US4872887A
Expired / Lapsed
US
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Method for flue gas conditioning with the decomposition products of ammonium sulfate or ammonium bisulfate
Assignee: Electric Power Research Institute
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Filing: 1988-09-12
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Granted: 1989-10-10
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Expires: 2008-09-12
Abstract
Abstract A method is provided for enhancing the efficiency of fly ash collection in an electrostatic precipitator by lowering the resistivity of the fly ash particles in the flue gas, comprising the steps of introducing an aqueous solution of ammonium sulfate or ammonium bisulfate into a slipstream of hot flue gas or hot combustion air in a chamber external to the main flue gas duct wherein thermal decomposition is effected, removing the NH3 decomposition product by catalytic oxidation to increase the effectiveness of the SO3 decomposition product, and then distributing the SO3 decomposition product into the main flue gas stream exiting from the air preheater at a point upstream from the electrostatic precipitator.
Inventors
- 👤 Ralph F. Altman
- 👤 John P. Gooch
- 👤 Edward B. Dismukes
- 👤 Edward C. Landham, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 12:44
CPC Classifications
B; B03; B03C; B03C3/00; B03C3/017; B03C3/01; B03C3/013
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
218 words
A method for conditioning flue gas containing suspended fly ash, comprising the steps of: (a) diverting a slipstream of flue gas from a main flue gas stream at a point upstream from an air preheater located directly upstream of an electrostatic precipitator where the temperature of said main flue gas stream is in the range of about 700° F. to 900° F., said diverted stream thereby having a temperature in the range of from about 700° F. to 900° F.; (b) introducing an aqueous solution of ammonium sulfate or ammonium bisulfate into said diverted flue gas slipstream thereby effecting thermal decomposition of said ammonium sulfate or bisulfate into its gaseous thermal decomposition products which include sulfur trioxide and ammonia; (c) flowing said gaseous thermal decomposition products through a catalyst capable of oxidizing NH 3 with O 2 to produce N 2 and H 2 O and suppressing the reaction whereby NH 3 and SO 3 interact by an oxidation-reduction process to produce N 2 , SO 2 and H 2 O; (d) then returning said diverted flue gas slipstream to said main flue gas stream at a point between said air preheater and said electrostatic precipitator thereby distributing said gaseous thermal decomposition products into said main flue gas stream flowing between said air preheater and said electrostatic precipitator.
Claim 2
Independent Claim
218 words
A method for conditioning flue gas containing suspended fly ash, comprising the steps of: (a) diverting a slipstream of flue gas from a main flue gas stream at a point upstream from an air preheater located directly upstream of an electrostatic precipitator where the temperature of said main flue gas stream is in the range of about 700° F. to 900° F., said diverted stream thereby having a temperature in the range of from about 700° F. to 900° F.; (b) introducing an aqueous solution of ammonium sulfate or ammonium bisulfate into said diverted flue gas slipstream thereby effecting thermal decomposition of said ammonium sulfate or bisulfate into its gaseous thermal decomposition products which include sulfur trioxide and ammonia; (c) flowing said gaseous thermal decomposition products through a catalyst capable of oxidizing NH 3 with O 2 to produce N 2 and H 2 O and suppressing the reaction whereby NH 3 and SO 3 interact by an oxidation-reduction process to produce N 2 , SO 2 and H 2 O; (d) then returning said diverted flue gas slipstream to said main flue gas stream at a point between said air preheater and said electrostatic precipitator thereby distributing said gaseous thermal decomposition products into said main flue gas stream flowing between said air preheater and said electrostatic precipitator.
Claim 3
Dependent Claim
34 words
A method according to claim 1, wherein said slipstream of flue gas containing said thermal decomposition products is directed to flow downwardly through said catalyst to prevent collection of fly ash in said catalyst.
Claim 4
Independent Claim
227 words
A method for conditioning flue gas containing suspended fly ash, comprising the steps of: (a) diverting a slipstream of combustion air from a main combustion air stream exiting the hot side of an air preheater after having passed through said preheater where the temperature of said main combustion air stream is in the range of about 700° F. to 900° F., said diverted combustion air slipstream thereby having a temperature in the range of from about 700° F. to 900° F.; (b) introducing an aqueous solution of ammonium sulfate or ammonium bisulfate into said diverted slipstream of combustion air, thereby effecting thermal decomposition of said ammonium sulfate or bisulfate into its gaseous thermal decomposition products which includes sulfur trioxide and ammonia; (c) flowing said gaseous thermal decomposition products through a catalyst capable of oxidizing NH 3 with O 2 to produce N 2 and H 2 O and suppressing other reactions whereby NH 3 and SO 3 interact by an oxidation-reduction process to produce N 2 , SO 2 and H 2 O; and (d) introducing said diverted slipstream of combustion air into a main flue gas stream at a point between said air preheater and an electrostatic precipitator located directly downstream of said air preheater, thereby distributing said gaseous thermal decomposition products into said main flue gas stream between said air preheater and said electrostatic precipitator.
Claim 5
Independent Claim
227 words
A method for conditioning flue gas containing suspended fly ash, comprising the steps of: (a) diverting a slipstream of combustion air from a main combustion air stream exiting the hot side of an air preheater after having passed through said preheater where the temperature of said main combustion air stream is in the range of about 700° F. to 900° F., said diverted combustion air slipstream thereby having a temperature in the range of from about 700° F. to 900° F.; (b) introducing an aqueous solution of ammonium sulfate or ammonium bisulfate into said diverted slipstream of combustion air, thereby effecting thermal decomposition of said ammonium sulfate or bisulfate into its gaseous thermal decomposition products which includes sulfur trioxide and ammonia; (c) flowing said gaseous thermal decomposition products through a catalyst capable of oxidizing NH 3 with O 2 to produce N 2 and H 2 O and suppressing other reactions whereby NH 3 and SO 3 interact by an oxidation-reduction process to produce N 2 , SO 2 and H 2 O; and (d) introducing said diverted slipstream of combustion air into a main flue gas stream at a point between said air preheater and an electrostatic precipitator located directly downstream of said air preheater, thereby distributing said gaseous thermal decomposition products into said main flue gas stream between said air preheater and said electrostatic precipitator.
Claim 6
Dependent Claim
24 words
A method according to claim 1 or 3, wherein said decomposition products from steps (b) and (c) are transported through a thermally insulated duct.
Claim 7
Dependent Claim
24 words
A method according to claim 1 or 3, wherein said decomposition products are distributed into said main flue gas stream through a distribution manifold.
Claim 8
Dependent Claim
26 words
A method according to claim 1 or 3, wherein said aqueous solution of ammonium sulfate contains from about 5 to 45% by weight of ammonium sulfate.
Claim 9
Dependent Claim
26 words
A method according to claim 1 or 3, wherein said aqueous solution of ammonium bisulfate contains from about 5 to 80% by weight of ammonium bisulfate.
Claim 10
Dependent Claim
60 words
A method according to claim 1 or 3, wherein said aqueous salt solution is sprayed at a rate sufficient to produce a sulfur trioxide concentration from about 250 to 2500 ppm by volume and said sulfur trioxide is then distributed into the main stream of flue gas to produce a concentration therein from about 2.5 to 25 ppm by volume.
Claim 11
Dependent Claim
31 words
A method according to claim 1 or 3, wherein said catalyst comprises a mixture of V 2 O 5 , K 2 O, and SO 3 on an SiO 2 support.
Claim 12
Dependent Claim
17 words
A method according to claim 1 or 3, wherein said catalyst is in the form of pellets.
Claim 13
Dependent Claim
18 words
A method according to claim 1 or 3, wherein said catalyst is in the form of hollow tubes.
Claim 14
Dependent Claim
34 words
A method according to claim 1 or 3, wherein said catalyst is applied to a parallel-passage support having individual channels formed in a solid piece of the substrate to which said catalyst is applied.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-10-09 | 1993-04-10 | 1993-10-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-10-09 | 1997-04-10 | 1997-10-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-10-09 | 2001-04-10 | 2001-10-10 | $7700.00 | Window Closed / Lapsed |