US4226831A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus for removal of sulfur from gas
Assignee: Allis Chalmers Corp
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Filing: 1979-03-16
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Granted: 1980-10-07
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Expires: 1999-03-16
Abstract
Abstract Emission gas to be scrubbed of sulfur dioxide or the like has turbulent lengthwise flow through an elongated mixing vessel. At a mixing zone in the vessel, near where said gas enters it, finely comminuted lime (Blaine Number preferably 6000 before calcining) is fed into the gas and carried out of the vessel with the gas to a cyclone separator. From the cyclone the gas passes to a baghouse at which residual lime is removed from it and it is released. A minor portion of the lime separated at the cyclone is sent to waste; most is returned to the mixing zone for recycling. Make-up lime is fed to the mixing zone from a suspension calcining furnace, reaching the mixing zone while still heated. To maintain 650 DEG C. to 750 DEG C. at the mixing zone, recycled lime may be reheated in passing from the cyclone to that zone. The total of recycled and fresh lime fed to the mixing zone is at least nine times the quantity required for stoichiometric reaction with pollutant in the emission gas and can be 40 or more times that quantity.
Inventors
- 👤 Louis R. Dilworth
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 01:20
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
390 words
Apparatus for removing pollutant gases such as sulfur dioxide from emission gas to be released into the atmosphere, said apparatus comprising: A. a mixing vessel (5) having (1) an outlet (8), (2) an inlet zone (107) spaced from said outlet (8), and (3) inlet means (6, 7) communicating with the inlet zone (107) for admitting emission gas and pollutant adsorbing particulate medium into the inlet zone (107), with said inlet means being arranged to produce turbulent flow of the emission gas and the medium in the vessel (5); B. pollutant containing emission gas delivery means (9) connected to the inlet means (at 6) for supplying emission gas to the inlet zone (107) of vessel (5); C. pollutant adsorbing particulate medium feed means (25, 12, 13) connected to the inlet means (at 7) for supplying fresh pollutant adsorbing particulate medium to the inlet zone (107) of vessel (5); D. a gas cleaner (10) for separating particulate medium from emission gas, and having (1) an inlet (110) connected with the outlet (8) of the mixing vessel (5), (2) a gas outlet (210), and (3) a particulate medium outlet (310); E. suction means (32) connected to the gas outlet (210) of the gas cleaner (10) for drawing emission gas and medium from the inlet zone (107) through the vessel (5) and the vessel outlet (8) into the gas cleaner (10); F. recirculation means (16, 17) connecting the particulate medium outlet (310) of the gas cleaner (10) to the inlet zone (107) of the mixing vessel (5) to thereby define a particulate medium recirculating loop structure (16, 17, 5, 8, 10, 16); G. particulate medium discharge means (33, 34, 35) connected to the loop structure (16, 17, 5, 8, 10, 16) downstream of the particulate medium outlet (310) of the gas cleaner (10) and upstream of the inlet zone (107) of the vessel (5); and H. the medium feed means (25, 12, 13) including (1) a furnace (12) in which fresh particulate medium is heated to a temperature high enough to cause the medium to chemically react with and adsorb pollutant gas from the emission gas; and (2) medium transporting means (13) connecting the furnace (12) to the inlet zone (107) of the mixing vessel (5) to deliver fresh medium into said inlet zone (107) while the fresh medium is at substantially said temperature.
Claim 2
Dependent Claim
390 words
Apparatus for removing pollutant gases such as sulfur dioxide from emission gas to be released into the atmosphere, said apparatus comprising: A. a mixing vessel (5) having (1) an outlet (8), (2) an inlet zone (107) spaced from said outlet (8), and (3) inlet means (6, 7) communicating with the inlet zone (107) for admitting emission gas and pollutant adsorbing particulate medium into the inlet zone (107), with said inlet means being arranged to produce turbulent flow of the emission gas and the medium in the vessel (5); B. pollutant containing emission gas delivery means (9) connected to the inlet means (at 6) for supplying emission gas to the inlet zone (107) of vessel (5); C. pollutant adsorbing particulate medium feed means (25, 12, 13) connected to the inlet means (at 7) for supplying fresh pollutant adsorbing particulate medium to the inlet zone (107) of vessel (5); D. a gas cleaner (10) for separating particulate medium from emission gas, and having (1) an inlet (110) connected with the outlet (8) of the mixing vessel (5), (2) a gas outlet (210), and (3) a particulate medium outlet (310); E. suction means (32) connected to the gas outlet (210) of the gas cleaner (10) for drawing emission gas and medium from the inlet zone (107) through the vessel (5) and the vessel outlet (8) into the gas cleaner (10); F. recirculation means (16, 17) connecting the particulate medium outlet (310) of the gas cleaner (10) to the inlet zone (107) of the mixing vessel (5) to thereby define a particulate medium recirculating loop structure (16, 17, 5, 8, 10, 16); G. particulate medium discharge means (33, 34, 35) connected to the loop structure (16, 17, 5, 8, 10, 16) downstream of the particulate medium outlet (310) of the gas cleaner (10) and upstream of the inlet zone (107) of the vessel (5); and H. the medium feed means (25, 12, 13) including (1) a furnace (12) in which fresh particulate medium is heated to a temperature high enough to cause the medium to chemically react with and adsorb pollutant gas from the emission gas; and (2) medium transporting means (13) connecting the furnace (12) to the inlet zone (107) of the mixing vessel (5) to deliver fresh medium into said inlet zone (107) while the fresh medium is at substantially said temperature.
Claim 3
Dependent Claim
75 words
The apparatus of claim 1, further characterized by: (1) said furnace (12) being charged with a particulate medium having a substantial content of an alkali earth metal carbonate which is calcined by said temperature to which the medium is heated; and (2) said medium transporting means (13) is constructed and arranged to deliver freshly calcined medium into said zone (107) of the mixing vessel (5) while hot, to maintain said temperature at said zone (107).
Claim 4
Dependent Claim
61 words
The apparatus of claim 1 wherein said furnace (12) comprises (1) a substantially cylindrical suspension chamber (20) having a feed inlet (27) near one end thereof by which feed material is introduced into said chamber substantially tangentially for swirling flow within the chamber; and (2) a fuel burner (22) mounted in said chamber (20) and arranged to direct combusting fuel thereinto.
Claim 5
Dependent Claim
34 words
The apparatus of claim 3 wherein said fuel burner (22) is mounted substantially coaxially in said one end of said chamber (20) and is arranged to direct combusting fuel substantially axially into the same.
Claim 6
Dependent Claim
45 words
The apparatus of claim 1, further characterized by: said recirculation means (16, 17) including a suspension heater (15) by which the particulate medium moving towards said zone (107) from the gas cleaner (10) is reheated so that it enters said zone (107) at said temperature.
Claim 7
Dependent Claim
81 words
The apparatus of claim 1 wherein said particulate medium discharge means (33, 34, 35) includes a waste duct (33), a waste chamber (34) and a movable seal means (35) in said waste duct (33), spaced from said loop structure (16, 17, 5, 8, 10, 16), for obstructing the waste duct (33) to provide a gas seal thereacross and to cause accumulations of particulate medium to develop and to be passed towards said waste chamber (34) while said gas seal is maintained.
Claim 8
Dependent Claim
84 words
The apparatus of claim 1 wherein said mixing vessel (5) is vertically elongated and has said outlet (8) at its top, and wherein said inlet (6) for emission gas comprises an orifice at the bottom of the mixing vessel (5) that is of smaller diameter than the interior of the mixing vessel (5) so that particulate adsorbing medium entering said zone (107) is carried upwardly through the mixing vessel (5) by emission gas flowing turbulently from said orifice (at 6) to said outlet (8).
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-10-07 | 1984-04-07 | 1984-10-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-10-07 | 1988-04-07 | 1988-10-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-10-07 | 1992-04-07 | 1992-10-07 | $7700.00 | Window Closed / Lapsed |