US4956162A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for removal of particulates and SO2 from combustion gases
Assignee: Electric Power Research Institute
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Filing: 1988-08-02
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Granted: 1990-09-11
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Expires: 2008-08-02
Abstract
Abstract This invention pertains to methods for removal of pollution from the exhaust gas stream of combustion sources. More particularly, the invention relates to an improved method of elimination of particulate matte, sulfur dioxide (SO 2 ) and volatile toxic materials from the flue gas of coal fired boilers, especially in large electric generating plants.
Inventors
- 👤 Wallace B. Smith
- 👤 Dan V. Giovanni
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 19:22
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508; B03; B03C; B03C3/00; B03C3/019; F; F23; F23J; F23J15/00; F23J15/006; F23J2215/00; F23J2215/20; F23J2217/00; F23J2217/10; F23J2217/102; F23J2219/00; F23J2219/60
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
119 words
A process for removing pollutants, including particulates and SO 2 , from coal fired boiler flue gases, said process comprising: electrostatically removing particulates from the flue gas: thereafter reducing the temperature of the flue gas to a temperature approaching the temperature for moisture saturation of the flue gas and being less than 135°F. and thereafter injecting dry calcium based sulfur reacting sorbent material into the flue gas in an amount at least sufficient to react with the SO 2 and SO 3 in the flue gas; and thereafter filtering the flue gas through a fabric filter to remove the reaction product of the sorbent material and SO 2 , as well as unreacted sorbent material, from the flue gas.
Claim 2
Dependent Claim
119 words
A process for removing pollutants, including particulates and SO 2 , from coal fired boiler flue gases, said process comprising: electrostatically removing particulates from the flue gas: thereafter reducing the temperature of the flue gas to a temperature approaching the temperature for moisture saturation of the flue gas and being less than 135°F. and thereafter injecting dry calcium based sulfur reacting sorbent material into the flue gas in an amount at least sufficient to react with the SO 2 and SO 3 in the flue gas; and thereafter filtering the flue gas through a fabric filter to remove the reaction product of the sorbent material and SO 2 , as well as unreacted sorbent material, from the flue gas.
Claim 3
Dependent Claim
16 words
A process of claim 1, wherein the flue gas temperature reduction is accomplished by heat exchange.
Claim 4
Dependent Claim
19 words
A process of claim 2, wherein the flue gas temperature reduction is accomplished by humidification of the flue gas.
Claim 5
Dependent Claim
22 words
A process of claim 7, including the further step of electrostatically enhancing the sorbent material just prior to the fabric filtering step.
Claim 6
Dependent Claim
127 words
A process for removing pollutants, including particulates and SO 2 , from coal fired boiler flue gases, said process comprising: electrostatically removing particulates from the flue gas; thereafter reducing the temperature of the flue gas to a temperature which is less than 135°F. and at least 5°F. above and less than 20 °F. above the temperature for moisture saturation of the flue gas, and injecting dry calcium based sulfur reacting sorbent material into the flue gas in an amount at least sufficient to react with SO 2 and SO 3 in the flue gas; and thereafter filtering the flue gas through a fabric filter to remove the reaction product of the sorbent material and SO 2 , as well as unreacted sorbent material, from the flue gas.
Claim 7
Dependent Claim
127 words
A process for removing pollutants, including particulates and SO 2 , from coal fired boiler flue gases, said process comprising: electrostatically removing particulates from the flue gas; thereafter reducing the temperature of the flue gas to a temperature which is less than 135°F. and at least 5°F. above and less than 20 °F. above the temperature for moisture saturation of the flue gas, and injecting dry calcium based sulfur reacting sorbent material into the flue gas in an amount at least sufficient to react with SO 2 and SO 3 in the flue gas; and thereafter filtering the flue gas through a fabric filter to remove the reaction product of the sorbent material and SO 2 , as well as unreacted sorbent material, from the flue gas.
Claim 8
Dependent Claim
224 words
A process for removing pollutants, including particulate material and SO 2 , from coal fired boiler flue gases, said process comprising (a) electrostatically removing particulates from the flue gas; (b) thereafter reducing the temperature of the flue gas to a temperature which is more than 20 °F. and less than 50 °F. above the temperature for moisture saturation of the flue gas; (c) thereafter passing the cooled flue gas to a fabric filter unit wherein the flue gas is filtered through a fabric filter to remove particulate material therefrom; (d) and injecting dry calcium based sulfur reacting sorbent material into the flue gas in or proximate the fabric filter unit in an amount at least sufficient to react with the SO 2 and SO 3 in the flue gas to form a particulate reaction product which can be separated in the fabric filter unit from the flue gas, wherein the temperature of the flue gas in the fabric filter unit is further reduced by the introduction of cooling air at a temperature at least 20 °F. less than the moisture saturation temperature of the flue gas into the fabric filter unit, or proximate the fabric filter unit, in an amount such as to reduce the temperature of the flue gas exiting the fabric filter unit to a temperature which is less than 135 °F.
Claim 9
Dependent Claim
224 words
A process for removing pollutants, including particulate material and SO 2 , from coal fired boiler flue gases, said process comprising (a) electrostatically removing particulates from the flue gas; (b) thereafter reducing the temperature of the flue gas to a temperature which is more than 20 °F. and less than 50 °F. above the temperature for moisture saturation of the flue gas; (c) thereafter passing the cooled flue gas to a fabric filter unit wherein the flue gas is filtered through a fabric filter to remove particulate material therefrom; (d) and injecting dry calcium based sulfur reacting sorbent material into the flue gas in or proximate the fabric filter unit in an amount at least sufficient to react with the SO 2 and SO 3 in the flue gas to form a particulate reaction product which can be separated in the fabric filter unit from the flue gas, wherein the temperature of the flue gas in the fabric filter unit is further reduced by the introduction of cooling air at a temperature at least 20 °F. less than the moisture saturation temperature of the flue gas into the fabric filter unit, or proximate the fabric filter unit, in an amount such as to reduce the temperature of the flue gas exiting the fabric filter unit to a temperature which is less than 135 °F.
Claim 10
Dependent Claim
26 words
Process of claim 6, wherein the temperature of the flue gas exiting the fabric filter is less than 15°F above the flue gas moisture saturation temperature.
Claim 11
Dependent Claim
25 words
Process of claim 6, wherein the temperature of the flue gas exiting the fabric filter is about 10 °F. above the flue gas saturation temperature.
References Cited (Backward Citations)
US4478810A
Cited
US4559211A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1993-09-10 | 1994-03-12 | 1994-09-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-09-10 | 1998-03-12 | 1998-09-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-09-10 | 2002-03-12 | 2002-09-11 | $7700.00 | Window Closed / Lapsed |