US4726940A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of purifying exhaust gas
Assignee: Kanadevia Corp
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Filing: 1986-05-21
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Granted: 1988-02-23
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Expires: 2006-05-21
Abstract
Abstract A method of purifying an exhaust gas characterized by dispersing individually independent fine particles of a Ca-containing absorbent in a carrier gas to a high concentration by a dividing-dispersing device to which the carrier gas and the absorbent are supplied, the absorbent being up to 10 microns in mean particle diameter, introducing the resulting aerosol of high concentration into the exhaust gas to uniformly mix the aerosol with the exhaust gas and thereafter introducing the exhaust gas into a dust collector, whereby the fine particles of absorbent having absorbed harmful acid substances from the exhaust gas are removed together with dust and soot. The absorbent forming secondary agglomerates before reaching the dividing-dispersing device are divided into individually independent primary particles and then dispersed in the carrier gas by the device, so that when introduced into the exhaust gas, the absorbent reacts with the harmful acid substance over an increased area of contact to achieve an improved removal efficiency.
Inventors
- 👤 Yoshio Kobayashi
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 21:21
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/68
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
165 words
A method of purifying an exhaust gas which contains HCl flowing through an exhaust gas passage comprising; preparing an aerosol by dispersing substantially individually independent fine particles of Ca-containing absorbent, which have a mean particle size of up to 5 microns, at a high concentration of 50 to 500 g/Nm 3 in a carrier gas flowing at a high speed of several tens to 300 m/s to entrain therein the absorbent; introducing the aerosol of the said carrier gas and absorbent into the exhaust gas passage and uniformly mixing the aerosol with the exhaust gas which contains the HCl and has a temperature range of 150° to 400° C., the introduction and mixing being conducted so that the individual absorbent particles do not agglomerate during the transfer into the exhaust passage and the absorbent particles concentrate at 1 to 20 g/Nm 3 in the exhaust gas; thereafter removing the absorbent particles, which have absorbed the HCl, together with dust and soot, from the exhaust gas.
Claim 2
Independent Claim
165 words
A method of purifying an exhaust gas which contains HCl flowing through an exhaust gas passage comprising; preparing an aerosol by dispersing substantially individually independent fine particles of Ca-containing absorbent, which have a mean particle size of up to 5 microns, at a high concentration of 50 to 500 g/Nm 3 in a carrier gas flowing at a high speed of several tens to 300 m/s to entrain therein the absorbent; introducing the aerosol of the said carrier gas and absorbent into the exhaust gas passage and uniformly mixing the aerosol with the exhaust gas which contains the HCl and has a temperature range of 150° to 400° C., the introduction and mixing being conducted so that the individual absorbent particles do not agglomerate during the transfer into the exhaust passage and the absorbent particles concentrate at 1 to 20 g/Nm 3 in the exhaust gas; thereafter removing the absorbent particles, which have absorbed the HCl, together with dust and soot, from the exhaust gas.
Claim 3
Dependent Claim
31 words
A method as defined in claim 1 wherein the Ca-containing absorbent is at least one member selected from the group consisting of quick lime, slaked lime, calcined dolomite and slaked dolomite.
Claim 4
Independent Claim
168 words
A method of purifying an exhaust gas which contains SO x flowing through an exhaust gas passage comprising; preparing an aerosol by dispersing substantially individually independent fine particles of Ca-containing absorbent, which have a mean particle size of 1 to 3 microns, at a high concentration of 50 to 500 g/Nm 3 in a carrier gas flowing at a high speed of several tens to 300 m/s to entrain therein the absorbent; introducing the aerosol of the said carrier gas and absorbent into the exhaust gas passage and uniformly mixing the aerosol with the exhaust gas which contains the SO x and has a temperature range of 900° to 1200° C., the introduction and mixing being conducted so that the individual absorbent particles do not agglomerate during transfer into the exhaust passage and the absorbent particles concentrate at 1 to 20 g/Nm 3 in the exhaust gas; thereafter removing the absorbent particles, which have absorbed the SO x , together with dust and soot, from the exhaust gas.
Claim 5
Independent Claim
168 words
A method of purifying an exhaust gas which contains SO x flowing through an exhaust gas passage comprising; preparing an aerosol by dispersing substantially individually independent fine particles of Ca-containing absorbent, which have a mean particle size of 1 to 3 microns, at a high concentration of 50 to 500 g/Nm 3 in a carrier gas flowing at a high speed of several tens to 300 m/s to entrain therein the absorbent; introducing the aerosol of the said carrier gas and absorbent into the exhaust gas passage and uniformly mixing the aerosol with the exhaust gas which contains the SO x and has a temperature range of 900° to 1200° C., the introduction and mixing being conducted so that the individual absorbent particles do not agglomerate during transfer into the exhaust passage and the absorbent particles concentrate at 1 to 20 g/Nm 3 in the exhaust gas; thereafter removing the absorbent particles, which have absorbed the SO x , together with dust and soot, from the exhaust gas.
Claim 6
Dependent Claim
33 words
A method as defined in claim 3 wherein the Ca-containing absorbent is at least one member selected from the group consisting of limestone, quick lime, slaked lime, dolomite, calcined dolomite and slaked dolomite.
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) | 1991-02-22 | 1991-08-24 | 1992-02-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-02-22 | 1995-08-24 | 1996-02-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-02-22 | 1999-08-24 | 2000-02-23 | $7700.00 | Window Closed / Lapsed |