GB1123184A - Improved method for recovering alumina from aluminate liquor - Google Patents
Improved method for recovering alumina from aluminate liquorInfo
- Publication number
- GB1123184A GB1123184A GB36569/65A GB3656965A GB1123184A GB 1123184 A GB1123184 A GB 1123184A GB 36569/65 A GB36569/65 A GB 36569/65A GB 3656965 A GB3656965 A GB 3656965A GB 1123184 A GB1123184 A GB 1123184A
- Authority
- GB
- United Kingdom
- Prior art keywords
- column
- liquor
- methanol
- vapour
- content
- 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
- 150000004645 aluminates Chemical class 0.000 title abstract 4
- 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
- 238000000034 method Methods 0.000 title abstract 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract 33
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 3
- 238000001704 evaporation Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 238000001556 precipitation Methods 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/02—Aluminium oxide; Aluminium hydroxide; Aluminates
- C01F7/04—Preparation of alkali metal aluminates; Aluminium oxide or hydroxide therefrom
- C01F7/14—Aluminium oxide or hydroxide from alkali metal aluminates
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
<PICT:1123184/C1/1> A method of recovering alumina from aluminate liquor, comprises passing aluminate liquor down a column, passing a vapour mixture containing steam and methanol and/or ethanol through said column in countercurrent to the aluminate liquor, whereby alumina hydrate is precipitated and separating solid hydrate from the methanol and/or ethanolcontaining liquor thus formed. In a preferred embodiment the methanol and/or ethanol is driven off from the methanol and/or ethanolcontaining liquor in a distilling column, at least part of the vapour from the first column being introduced into the lower part of the distilling column and at least part of the vapour from the distilling column being introduced into the lower part of said first column. In the drawing, liquor 10 which has been separated from red mud is introduced into the top of column 3 and flows downwards, its methanol content increasing and its water content becoming less. Liquid methanol 15 containing about 20 mol% water is added to the emerging liquor 14 which flows into the precipitation agitators 9. When the hydrate has been stirred out and separated from the liquor, the liquor 11 is pumped into column 2 in which it loses the main proportion of its methanol content. The remaining methanol is driven off in column 4 and the liquor 12 which leaves column 4 contains only traces of methanol. The liquor 12 from which methanol has been expelled is concentrated by evaporating a portion of its water content. The concentration of the liquor may be carried out in a multi-stage evaporator, the first stage of which is heated with steam. Vapour 16 from column 2 may be condensed in a water-cooled condenser and part may be used to heat evaporator 8 which operates at less than atmospheric pressure and is used for concentrating liquor 12. The major part of the vapour 16 is taken into column 1. The vapour 17 leaving column 1 may be introduced into column 2, the remainder into column 3 from which vapour 19 with a very small methanol content can be withdrawn. Vapour 19 is taken into the bottom part of column 4.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| YU120664 | 1964-08-25 | ||
| DEF0043925 | 1964-09-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1123184A true GB1123184A (en) | 1968-08-14 |
Family
ID=25976452
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB36569/65A Expired GB1123184A (en) | 1964-08-25 | 1965-08-25 | Improved method for recovering alumina from aluminate liquor |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB1123184A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4430310A (en) | 1983-02-08 | 1984-02-07 | Kaiser Aluminum & Chemical Corporation | Purification of impure Bayer process liquors |
| US4464347A (en) * | 1982-12-27 | 1984-08-07 | Aluminum Company Of America | Recovery of aluminum from spent liquor |
| US4496524A (en) * | 1984-03-08 | 1985-01-29 | Aluminum Company Of America | Process for the removal of sodium oxalate compounds from Bayer spent liquor |
| US4581207A (en) * | 1982-12-27 | 1986-04-08 | Aluminum Company Of America | Recovery of aluminum from spent liquor |
| EP0271104A3 (en) * | 1986-12-11 | 1988-09-07 | Aluminum Company Of America | Controlled crystal form of aluminum hydroxide |
| EP0327660A1 (en) * | 1988-02-11 | 1989-08-16 | VAW Aluminium AG | Process for the production of fillers and fire-preventing materials based on hydrargillite-type aluminium hydroxide |
| US4900537A (en) * | 1986-12-11 | 1990-02-13 | Biotage, Inc. | Control of form of crystal precipitation of aluminum hydroxide using cosolvents and varying caustic concentration |
| US5019360A (en) * | 1987-11-24 | 1991-05-28 | Northern States Power Company | Method for the processing of fly ash, scrubber sludge and the like; and product |
| RU2184703C2 (en) * | 2000-06-27 | 2002-07-10 | Акционерное общество открытого типа "Всероссийский алюминиево-магниевый институт" | Method of processing aluminate solution in production of alumina from nepheline |
| CN101234773B (en) * | 2007-02-02 | 2010-12-08 | 中国科学院过程工程研究所 | A kind of method utilizing sodium aluminate solution to produce aluminum hydroxide |
-
1965
- 1965-08-25 GB GB36569/65A patent/GB1123184A/en not_active Expired
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4464347A (en) * | 1982-12-27 | 1984-08-07 | Aluminum Company Of America | Recovery of aluminum from spent liquor |
| US4581207A (en) * | 1982-12-27 | 1986-04-08 | Aluminum Company Of America | Recovery of aluminum from spent liquor |
| US4430310A (en) | 1983-02-08 | 1984-02-07 | Kaiser Aluminum & Chemical Corporation | Purification of impure Bayer process liquors |
| US4496524A (en) * | 1984-03-08 | 1985-01-29 | Aluminum Company Of America | Process for the removal of sodium oxalate compounds from Bayer spent liquor |
| EP0271104A3 (en) * | 1986-12-11 | 1988-09-07 | Aluminum Company Of America | Controlled crystal form of aluminum hydroxide |
| US4822593A (en) * | 1986-12-11 | 1989-04-18 | Aluminum Company Of America | Control of form of crystal precipitation of aluminum hydroxide using cosolvents and varying caustic concentration |
| US4900537A (en) * | 1986-12-11 | 1990-02-13 | Biotage, Inc. | Control of form of crystal precipitation of aluminum hydroxide using cosolvents and varying caustic concentration |
| US5019360A (en) * | 1987-11-24 | 1991-05-28 | Northern States Power Company | Method for the processing of fly ash, scrubber sludge and the like; and product |
| EP0327660A1 (en) * | 1988-02-11 | 1989-08-16 | VAW Aluminium AG | Process for the production of fillers and fire-preventing materials based on hydrargillite-type aluminium hydroxide |
| RU2184703C2 (en) * | 2000-06-27 | 2002-07-10 | Акционерное общество открытого типа "Всероссийский алюминиево-магниевый институт" | Method of processing aluminate solution in production of alumina from nepheline |
| CN101234773B (en) * | 2007-02-02 | 2010-12-08 | 中国科学院过程工程研究所 | A kind of method utilizing sodium aluminate solution to produce aluminum hydroxide |
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