US2005178303A1PendingUtilityA1
Method for in-furnace reduction and control of sulfur trioxide
Priority: Feb 14, 2004Filed: Mar 10, 2004Published: Aug 18, 2005
Est. expiryFeb 14, 2024(expired)· nominal 20-yr term from priority
Inventors:Brian S. Higgins
F23C 6/04F23C 2900/06041
40
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Claims
Abstract
A method for controlling SO 3 in a combustion process of a sulfur-containing fuel, the method steps including partially combusting the fuel to create a reducing environment; maintaining the reducing environment for a sufficient period such that SO 3 is reduced to SO 2 to achieve a desirable level of SO 3 ; and combusting the remainder of the fuel in an oxidizing environment; thereby reducing the conversion of levels of SO 3 in the flue gases.
Claims
exact text as granted — not AI-modified1 . A method for reducing SO 3 in a combustion process of a sulfur-containing fuel, the method steps comprising:
a) partially combusting the fuel in a first stage to create a reducing environment; b) maintaining the reducing environment for a sufficient time period such that SO 3 is reduced to SO 2 to achieve a desirable level of SO 3 ; c) combusting the remainder of the fuel and combustion intermediates in a second stage with oxidizing environment; thereby reducing the levels of SO 3 in the flue gases.
2 . The method of claim 1 , further including the step of micro-staging the first stage fuel combustion.
3 . The method of claim 2 , wherein the micro-staging is provided through the use of low-NOx burners.
4 . The method of claim 1 , further including the step of macro-staging the first stage of fuel combustion.
5 . The method of claim 4 , wherein the macro-staging is provided through the use of over-fired air.
6 . The method of claim 1 , further including a combination of micro-staging and macro-staging.
7 . The method of claim 6 , wherein the micro-staging is provided by low-NOx burners and the macro-staging is provided by over-fired air.
8 . The method of claim 1 , wherein the fuel is coal.
9 . A combustion furnace operated with a method for controlling SO 3 in a combustion process of a sulfur-containing fuel, the method steps comprising:
a) partially combusting the fuel to create a reducing environment; b) maintaining the reducing environment for a sufficient period such that SO 3 is reduced to SO 2 to achieve a desirable level of SO 3 ; c) combusting the remainder of the fuel in an oxidizing environment; thereby reducing the conversion of levels of SO 3 in the flue gases.
10 . The method of claim 9 , further including the step of micro-staging the first stage fuel combustion.
11 . The method of claim 10 , wherein the micro-staging is provided through the use of low-NOx burners.
12 . The method of claim 9 , further including the step of macro-staging the first stage of fuel combustion.
13 . The method of claim 12 , wherein the macro-staging is provided through the use of over-fired air.
14 . The method of claim 9 , further including a combination of micro-staging and macro-staging.
15 . The method of claim 14 , wherein the micro-staging is provided by low-NOx burners and the macro-staging is provided by over-fired air.
16 . The method of claim 9 , wherein the fuel is coal
17 . A method for controlling SO 3 concentrations in a combustion process of a sulfur-containing fuel, the method steps comprising:
a) partially combusting the fuel in a first stage to create a reducing environment; b) adjusting the reducing environment time period such that SO 3 is preferentially reduced to SO 2 to achieve a desirable level of SO 3 ; c) combusting the remainder of the fuel and combustion intermediates in a second stage with oxidizing environment; thereby controlling the levels of SO 3 in the flue gases.
18 . The method of claim 17 , further including the step of micro-staging the first stage fuel combustion.
19 . The method of claim 18 , wherein the micro-staging is provided through the use of low-NOx burners.
20 . The method of claim 17 , further including the step of macro-staging the first stage of fuel combustion.
21 . The method of claim 20 , wherein the macro-staging is provided through the use of over-fired air.
22 . The method of claim 17 , further including a combination of micro-staging and macro-staging.
23 . The method of claim 22 , wherein the micro-staging is provided by low-NOx burners and the macro-staging is provided by over-fired air.
24 . The method of claim 17 , wherein the fuel is coal.Join the waitlist — get patent alerts
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