US4292285A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for removing compounds with offensive odor from a gas containing the same
Assignee: Taiyo Kaken Co Ltd
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Filing: 1979-12-10
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Granted: 1981-09-29
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Expires: 1999-12-10
Abstract
Abstract A method for removing compounds with offensive odor from an exhaust gas containing the same with a deodorant comprising a mixture of spherical particles of activated carbon and spherical particles of porous carbon impregnated with phosphoric acid or ammonium phosphate placed in a fluidized-bed type deodorizing unit.
Inventors
- 👤 Masaaki Nakao
- 👤 Zenya Shiiki
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 21:45
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
349 words
In the method of removing basic compounds and other compounds with offensive odor from a large amount of a flowing exhaust gas containing the same at a low concentration by bringing said gas into contact with particles of activated carbon, the improvement comprising: using a mixture of (1) particles of activated carbon having a value of compression strength of 500 to 1,500 g/cm 2 and (2) particles of porous carbon impregnated with an amount of 1-50% by weight of phosphoric acid or ammonium phosphate or mixtures thereof, said particles of activated carbon being prepared by (a) mixing a pitch of softening point of 50° to 350° C., of a carbon content of 80 to 97%, of a ratio of hydrogen to carbon of 0.3 to 2.5 and of a nitrobenzene-insoluble fraction of less than 60% by weight with at least one aromatic hydrocarbon, (b) forming the mixture into substantially spherical particulate shape, (c) immersing the thus formed spherical particles into a solvent in which said pitch is hardly soluble but said aromatic hydrocarbon is easily soluble thereby extracting said aromatic hydrocarbon from said spherical particles of pitch, (d) oxidizing the extracted particles at a temperature of from room temperature to 400° C. with an oxidant thereby forming infusible pitch particles, (e) carbonizing the pitch particles thus made infusible in an inert atmosphere at a temperature higher than 600° C., and (f) activating said carbonized particles with steam; controlling the humidity of said exhaust gas; bringing said controlled exhaust gas into countercurrent contact in a fluidized bed with said mixture of particles of activated carbon and particles of porous carbon impregnated with phosphoric acid or ammonium phosphate or mixtures thereof at a temperature of lower than 100° C. thereby removing from said exhaust gas said compounds with offensive odor; heating said mixture after said countercurrent contact with said exhaust gas together with steam thereby expelling said compounds with offensive odor as condensed gaseous matter from said mixture and also regenerating the adsorbing capability of said mixture of particles; and recycling the thus regenerated mixture into said step of countercurrent contact.
Claim 2
Dependent Claim
349 words
In the method of removing basic compounds and other compounds with offensive odor from a large amount of a flowing exhaust gas containing the same at a low concentration by bringing said gas into contact with particles of activated carbon, the improvement comprising: using a mixture of (1) particles of activated carbon having a value of compression strength of 500 to 1,500 g/cm 2 and (2) particles of porous carbon impregnated with an amount of 1-50% by weight of phosphoric acid or ammonium phosphate or mixtures thereof, said particles of activated carbon being prepared by (a) mixing a pitch of softening point of 50° to 350° C., of a carbon content of 80 to 97%, of a ratio of hydrogen to carbon of 0.3 to 2.5 and of a nitrobenzene-insoluble fraction of less than 60% by weight with at least one aromatic hydrocarbon, (b) forming the mixture into substantially spherical particulate shape, (c) immersing the thus formed spherical particles into a solvent in which said pitch is hardly soluble but said aromatic hydrocarbon is easily soluble thereby extracting said aromatic hydrocarbon from said spherical particles of pitch, (d) oxidizing the extracted particles at a temperature of from room temperature to 400° C. with an oxidant thereby forming infusible pitch particles, (e) carbonizing the pitch particles thus made infusible in an inert atmosphere at a temperature higher than 600° C., and (f) activating said carbonized particles with steam; controlling the humidity of said exhaust gas; bringing said controlled exhaust gas into countercurrent contact in a fluidized bed with said mixture of particles of activated carbon and particles of porous carbon impregnated with phosphoric acid or ammonium phosphate or mixtures thereof at a temperature of lower than 100° C. thereby removing from said exhaust gas said compounds with offensive odor; heating said mixture after said countercurrent contact with said exhaust gas together with steam thereby expelling said compounds with offensive odor as condensed gaseous matter from said mixture and also regenerating the adsorbing capability of said mixture of particles; and recycling the thus regenerated mixture into said step of countercurrent contact.
Claim 3
Dependent Claim
41 words
The method according to claim 1, wherein said mixture comprises one part by weight of said spherical particles of porous carbon impregnated with phosphoric acid and/or ammonium phosphate, 0 to 5 parts by weight of said spherical particles of activated carbon.
Claim 4
Dependent Claim
41 words
The method according to claim 2, wherein said mixture comprises one part by weight of said spherical particles of activated carbon and one to two parts by weight of said particles of porous carbon impregnated with phosphoric acid and/or ammonium phosphate.
Claim 5
Dependent Claim
21 words
The method according to claim 1, wherein said spherical particles of activated carbon are of 0.2 to 2.0 mm in diameter.
Claim 6
Dependent Claim
25 words
The method according to claim 1, wherein said steam used for regenerating step is a superheated steam at a temperature of 100° to 500° C.
Claim 7
Dependent Claim
19 words
The method according to claim 5, wherein said superheated steam is at a temperature of 150° to 300° C.
Claim 8
Dependent Claim
21 words
The method according to claim 1, wherein said controlled exhaust gas has a value of humidity of 40 to 90% R.H.
Claim 9
Dependent Claim
21 words
The method according to claim 1, wherein said particles of porous carbon are impregnated with 10-25% by weight of phosphoric acid.
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) | 1984-09-28 | 1985-03-30 | 1985-09-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-09-28 | 1989-03-30 | 1989-09-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-09-28 | 1993-03-30 | 1993-09-29 | $7700.00 | Window Closed / Lapsed |