow of ammonia-containing exhaust gas contacts the sorbent bed at a temperature of less than 50° C. for storing the ammonia; and in the second configuration a flow of heated gas maintains the sorbent bed at a temperature of at least 300° C. for releasing and treating the ammonia in situ.
1. A method of treating an ammonia-containing exhaust gas, the method comprising:
(i) providing an exhaust gas treatment system for the treatment of an ammonia-containing exhaust gas, the exhaust gas treatment system comprising:
a first gas inlet for providing a flow of ammonia-containing exhaust gas;
a second gas inlet for providing a flow of heated gas;
a plurality of sorbent beds comprising a copper-doped small-pore zeolite;
an exhaust gas outlet; and
a valve system configured to establish independently for each sorbent bed fluid communication in a first or second configuration, wherein:
i) in the first configuration a flow of ammonia-containing exhaust gas from the first gas inlet contacts the sorbent bed at a temperature of less than 50° C. for storing the ammonia and then passes to the exhaust gas outlet; and
ii) in the second configuration a flow of heated gas from the second gas inlet contacts the sorbent bed and then passes to the exhaust gas outlet, wherein the flow of heated gas maintains the sorbent bed at a temperature of at least 300° C.;
wherein the valve system is configured to ensure that at least one sorbent bed is in the first configuration,
and wherein, the exhaust gas treatment system comprises a control module for controlling the valve system and the flow of heated gas, the control module having an operation mode configured to heat each sorbent bed to the temperature of at least 300° C. with a heating profile reaching 200° C. in 60 minutes or less when switching each sorbent bed from the first configuration to the second configuration,
wherein the method comprises:
(i) contacting one or more sorbent beds, each in the first configuration, with a flow of ammonia-containing exhaust gas at a temperature of less than 50° C., thereby storing the ammonia; and
(ii) intermittently switching at least one sorbent bed from the first configuration to the second configuration to heat the sorbent bed to the temperature of at least 300° C. with a heating profile reaching 200° C. in 60 minutes or less, wherein at least one sorbent bed is in kept in the first configuration.
2. The method according to claim 1 wherein the copper-doped small-pore zeolite has a CHA or AEI-type framework structure.
3. The method according to claim 1 , wherein the exhaust gas treatment system further comprises a dehumidifier, and wherein the flow of ammonia-containing exhaust gas from the first gas inlet is treated by the dehumidifier before it contacts each sorbent bed in the first configuration.
4. The method according to claim 1 , wherein the copper-doped small-pore zeolite is doped with copper in an amount of from 1 to 6 wt %.
5. The method according to claim 1 , wherein the exhaust gas treatment system comprises only two sorbent beds.
6. The method according to claim 1 , wherein the flow of heated gas maintains the sorbent bed at a temperature of at least 350° C.
7. The method according to claim 1 , wherein the flow of ammonia-containing exhaust gas from the first gas inlet contacts the sorbent bed at a temperature of from 10° C. to 30° C.
8. The method according to claim 7 , wherein the ammonia-containing exhaust gas is a livestock house exhaust gas.
9. The method according to claim 1 , wherein the flow of heated gas is heated by a hydrocarbon gas burner.
10. The method according to claim 1 wherein the exhaust gas treatment system further comprises one or more material filters and wherein the ammonia-containing exhaust gas is filtered before contacting the sorbent beds.
11. The method according to claim 1 wherein the exhaust gas treatment system further comprises a contaminant sorbent material upstream of the plurality of sorbent beds, wherein the contaminant is selected from one or more of As, SO 2 , SO 3 , H 2 S, Hg and Cl, wherein the ammonia-containing exhaust gas is treated with the contaminant sorbent material before contacting the sorbent beds.
12. The method according to claim 1 wherein the exhaust gas treatment system further comprises one or more ammonia sensors in communication with each sorbent bed to determine an ammonia loading status for establishing when the control module should reconfigure the valve system.
13. The method according to claim 1 , wherein the valve system is further configured to establish, independently for each sorbent bed, fluid communication in a third configuration, wherein:
(iii) in the third configuration for cooling of the sorbent bed gases are prevented from leaving the sorbent bed until it is at a temperature below 50° C.
14. The method according to claim 1 , wherein:
(i) the heating profile reaches 300° C. from 200° C. in less than 30 minutes and/or
(ii) the heating profile reaches 200° C. in less than 10 minutes.
15. An exhaust gas treatment system for the treatment of an ammonia-containing exhaust gas, the exhaust gas treatment system comprising:
a first gas inlet for providing a flow of ammonia-containing exhaust gas;
a second gas inlet for providing a flow of heated gas;
a plurality of sorbent beds comprising a copper-doped small-pore zeolite;
an exhaust gas outlet; and
a valve system configured to establish independently for each sorbent bed fluid communication in a first or second configuration, wherein:
i) in the first configuration a flow of ammonia-containing exhaust gas from the first gas inlet contacts the sorbent bed at a temperature of less than 50° C. for storing the ammonia and then passes to the exhaust gas outlet; and
ii) in the second configuration a flow of heated gas from the second gas inlet contacts the sorbent bed and then passes to the exhaust gas outlet, wherein the flow of heated gas maintains the sorbent bed at a temperature of at least 300° C.;
wherein the valve system is configured to ensure that at least one sorbent bed is in the first configuration,
and wherein, the exhaust gas treatment system comprises a control module for controlling the valve system and the flow of heated gas, the control module having an operation mode configured to heat each sorbent bed to the temperature of at least 300° C. with a heating profile reaching 200° C. in 60 minutes or less when switching each sorbent bed from the first configuration to the second configuration.
16. The exhaust gas treatment system according to claim 15 , wherein the copper-doped small-pore zeolite has a CHA or AEI-type framework structure.
17. The exhaust gas treatment system according to claim 15 , wherein the exhaust gas treatment system is for performing the method according to claim 1 .
18. A livestock house, HVAC installation, waste water treatment plant, or a mine, comprising the exhaust gas treatment system according to claim 15 .