Patent US4940569A successfully refreshed from Google Patents.
US4940569A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Sorbent and processes for removing nitrogen oxides, sulfur oxides and hydrogen sulfide from gas streams
Assignee: Noxso Corp
•
Filing: 1988-09-20
•
Granted: 1990-07-10
•
Expires: 2008-09-20
Abstract
Abstract Novel sorbents comprising (a) an alumina substrate having a pore volume between 0.4 and 0.8 cc/g, and (b) an alkali or alkaline earth component, for example, sodium carbonate, wherein the amount of the alkali or alkaline earth component is between 50 and 400 μg per m 2 of the substrate. The sorbents of the present invention are outstandingly effective for the removal of nitrogen oxides, sulfur oxides and hydrogen sulfide from waste gas streams.
Inventors
- 👤 Lewis G. Neal
- 👤 John L. Haslbeck
- 👤 Hsiaopin Tseng
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 22:29
CPC Classifications
B; B01; B01J; B01J20/00; B01J20/02; B01J20/06; B01J20/08; B01D; B01D53/00; B01D53/02; B01D53/06; B01D53/10; B01D53/12; B01D2251/00; B01D2251/60; B01D2251/604; B01D2253/00; B01D2253/10; B01D2253/104; B01D2253/25; B01D2253/30; B01D2253/302; B01D2253/306; B01D2253/308; B01D2257/00; B01D2257/30; B01D2257/302; B01D2257/304; B01D2257/40; B01D2257/404
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
209 words
A process for the removal of nitrogen oxides and sulfur oxides from a sorbent containing them, comprising: (a) removing said nitrogen oxides from a sorbent comprising: (i) a gamma alumina substrate having a surface area between 100 m 2 /g and 500 m 2 /g and a pore volume between 0.4 and 0.8 cc/g, said gamma alumina substrate having a bimodal pore size disribution comprising micropores and macropores, said micropores having an average pore diameter d 1 in the range of between 30 and 400 Angstroms and said macropores having an average pore diameter d 2 in the range of between 80 and 3000 Angstroms, (ii) an alkali metal component, said substrate impregnated with the alkali metal component and the amount of said alkali metal component being between 50 and 400 μg per m 2 of said substrate; by contacting said nitrogen oxides and sulfur oxides containing sorbent with a stream of air heated to a temperature of above 532° C. and carrying said removed oxides away in a hot air stream; and (b) subsequently, contacting said sulfur oxides containing sorbent with a regenerant stream of methane which reacts with the sorbed sulfur oxides to produce a stream of elemental sulfur and carrying said stream of elemental sulfur away.
Claim 2
Dependent Claim
209 words
A process for the removal of nitrogen oxides and sulfur oxides from a sorbent containing them, comprising: (a) removing said nitrogen oxides from a sorbent comprising: (i) a gamma alumina substrate having a surface area between 100 m 2 /g and 500 m 2 /g and a pore volume between 0.4 and 0.8 cc/g, said gamma alumina substrate having a bimodal pore size disribution comprising micropores and macropores, said micropores having an average pore diameter d 1 in the range of between 30 and 400 Angstroms and said macropores having an average pore diameter d 2 in the range of between 80 and 3000 Angstroms, (ii) an alkali metal component, said substrate impregnated with the alkali metal component and the amount of said alkali metal component being between 50 and 400 μg per m 2 of said substrate; by contacting said nitrogen oxides and sulfur oxides containing sorbent with a stream of air heated to a temperature of above 532° C. and carrying said removed oxides away in a hot air stream; and (b) subsequently, contacting said sulfur oxides containing sorbent with a regenerant stream of methane which reacts with the sorbed sulfur oxides to produce a stream of elemental sulfur and carrying said stream of elemental sulfur away.
Claim 3
Dependent Claim
159 words
A process for the removal of nitrogen oxides and sulfur oxides from a sorbent containing them, comprising: (a) removing said nitrogen oxides from a sorbent comprising: (i) a gamma alumina substrate having a surface area between 100 m 2 /g and 500 m 2 /g and a pore volume between 0.4 and 0.8 cc/g, and (ii) an alkali metal component, impregnated with said alkali metal component and said substrate the amount of said alkali metal component being between 150 and 250 μg per m 2 of said substrate; by contacting said nitrogen oxides and sulfur oxides containing sorbent with a stream of air heated to a temperature of above 532° C. and carrying said removed oxides away in a hot air stream; and (b) subsequently, contacting said sulfur oxides containing sorbent with a regenerant stream of methane which reacts with the sorbed sulfur oxides to produce a stream of elemental sulfur and carrying said stream of elemental sulfur away.
Claim 4
Dependent Claim
159 words
A process for the removal of nitrogen oxides and sulfur oxides from a sorbent containing them, comprising: (a) removing said nitrogen oxides from a sorbent comprising: (i) a gamma alumina substrate having a surface area between 100 m 2 /g and 500 m 2 /g and a pore volume between 0.4 and 0.8 cc/g, and (ii) an alkali metal component, impregnated with said alkali metal component and said substrate the amount of said alkali metal component being between 150 and 250 μg per m 2 of said substrate; by contacting said nitrogen oxides and sulfur oxides containing sorbent with a stream of air heated to a temperature of above 532° C. and carrying said removed oxides away in a hot air stream; and (b) subsequently, contacting said sulfur oxides containing sorbent with a regenerant stream of methane which reacts with the sorbed sulfur oxides to produce a stream of elemental sulfur and carrying said stream of elemental sulfur away.
Claim 5
Dependent Claim
40 words
Process according to claim 1 or 2 wherein said process further comprises: (c) subsequently, contacting said sorbent removed of said nitrogen oxides and said sulfur oxides with atmospheric air to reduce the temperature of said sorbent to about 120° C.
References Cited (Backward Citations)
CH88554A
Cited
US2684283A
Cited
US2992884A
Cited
US3065056A
Cited
US3260679A
Cited
US3291564A
Cited
US3382033A
Cited
US3411865A
Cited
US3398131A
Cited
US3492083A
Cited
US3498743A
Cited
US3410909A
Cited
GB1154009A
Cited
US3589863A
Cited
US3557025A
Cited
US3551093A
Cited
US3669617A
Cited
US3632314A
Cited
US3755556A
Cited
US3660032A
Cited
US3725531A
Cited
US3682585A
Cited
US3864450A
Cited
US3755535A
Cited
US3974096A
Cited
US4323544A
Cited
US4426365A
Cited
US3948809A
Cited
US3880618A
Cited
US3957952A
Cited
DE2419103A1
Cited
US4187282A
Cited
US4071436A
Cited
US4115515A
Cited
US4039650A
Cited
US4798711A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1993-07-09 | 1994-01-08 | 1994-07-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-07-09 | 1998-01-08 | 1998-07-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-07-09 | 2002-01-08 | 2002-07-10 | $7700.00 | Window Closed / Lapsed |