US4518571A
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Process for desilication of aluminate liquors in the production of alumina
Assignee: LENINGRADSKY TEKHNOLOGICHESKY INSTITUT IMENI LENSOVETA USSR LENINGRAD MOSKOVSKY PROSPEKT 26
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Filing: 1984-02-27
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Granted: 1985-05-21
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Expires: 2004-02-27
Abstract
Abstract The process consists of two desilication stages. In the first stage the aluminate liquor resulting from digestion of the sinter is subjected to an autoclave treatment to remove the major portion of impurities of SiO2 and Fe2O3. In the second stage the aluminate liquor is treated with a desilication agent comprising a lime pulp containing oxides CaO, Al2O3, SiO2, Fe2O3, Na2O in a mass ratio of CaO:(SiO2+Fe2O3)=1,000 to 5,000:1 and Na2Al2O3=0.25-0.60:1, wherein CaO is active, Na2O-in the carbonate form. This lime pulp is employed in such an amount as to ensure the content of active CaO in the aluminate liquor within the range of from 5 to 10 g/l . The impurities of SiO2 and Fe2O3 present in the liquor pass into the solid phase with the formation of calcium hydrogarnets of the formula 3 CaO(Al,Fe)2O3 mSiO2(6-2m)H2O, wherein m=0.01-0.5 which are separated as a mud.
Inventors
- 👤 Nikolai A. Kaluzhsky
- 👤 Viktor M. Sizyakov
- 👤 Vladimir V. Andreev
- 👤 Alexei I. Alexeev
- 👤 Khoren A. Badaliants
- 👤 Isaak A. Zatulovsky
- 👤 Valentin I. Korneev
- 👤 Ivan M. Kostin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 05:14
CPC Classifications
B; B22; B22C; B22C1/00; B22C1/16; B22C1/18; C; C01; C01F; C01F7/00; C01F7/02; C01F7/46; C01F7/47; C04; C04B; C04B7/00; C04B7/24; Y; Y02; Y02P; Y02P40/00; Y02P40/10
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
202 words
A process for desilication of aluminate liquors in the production of Alumina comprising two stages of desilication: (1) Heat-treating an aluminate liquor, obtained after digestion of a sinter, at a temperature of 150°-170° C. under a pressure of 6 to 12 atmospheres to remove the main portion of SiO 2 and Fe 2 O 3 impurities in the form of an aluminosilicate mud which is separated; (2) Treating the aluminate liquor with a desilication agent which is a lime pulp containing oxides CaO, Al 2 O 3 , SiO 2 , Fe 2 O 3 NaO 2 in a mass ratio of CaO: (SiO 2 +Fe 2 O 3 )=1,000-5,000:1 and Na 2 O:Al 2 O 3 =0.25-0.60:1, said Na 2 O being in the carbonate form, wherein CaO is active in an amount ensuring the content of active CaO in the aluminate liquor within the range of 5 to 10 g/l, whereby the remaining portion of SiO 2 and Fe 2 O 3 impurities being removed, pass into the solid phase with the formation of calcium hydrogarnet of the formula: 3CaO(Al, Fe) 2 O 3 .mSiO 2 .(6-2m).H 2 O, wherein m=0.01-0.5, which is separated in the form of a mud.
Claim 2
Dependent Claim
202 words
A process for desilication of aluminate liquors in the production of Alumina comprising two stages of desilication: (1) Heat-treating an aluminate liquor, obtained after digestion of a sinter, at a temperature of 150°-170° C. under a pressure of 6 to 12 atmospheres to remove the main portion of SiO 2 and Fe 2 O 3 impurities in the form of an aluminosilicate mud which is separated; (2) Treating the aluminate liquor with a desilication agent which is a lime pulp containing oxides CaO, Al 2 O 3 , SiO 2 , Fe 2 O 3 NaO 2 in a mass ratio of CaO: (SiO 2 +Fe 2 O 3 )=1,000-5,000:1 and Na 2 O:Al 2 O 3 =0.25-0.60:1, said Na 2 O being in the carbonate form, wherein CaO is active in an amount ensuring the content of active CaO in the aluminate liquor within the range of 5 to 10 g/l, whereby the remaining portion of SiO 2 and Fe 2 O 3 impurities being removed, pass into the solid phase with the formation of calcium hydrogarnet of the formula: 3CaO(Al, Fe) 2 O 3 .mSiO 2 .(6-2m).H 2 O, wherein m=0.01-0.5, which is separated in the form of a mud.
Claim 3
Dependent Claim
24 words
A process according to claim 1, wherein desilication in the second stage is conducted at a temperature of 60°-95° C. under a normal pressure.
Claim 4
Dependent Claim
115 words
A process according to claim 1, wherein the desilication agent (lime pulp) is obtained by mixing a lime milk containing from 150 to 200 g/l CaO with an aluminate liquor obtained at the second desilication stage, the components being mixed to ensure the content of CaO in the pulp equal to between 70 and 90 g/l at a weight ratio of Ca: (SiO 2 +Fe 2 O 3 )=1,000 to 5,000:1 and Na 2 O: Al 2 O 3 =0.25 to 0.60:1, wherein CaO is active and Na 2 O is in the carbonate form, and holding the mixture at stirring for 1 to 2 hours at a temperature of from 60° to 75° C.
References Cited (Backward Citations)
No citation records indexed.
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