Patent US3907982A successfully refreshed from Google Patents.
US3907982A
Expired / Lapsed
US
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Calcining method for alumina
Assignee: Vista Chemical Co
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Filing: 1973-05-31
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Granted: 1975-09-23
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Expires: 1993-05-31
Abstract
Abstract Alumina having improved color characteristics and improved extrusion properties is produced by an improvement in the process for producing low-density, high-porosity, high-surface area alumina from an aqueous alumina slurry by contacting said aqueous alumina slurry with an effective amount of an organic solvent to form a solvent-aqueous alumina mixture; drying said mixture and recovering said low-density, high-porosity, high-surface area alumina; comprising drying said solvent-aqueous alumina mixture in an atmosphere containing at least 0.5 volume percent carbon dioxide.
Inventors
- 👤 Bruce E Leach
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 13:41
CPC Classifications
C; C01; C01F; C01F7/00; C01F7/02; C01F7/34; C01F7/36
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
229 words
IN A PROCESS FOR PRODUCING A LOW-DENSITY, HIGH-POROSITY, HIGH-SURFACE AREA PRODUCT ALUMINA FROM AN AQUEOUS ALUMINA SLURRY CONTAINING UP TO ABOUT 32 WEIGHT PERCENT AL2O3 AND PRODUCED BY: A. HYDROLYZING ALUMINUM ALKOXIDES WITH AN EFFECTIVE AMOUNT OF WATER TO FORM AN ORGANIC REACTION PRODUCT AND AN AQUEOUS ALUMINA SLURRY, AND, B. THEREAFTER SEPARATING THE AQUEOUS ALUMINA SLURRY FROM THE ORGANIC REACTION PRODUCT, WHEREIN SAID AQUEOUS ALUMINA SLURRY IS CONTACTED WITH AN ORGANIC SOLVENT SELECTED FROM THE GROUP CONSISTING OF ETHANOL, PROPANOL, ISOPROPANOL, BUTANOL, ISOBUTANOL AND TERTIARY BUTANOL IN AN AMOUNT SUFFICIENT TO PRODUCE A PRODUCT ALUMINA HAVING A LOOSE BULK DENSITY FROM ABOUT 7.5 TO ABOUT 25 LB/FT3, A SURFACE AREA FROM ABOUT 275 TO ABOUT 400 M2/G AND A PORE VOLUME FROM ABOUT 1 TO ABOUT 2.75 CC/G, TO FORM A SOLVENTAQUEOUS ALUMINA MIXTURE, SAID MIXTURE IS DRIED AND SAID DRIED ALUMINA IS CALCINED AND SAID PRODUCT ALUMINA IS RECOVERED, THE IMPROVEMENT COMPRISING CALCINING SAID DRIED ALUMINA AT A TEMPERATURE IN EXCESS OF 350*F IN AN ATMOSPHERE CONTAINING FROM ABOUT 1.0 TO ABOUT 20.0 VOLUME PERCENT CARBON DIOXIDE IN MIXTURE WITH GASES SELECTED FROM THE GROUP CONSISTING OF AIR, NITROGEN, ARGON, HELIUM, HYDROGEN, CARBON MONOXIDE, SUPERHEATED STEAM, AND MIXTURES OF SUPERHEATED STEAM AND HYDROCARBON COMPOUNDS CONTAINING UP TO ABOUT 30 CARBON ATOMS AND MIXTURES THEREOF AND RECOVERING SAID PRODUCT ALUMINA, SAID PRODUCT ALUMINA BEING SUBSTANTIALLY WHITE AND EXTRUDABLE.
Claim 2
Dependent Claim
229 words
IN A PROCESS FOR PRODUCING A LOW-DENSITY, HIGH-POROSITY, HIGH-SURFACE AREA PRODUCT ALUMINA FROM AN AQUEOUS ALUMINA SLURRY CONTAINING UP TO ABOUT 32 WEIGHT PERCENT AL2O3 AND PRODUCED BY: A. HYDROLYZING ALUMINUM ALKOXIDES WITH AN EFFECTIVE AMOUNT OF WATER TO FORM AN ORGANIC REACTION PRODUCT AND AN AQUEOUS ALUMINA SLURRY, AND, B. THEREAFTER SEPARATING THE AQUEOUS ALUMINA SLURRY FROM THE ORGANIC REACTION PRODUCT, WHEREIN SAID AQUEOUS ALUMINA SLURRY IS CONTACTED WITH AN ORGANIC SOLVENT SELECTED FROM THE GROUP CONSISTING OF ETHANOL, PROPANOL, ISOPROPANOL, BUTANOL, ISOBUTANOL AND TERTIARY BUTANOL IN AN AMOUNT SUFFICIENT TO PRODUCE A PRODUCT ALUMINA HAVING A LOOSE BULK DENSITY FROM ABOUT 7.5 TO ABOUT 25 LB/FT3, A SURFACE AREA FROM ABOUT 275 TO ABOUT 400 M2/G AND A PORE VOLUME FROM ABOUT 1 TO ABOUT 2.75 CC/G, TO FORM A SOLVENTAQUEOUS ALUMINA MIXTURE, SAID MIXTURE IS DRIED AND SAID DRIED ALUMINA IS CALCINED AND SAID PRODUCT ALUMINA IS RECOVERED, THE IMPROVEMENT COMPRISING CALCINING SAID DRIED ALUMINA AT A TEMPERATURE IN EXCESS OF 350*F IN AN ATMOSPHERE CONTAINING FROM ABOUT 1.0 TO ABOUT 20.0 VOLUME PERCENT CARBON DIOXIDE IN MIXTURE WITH GASES SELECTED FROM THE GROUP CONSISTING OF AIR, NITROGEN, ARGON, HELIUM, HYDROGEN, CARBON MONOXIDE, SUPERHEATED STEAM, AND MIXTURES OF SUPERHEATED STEAM AND HYDROCARBON COMPOUNDS CONTAINING UP TO ABOUT 30 CARBON ATOMS AND MIXTURES THEREOF AND RECOVERING SAID PRODUCT ALUMINA, SAID PRODUCT ALUMINA BEING SUBSTANTIALLY WHITE AND EXTRUDABLE.
Claim 3
Dependent Claim
54 words
The improvement of claim 1 wherein said atmosphere contains from about 1.0 to about 20.0 volume percent carbon dioxide in mixture with gases selected from the group consisting of nitrogen, argon, helium, hydrogen, carbon monoxide, superheated steam, mixtures of superheated steam, and hydrocarbon compounds containing up to about 30 carbon atoms, and mixtures thereof.
Claim 4
Dependent Claim
27 words
The improvement of claim 2 wherein said carbon dioxide is present in an amount equal to from about 1 to about 8 volume percent of said atmosphere.
Claim 5
Dependent Claim
28 words
The improvement of claim 3 wherein said calcining is controlled to produce an alumina product having an Al2O3 content from about 77 to about 97 weight percent Al2O3.
Claim 6
Dependent Claim
152 words
The improvement of claim 2 wherein said drying is accomplished by: a. heating said solvent-aqueous alumina mixture to about 300*F to obtain partially dried alumina containing from about 70 to about 76 weight percent Al2O3; and, b. heating to about 300*F and simultaneously contacting said partially dried alumina with superheated steam for at least about 1 minute to obtain semi-dry alumina containing from about 70 to about 82 weight percent Al2O3; and wherein said calcining is accomplished by calcining said semi-dry alumina to about 800*F for at least about 4 minutes in the presence of said atmosphere containing from about 1.0 to about 8.0 volume percent carbon dioxide to obtain said product alumina containing from about 86 to about 90 weight percent Al2O3; and thereafter cooling to at least about 300*F in the presence of said atmosphere to obtain said product alumina containing from about 86 to about 90 weight percent Al2O3.
Claim 7
Dependent Claim
15 words
The improvement of claim 2 wherein said aqueous alumina slurry of(b) has been steam stripped.
Claim 8
Dependent Claim
10 words
The improvement of claim 6 wherein said gas is air.
Claim 9
Dependent Claim
152 words
The improvement of claim 5 wherein said drying is accomplished by: a. heating said solvent-aqueous alumina mixture to about 300*F to obtain partially dried alumina containing from about 70 to about 76 weight percent Al2O3; b. heating to about 300*F and simultaneously contacting said partially dried alumina with superheated steam for at least about 1 minute to obtain semi-dry alumina containing from about 79 to about 82 weight percent Al2O3; and, wherein said calcining is accomplished by calcining said semi-dry alumina to about 800*F for at least about 4 minutes in the presence of said atmosphere containing from about 1.0 to about 8.0 volume percent carbon dioxide to obtain said product alumina containing from about 86 to about 90 weight percent Al2O3; and thereafter cooling to at least about 300*F in the presence of said inert atmosphere to obtain said product alumina containing from about 86 to aBout 90 weight percent Al2O3.
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) | 1978-09-22 | 1979-03-24 | 1979-09-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-09-22 | 1983-03-24 | 1983-09-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-09-22 | 1987-03-24 | 1987-09-23 | $7700.00 | Window Closed / Lapsed |