GB1347106A - Preparation of alumina - Google Patents
Preparation of aluminaInfo
- Publication number
- GB1347106A GB1347106A GB2179871A GB2179871A GB1347106A GB 1347106 A GB1347106 A GB 1347106A GB 2179871 A GB2179871 A GB 2179871A GB 2179871 A GB2179871 A GB 2179871A GB 1347106 A GB1347106 A GB 1347106A
- Authority
- GB
- United Kingdom
- Prior art keywords
- alkali metal
- pores
- aqueous solution
- solids content
- precipitated
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 title abstract 3
- 239000011148 porous material Substances 0.000 abstract 5
- 239000000017 hydrogel Substances 0.000 abstract 3
- 239000007787 solid Substances 0.000 abstract 3
- 229910000288 alkali metal carbonate Inorganic materials 0.000 abstract 2
- 150000008041 alkali metal carbonates Chemical class 0.000 abstract 2
- 239000001099 ammonium carbonate Substances 0.000 abstract 2
- 239000007864 aqueous solution Substances 0.000 abstract 2
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 abstract 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 abstract 1
- 229910001413 alkali metal ion Inorganic materials 0.000 abstract 1
- 150000004645 aluminates Chemical class 0.000 abstract 1
- 159000000013 aluminium salts Chemical class 0.000 abstract 1
- 229910000329 aluminium sulfate Inorganic materials 0.000 abstract 1
- 235000012538 ammonium bicarbonate Nutrition 0.000 abstract 1
- 235000012501 ammonium carbonate Nutrition 0.000 abstract 1
- 238000001354 calcination Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 238000012986 modification Methods 0.000 abstract 1
- 230000004048 modification Effects 0.000 abstract 1
- 238000001556 precipitation Methods 0.000 abstract 1
- 239000011541 reaction mixture Substances 0.000 abstract 1
- 239000002002 slurry Substances 0.000 abstract 1
- 239000000243 solution Substances 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/633—Pore volume less than 0.5 ml/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/635—0.5-1.0 ml/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/66—Pore distribution
- B01J35/67—Pore distribution monomodal
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
1347106 Alumina hydrogel SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ NV 19 April 1971 [16 Feb 1970] 21798/71 Heading C1A An alumina hydrogel is precipitated by concurrently reacting an aqueous solution of an aluminium salt with an aqueous solution of an aluminate at pH 8À5-10À5, and 20-40 C., to a solids content of the reaction mixture of up to 40 gm/l. and the resulting hydrogel is separated and washed with 0À005-1 M. ammonium carbonate or bicarbonate solution which is free from alkali metal ions, and then dried and calcined, to give a product having the following characteristics: Bulk density 0À5-0À8 gm/c.c. Surface area 200-350 m<SP>2</SP>/gm. Pore volume 0À4-0À7 c.c./gm. Average pore diam. 60-120 (<1% pores below 30 and <1% pores greater than 350 , at least 70% pores 40-160 ). An alkali metal carbonate may be added before or after precipitation. The precipitated slurry preferably contains 20-40 gm/litre solids. Calcination is preferably performed at 450- 650 C. in a non-reducing atmosphere. In a modification the reaction is performed in the presence of an alkali metal carbonate, to a solids content of up to 80 gms/l.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US1170970A | 1970-02-16 | 1970-02-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1347106A true GB1347106A (en) | 1974-02-27 |
Family
ID=21751639
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2179871A Expired GB1347106A (en) | 1970-02-16 | 1971-04-19 | Preparation of alumina |
Country Status (5)
Country | Link |
---|---|
CA (1) | CA952289A (en) |
DE (1) | DE2107147A1 (en) |
FR (1) | FR2080526B1 (en) |
GB (1) | GB1347106A (en) |
NL (1) | NL7101963A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0208357A2 (en) * | 1985-07-05 | 1987-01-14 | Shell Internationale Researchmaatschappij B.V. | Wide pore alumina supports |
FR3049595A1 (en) * | 2016-04-05 | 2017-10-06 | Ifp Energies Now | PROCESS FOR PREPARING A MESOPOROUS AND MACROPOROUS ALUMINA FROM AT LEAST ONE DAWSONITE PRECURSOR |
CN112516993A (en) * | 2019-09-17 | 2021-03-19 | 中国石油化工股份有限公司 | Preparation method of alumina carrier |
FR3112496A1 (en) * | 2020-07-20 | 2022-01-21 | IFP Energies Nouvelles | Method for washing a suspension of metal oxides |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA1123173A (en) * | 1974-09-09 | 1982-05-11 | Nalco Chemical Company | Controlling the pore diameter of precipitated alumina |
FR3122585A1 (en) | 2021-05-04 | 2022-11-11 | Universite Claude Bernard Lyon 1 | Mesoporous solid to regulate humidity in enclosed spaces |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1331328A (en) * | 1960-04-15 | 1963-07-05 | Exxon Research Engineering Co | Hydrorefining catalyst and hydrorefining process |
-
1971
- 1971-02-15 DE DE19712107147 patent/DE2107147A1/en active Pending
- 1971-02-15 NL NL7101963A patent/NL7101963A/xx unknown
- 1971-02-15 FR FR7104979A patent/FR2080526B1/fr not_active Expired
- 1971-02-15 CA CA105,389A patent/CA952289A/en not_active Expired
- 1971-04-19 GB GB2179871A patent/GB1347106A/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0208357A2 (en) * | 1985-07-05 | 1987-01-14 | Shell Internationale Researchmaatschappij B.V. | Wide pore alumina supports |
EP0208357A3 (en) * | 1985-07-05 | 1989-10-11 | Shell Internationale Research Maatschappij B.V. | Wide pore alumina supports |
FR3049595A1 (en) * | 2016-04-05 | 2017-10-06 | Ifp Energies Now | PROCESS FOR PREPARING A MESOPOROUS AND MACROPOROUS ALUMINA FROM AT LEAST ONE DAWSONITE PRECURSOR |
CN112516993A (en) * | 2019-09-17 | 2021-03-19 | 中国石油化工股份有限公司 | Preparation method of alumina carrier |
FR3112496A1 (en) * | 2020-07-20 | 2022-01-21 | IFP Energies Nouvelles | Method for washing a suspension of metal oxides |
WO2022017831A1 (en) * | 2020-07-20 | 2022-01-27 | IFP Energies Nouvelles | Method for washing a metal oxide suspension |
Also Published As
Publication number | Publication date |
---|---|
DE2107147A1 (en) | 1971-09-02 |
CA952289A (en) | 1974-08-06 |
FR2080526A1 (en) | 1971-11-19 |
NL7101963A (en) | 1971-08-18 |
FR2080526B1 (en) | 1973-12-28 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PLNP | Patent lapsed through nonpayment of renewal fees |