AU551374B2 - Creación de Inventos y Patentes con Inteligencia Artificial

AU551374B2 – A method for recovering useful products from waste products obtained when manufacturing aluminium hydroxide
– Google Patents

AU551374B2 – A method for recovering useful products from waste products obtained when manufacturing aluminium hydroxide
– Google Patents
A method for recovering useful products from waste products obtained when manufacturing aluminium hydroxide

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Publication number
AU551374B2

AU551374B2
AU10441/83A
AU1044183A
AU551374B2
AU 551374 B2
AU551374 B2
AU 551374B2
AU 10441/83 A
AU10441/83 A
AU 10441/83A
AU 1044183 A
AU1044183 A
AU 1044183A
AU 551374 B2
AU551374 B2
AU 551374B2
Authority
AU
Australia
Prior art keywords
sodium
aluminium
solution
fluoroaluminate
fluorine
Prior art date
1982-01-07
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.)

Ceased

Application number
AU10441/83A
Other versions

AU1044183A
(en

Inventor
Hans Arne Lennart Berglund
Gosta Bertil Lagerstrom
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

Boliden AB

Original Assignee
Boliden AB
Priority date (The priority date 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 date listed.)
1982-01-07
Filing date
1982-12-21
Publication date
1986-04-24

1982-12-21
Application filed by Boliden AB
filed
Critical
Boliden AB

1983-07-28
Publication of AU1044183A
publication
Critical
patent/AU1044183A/en

1986-04-24
Application granted
granted
Critical

1986-04-24
Publication of AU551374B2
publication
Critical
patent/AU551374B2/en

2002-12-21
Anticipated expiration
legal-status
Critical

Status
Ceased
legal-status
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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

C01F7/48—Halides, with or without other cations besides aluminium

C01F7/50—Fluorides

C01F7/54—Double compounds containing both aluminium and alkali metals or alkaline-earth metals

C—CHEMISTRY; METALLURGY

C01—INORGANIC CHEMISTRY

C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C

C01B33/00—Silicon; Compounds thereof

C01B33/20—Silicates

C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates

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

C01F7/48—Halides, with or without other cations besides aluminium

C01F7/50—Fluorides

Abstract

PCT No. PCT/SE82/00434 Sec. 371 Date Aug. 31, 1983 Sec. 102(e) Date Aug. 31, 1983 PCT Filed Dec. 21, 1982 PCT Pub. No. WO83/02444 PCT Pub. Date Jul. 21, 1983.The invention relates to a method for recovering useable products from waste products deriving from the manufacture of aluminium fluoride on the basis of aluminium hydroxide and fluosilicic acid. Mother liquors and washing water from a scrubber in said process, which solutions contain aluminium, silica, fluorine, and phosphorous is reacted in a first step with sodium ions at pH 2-3, and a temperature of 50 DEG -100 DEG C. to give a precipitate of sodium fluoroaluminate, which is isolated. The filtrate from said first step can be reacted with the silica waste product obtained in the above mentioned aluminium fluoride manufacture.

Description

A METHOD FOR RECOVERING USEFUL PRODUCTS FROM WASTE PRODUCTS OBTAINED WHEN MANUFACTURING ALUMINIUM FLUORIDE
DESCRIPTION
Technical field
The present invention relates to a method for recovering useful products from waste products obtained when producing aluminium fluoride from aluminium hydroxide and fluosilicic acid; and more particularly to recovering sodium silicoaluminates and sodium fluoroaluminates from silica waste, mother liquor and wash-water deriving from the manufacture of aluminium fluoride.
An object of the present invention is to obtain a possibility of recovering useful and economically valuable products from the waste products obtained in the aluminium fluoride production.
Background of the invention
When manufacturing aluminium fluoride, several troublesome waste products are obtained which must be deposited and, optionally, rendered harmless. Thus, there is obtained a silica waste which contains fluorine and aluminium impurities, and a mother liquor and a wash-water containing fluorine, aluminium and silicon. These waste products present a serious problem, since they occur in relatively large quantities and require complicated and expensive treatment before they can be deposited. It is true that silica residues per se can be deposited, but – as will be understood – the direct deposit of silica contaminated with large quantities of harmful impurities cannot be tolerated. The mother liquor and the wash water must be neutralized with calcium hydroxide to a pH-value of about 10, at which the fluorine and silicate contents thereof precipitate. This precipitate is then separated from the mother liquor and wash water, for example by centrifugation, and subsequently deposited.
Thus, the aforementioned waste products constitute a serious environ¬ mental problem, even though they may be treated in the manner indi-
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cated before being deposited. In additon, substantial amounts of silicon and fluorine are lost when the waste is treated in said manner.
The reactions involved in the production of aluminium fluoride are given below, the waste products being underlined.
1. H2SiF6 + 2 A1(0H)3 »2-^*AlF3 ( ) + Si02
2. ^-A1F3 ) ^A1F3 • 3H£0 + mother liquor
3. 3-A!F3 • 3H20 – ->AlF3 + 3H20 ÷ scrubber water
Prior art recognizes some different methods for recovering active silica and cryolite as well as other compounds from fluosilicic acid and waste products from the preparation of aluminium fluoride.
AT,B, 314474 discloses the production of aluminium fluoride from fluosilicic acid recovered from the production of phosphate contain- ing fertilizers. Hereby 8-25% fluosilicic acid is reacted with alu¬ minium hydroxide in a relation which is 0.95 – 1.05:1 of the stoichio- etric relationship according to the formula. H2SiFβ + A1(0H)3 »
2 A1F3 + Si02 + H20 at a temperature of 60-100°C. The aluminium fluoride obtained can be used.for the production of cryolite. Aluminium hydroxide is thereby reacted with fluosilicic acid in two steps, using one third of the amount of aluminium hydroxide requested in the first step, and two thirds thereof in the second step, whereby a mixture containing aluminium fluoride, which is precipitated and separated off, and aluminium hydrofluoric acid is obtained. The aluminium hydrofluoric acid is then treated with alkali at pH 3-6.5, preferably at pH 6-6.5 and at a tempera¬ ture of 60°C to form cryolite. This process, however, requires very pure components as otherwise contaminations of i.a. phos¬ phates will precipitate and contaminate the cryolite. Any silica
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present will also form complexes which contaminates the cryolite and deteriorates the quality thereof.
Using fluosilicic acid and ammonia as starting materials active si- lica and cryolite can be prepared (AT, B, 315128). Thereby ammonium fluoride and silica are primarily prepared, whereafter the ammonium fluoride is reacted with sodium aluminate to the formation of cryolite.
SE,B, 366723 relates to a process to recover fluorine and aluminium from dilute, aqueous solutions, particularly mother liquors obtained in the crystallization of aluminium fluoride, whereby the mother liquors are treated with ammonia, or ammonium dicarbonate to give a chiolite-analogous ammonium compound, (NH.)5 Al3 F,. . The pre¬ cipitation of said compound is carried out at pH 6-6.5.
SE,B, 7502835-7 relates to a concentrated synthetic fluxing agent based on calcium fluoride, where remaining fluorine quantities from the production of aluminium fluoride from fluosilicic acid and alumi- niumhydroxide are precipitated using a calcium compound.
In accordance with SE,A, 8100218-0 a method for recovering useful products from waste of the described form is disclosed, whereby silica obtained in the manufacture of aluminium fluoride and con¬ taminated with, inter alia, fluorine and aluminium, is dissolved in a strongly basic hydroxide; mixing the first solution obtained with a second solution obtained by dissolving aluminium hydroxide with a strongly basic hydroxide, and with waste mother liquor and optionally also washing water from the manufacture of aluminium fluoride in such proportions that the pH-value of the mixture lies between about 10 and 14, the silica content of the waste products supplied being pre¬ cipitated as a silicoaluminate, which is separated off, preferably by filtration, for optional further treatment or for direct use, where¬ after fluorine, if present from the waste products, is recovered from the filtrate by adding thereto an aluminium compound in an amount sufficient to precipitate substantially all the fluorine content contained in the filtrate as a fluoroaluminate, which is separated

pff, preferably by filtration, for further use, and whereafter the final filtrate is passed to a recipient or utilized, for example, as process water in other processes.
Carrying out said method a sodium aluminium silicate is obtained which is rather alkaline and will thereby require a high demand of alum in the preparation of a paper from a paper pulp using said silicate as a filler.
Disclosure of the present invention
The present invention relates to a surprisingly distinctive method for recovering valuable substances in the form of useful products from waste of the aforedescribed kind, while at the same time sub¬ stantially eliminating the environmental problems created by the waste. The method according to the invention is of further economic interest, since, among other things, the waste need not be neutral¬ ized, meaning that no calcium hydroxide need to be used, which in turn means lower costs.
By the present method it has been shown possible to prepare an alumi¬ nium silicate which is less alkaline than that described above as well as it has been shown possible to precipitate a fluoroaluminate having a very high purity and a crystal size that can be varied depending on simple variations of the precipitation conditions.
The present method is thus characterized by adding alkali metal ions in the form of an alkali metal salt to collected mother liquors and washing water obtained in the manufacture of aluminium fluoride and being contaminated with aluminium, silica, and fluorine, and by adjusting the hydrogen ion concentration of said mother liquors and washing water to a pH of 2.0 to 3.0 by adding an alkali metal base while maintaining a temperature of said collected solutions of above about 50°C, isolating the alkali metal fluoroaluminate thereby pre¬ cipitated by filtration, whereafter the filtrate comprising silica and minor amounts of aluminium and fluorine can be passed to a second step for the recovery of one or more of said compounds, or otherwise used.

Further characteristics of the invention are set forth in the accom¬ panying claims.
The term alkali metal base above means any potassium, sodium, or lithium hydroxide, carbonate, hydrogen carbonate or sulphite, prefer¬ ably sodium hydroxide and sodium carbonate.
Thus, the useful product produced is a fluoroaluminate, preferably a sodium fluoroaluminate as chiolite or cryolite. In a second stage the silica content of the waste products can be rocovered in the form of a silicoalu inate, preferably sodium silicoaluminate. Such products as sodium fluoroaluminate (cryolite), and sodium silicoaluminate can be used directly, and are requested by the market. Sodium fluoroaluminate or cryolite is used to a large extent as a fluxing agent when producing aluminium electrolytically. Sodium silicoaluminate can be used as a pigment agent in the paper-making industry and in the rubber and paint industry.
Cryolite is thus used mainly as a fluxing agent in the aluminium in- dustry, but is also known as a fluxing agent when preparing enamels, as a filler in polishing/grinding discs, as an intensifying pigment, as a grinding powder, or as an insecticide.
According to the invention, the useable products are preferably re- covered from the waste in sequential steps in a coherent process, in which first fluorine and aluminium are recovered in the form of a fluoroaluminate, preferably sodium fluoroaluminate, and the silicon content in an optional subsequent step, is recovered in the form of a silicoaluminate, preferably sodium silicoaluminate.
When recovering the fluorine and aluminium contents of the waste products, particularly the mother liquors and washing water (scrubber water) from the aluminium fluoride production, for example in the form of sodium fluoroaluminate (cryolite), there are collected such mother liquors and/or washing water, the hydrogen ion concentration

thereof is controlled to be about pH 1 whereupon the hydrogen ion concentration is adjusted by the addition of sodium hydroxide and/or sodium carbonate to pH 2.0-3.0, more preferably 2.0-2.5. The temper¬ ature of the solution is brought to or maintained at, if already hot, at least 50°C, preferably 60 to 80°C. The amount of sodium added while adjusting the pH is most often too small and further sodium ions are thus requested, and are thereby added in the form of a sodium salt preferably sodium sulfate and/or sodium chloride. The sodium salt is from a dispensing point of view preferably added in the form of an aqueous solution. The addition of Na+-ions can be done either before or after the adjustment of the pH to 2.0-3.0. So added the sodium fluoroaluminate will precipitate and the precipitate is isolated preferably by way of filtration such as vacuum and/or pres¬ sure filtration.
Sometimes, in order to increase the yield the aluminium content in the precipitation step of cryolite is primarily held low, whereby a part of the fluorine content present is firstly coprecipitated as sodium fluorosilicate. In a later part of the reaction aluminium sulphate is then added whereby said silicate is dissolved and the fluorine set free is reacted with the aluminium to form cryolite.
Having thus isolated the sodium fluoroaluminate (cryolite) the silica content of the waste products of the above described reactions, i.e. mainly silica from reaction 1 but also silica present in the mother liquor and washing water, can be recovered e.g. in the form of sodium silicoaluminate. Thereby a sodium silicate solution is prepared by dissolving the silica from reaction 1 in sodium hydroxide as well as an aluminium sulfate solution is prepared. Said solutions are added to the filtrate obtained after isolation of the cryolite and pH is adjusted to 6 to 14, preferably 7 to 10, whereby the sodium silico¬ aluminate precipitates. The sodium silicoaluminate as precipitated is isolated by filtration e.g. vacuum and/or pressure filtration.

Under certain circumstances the fluorine content of the silica may be too high to be used directly in the preparation of sodium aluminium silicate as cryolite will precipitate together therewith. Thereby it is possible to remove the fluorine content from the silica by sus- pending the silica waste in sulphuric acid, heating the mixture, whereby fluorine and silicofluoride are driven off, isolated in a scrubber and passed on to the precipitation step of fluoroaluminate, and the silica is suspended in water for dissolving any aluminium sulphate present. The slurry thus obtained is then passed to a fil- tration step, where the solid, and now pure silica is separated off, washed and passed on to the dissolver for production of sodium sil¬ icate and the aluminium sulphate solution containing sulphuric acid is passed to the precipitation step of sodium aluminium silicate.
It is further possible to eliminate any coprecipitated phosphate in the cryolite, which coprecipitation may occur at higher pH levels in the range indicated, b slurrying the cryolite precipitated in.acidic environment i.e. at pH 1-2.
An exemplary, preferred embodiment of the process will now be de¬ scribed in more detail with reference to the accompanying drawing, the single figure of which is a flow sheet of said embodiment.
Mother liquors and washing water from the manufacture of aluminium fluoride are optionally but preferably collected in a buffer storage tank 1 in which the pH can be adjusted to pH /*->1 and the A1:6F molar ratio is adjusted to 1-1.25:1, 50% NaOH solution is stored in a storage tank 2, and a solution of Na2S0. is stored in storage’tank 3. In a further tank 4 a solution tof aluminium sulphate containing 8% A1203 is stored. The collected solution from buffer tank 1 having a temperature of preferably 50-70°C to keep the formation of Na2 SiFg low, is via conduit 5 added to a reaction vessel 6 provided with heating means and stirring means (not shown). Heating is provided by a steam jacket. Sodium hydroxide solution is slowly added via a conduit 7 and the addition is made and controlled by a pH-meter (not

shown) regulating the pH of the solution added to pH 2.0-2.5 (2.25
+ ~
– 0.25). To increase the sodium content of the reaction mixture sodium sulphate (or alternatively sodium chloride) solution is added from the tank 3 via conduit 8. When so adding and controlling the said additions a fine-particle solid precipitates, which solid con¬ sists of sodium fluoro aluminate. The addition of sodium is so made that substantially all fluorine present in the collected solution is eliminated.
In case the fluorine content is high and the aluminium content is low, aluminium is added to the reaction vessel 6 via a conduit 9 in the form of an aluminium sulphate solution containing about 8 % A1203, at which concentration the solution can be stored without risk of solid aluminium sulphate crystallizing.
In case the collected solution has a hydrogen ion concentration dif¬ fering from about pH 1 the pH can be adjusted by adding sulphuric acid or sodium hydroxide to said value. By adding Al in the form of aluminium sulphate the aluminium: 6 fluorine molar ratio can be con- trolled, whereby said ratio should be 1-1.25:1. Likewise, fluosilic acid can be added to control said ratio. The pH shall be about 1 as at higher pH fluorine seems to be present as complexes which do not dissolve but remain in solution after precipitation.
– The solution containing the precipitated sodium fluoroaluminate is then transferred via a conduit 10 to a sedimentation tank and then to a vacuo filtering device 11, wherein the solid sodium fluoro alumi¬ nate is separated off, washed, dried at about 100°C and calcinated at 500 to 700°C and is removed to a sacking station 19 and storage for delivery to the market. The sodium fluoroaluminate, cryolite, having a low residual content of phosphorous and silica is an excellent fluxing agent in the manufacture of aluminium.
In order to keep the quality of the cryolite high thereby eliminate problems when used as a fluxing agent the residual contents of Si and

P should be held very low. Cryolite of the present method meets these demands.
The filtrate obtained from the filtration apparatus can be transferred via a conduit 12 to a second reaction vessel 13 for the production of a sodium aluminium silicate.
EXAMPLE 1
. A combined solution consisting of a mother liquor and washing water •0 from a scrubber from the manufacture of aluminium fluoride comprising 15 g F/l, 3.6 g Si02/1, 4.4 g Al/1, ■*–* 50 mg 205/1 and having a pH of j 1 was used. The A1:6F molar ratio is thereby 1.25:1.
If the A1:6F molar ratio is > 1.25:1 further fluorine can be added 5 in the form of fluosilicic acid.
To 25 litres of this combined solution Na -ions in the form of a 35% sodium chloride solution (350 g NaCl in total) are added, whereupon 370 ml of 50% NaOH-solution was added slowly during 15 min to raise 0 pH to 2.2. The Na+-ion excess should be 1-2 g per litre. The solution was pre-heated to 60°C and so maintained. The reaction solution was continuously stirred. Sodium ions had thereby been added in at least an amount of three times the molar content of aluminium. When in¬ creasing the pH of the solution a precipitate consisting of natriu – 5 fluoroaluminate was obtained. The reaction time to complete the precipitation is 1 to 3 hr. The solution containing the precipitate being dispersed therein was transferred to a vacuum filtration appa¬ ratus, where the sodium fluoroaluminate was separated off, washed wwiitthh wwaa’ter, dried at about 100°C, calcinated at 500 to 700°C and 0 packed.
Yield:
Sodium fluoroaluminate: 650 g containing 55.6 % F, 28.8 % Na , 14.8 % Al , and 0.4 % Si02, and 0.03 % P fi
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10
EXAMPLE 2
A combined solution inance with that of Example 1 was treated in the same way as the solution was treated in Example 1 above with the following exception. When the reaction had went on for about 20 minutes 13.8 g of aluminium was added in the form of an aluminium sulphate solution, whereafter the reaction was continued for another 1.5 hr.
Residual Si02 in the sodium fluoroaluminate was thereby reduced to 0.07 %. All other analytical data corresponded to those obtained in Example 1.
EXAMPLE 3
2 litres of a combined solution comprising 18.5 g F/l, 10 g SiQ2/l9 5.0 g Al/1, ^-» 50 mg P20r 1 and having a pH of«^1 were used. The A1:6F molar ratio was thereby 1.15.
The solution was treated in accordance with Example 1, step 1, above using 28 g NaCl, and 30 ml of 50 % NaOH-solution. The end pH was 2.3, the reaction temperature 60°C, and the reaction time 3 hr.
Yield of sodium fluoroaluminate 64 g containing: 30.8 % Na, 52.1 % F, 12.8 % Al, and 0.58 % Si02 and 0.04 % P£05 (100 % cryolite).
The sodium fluoroaluminate prepared can be obtained in the form of cryolite alone, chiolite alone, or mixtures thereof, depending on the order in which the reactants are added together. Having the whole contents of sodium ions present from the beginning provides for a production of cryolite, whereby a late addition of sodium ions pro- vides for a formation of chiolite. This will be evident from the following Examples 4 to 9.
EXAMPLE 4
41 of a combined mother liquor and scrubber water solution of the composition given in Example 1 were added to a reaction vessel,.

n
whereupon 35 g NaCl were addod and the total mixture was brought to a temperature of 60°C. Thereafter sodium carbonate was added to pH 2.5. The precipitate obtained consisted of sodium fluoroaluminate in the form of 100 % cryol ite.
EXAMPLE 5
41 of a combined solution in accordance with Example 4 above and containing 35 g of NaCl were added simultaneously with a sodium car¬ bonate aqueous solution (58.5 g of Na2C03) to a reaction vessel. The temperature of the solutions was kept at 60°C. Final pH was 2.5. The precipitate obtained consisted of sodium fluoroaluminate in the form of 75 % cryolite, and 25 % chiolite.
EXAMPLE 6 41 of a combined solution in accordance with Example 4 above were neutralized to pH 2.5 using sodium carbonate, whereupon 35 g of NaCl were added. The temperature of the solutions was 60°C. The precipitate obtained consisted of sodium fluoroaluminate in the form of 100 % chiolite.
EXAMPLE 7
41 of a combined solution in accordance with Example 4 above were heated to 60°C and placed in a reaction vessel. To this solution
35 g of NaCl and sodium carbonate to pH 2.5 were added simultaneously. The precipitate obtained consisted of sodium fluoroaluminate in the form of 100 % chiolite.
EXAMPLE 8
To a reaction vessel an aqueous solution of sodium chloride (35 g) was added, whereupon sodium carbonate and 41 of a combined solution in accordance with Example 4 having an A1:6F molar ratio of 1.05:1 were added simultaneously. The precipitate obtained consisted of sodium fluoroaluminate in the form of 100 % cryolite.
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EXAMPLE 9
Cryolite was prepared in accordance with Example 1, whereafter, when still in the form of a slurry, sodium carbonate and H2SiFβ were added simultaneously to obtain an A1:6F olar ratio of 1.05 while maintaining pH of 2.5. Yield 100 % of cryolite.
In case chiolite has been obtained the NaF:AlFg weight ratio can be corrected to fulfil the requirements set forth by the aluminium in¬ dustry using cryolite as a fluxing agent whereby chiolite or chiolite/ cryolite is granulated together with sodium carbonate to give a correct weight ratio, viz. 1.5.
Sodium fluoroaluminate can be prepared in a continuous process accord¬ ing to the present invention as well, whereby such a process will be exemplified below.
EXAMPLE 10
The combined solution identified (Ex 4) is stored in a buffer tank at 60°C -from where it is pumped to a first reaction vessel, from there to a second reaction vessel, from there to a third reaction vessel from which any precipitate formed is drawn off and allowed to settle in a fourth reaction vessel. The addition of the reactants can be made to the different reaction vessels in different orders depending on the final compound/product wanted.
The combined solution used in a series of tests of the continuous production contained as follows: F 12.0 g/1; Al 3.6 g/1; Si02 2.57 g/1; Ca 210 mg/1; 20g 60 mg/1. A1:6F molar ratio 1.26. Sodium chloride solution: 200 g NaCl/1. Technical grade of sodium carbonate.
– ~~

Test parameters
Test Add tion Addition Addition Addition Addition Reaction Cryolite Chiol of comb, of NaCl of NaCl of NaCl of temp solution solution to vessel to comb, Na2C03 solution to vessel no ml/m n ml/min no g/i no % %
1 170 16.7 1 20 50 93 7 2 170 16.4 2 20 50 40 60 3 173 16.3 1 20 60 S3 7 4 173 33.2
« 1 •40 50 100 0 5 170 Buffer 12 ,2,3 50 10 90 tank
170 15 1 18.8 60 17 83
Analyses of final products
Test H20 Na Al F Si02 P2°5 no 350°C % % % % %
1 3.11 31.1 12. .6 52.4 0.69 0.12
2 2.57 28.9 .13. .3 54.2 0.79 0.11
3 1.95 30.5 ■’• 12. .3 53.2 0.21 0.15
4 2.24 30.7 12. .5 52.8 0.46 0.12
5 3.00 26.5 14. ,5 53.5 – –
6 3.06 26.7 14.4 53.2 – –
Analyses of filtrate
Test -Na F Al Si02 P2°5 PH no g/i g/i g/i g/i mg/1
1 6.3 1.4 1.0 2.4 33 2.45
2 5.8 1.4 0.95 2.3 33 2.48
3 5.6 1.8 1.1 2.5 36 2.46
4χ) 12.1 0.12 0.05 3.4 25 2.50
5 5.0 1.6 0.6 2.3 35 2.43
6 4.8., 1.7 0.58 2.3 38 2.11 x) Cryolite suspension adjusted with hexafluorosilicic acid to A1/6F = 1.05 and sodium carbonate to pH 2, the contents prior to the adjustment being Na 12.1%; F 1.5%; Al 0.’95; Si022.2; pH 2.52.

Claims (1)

1. A method for recovering useable products from waste products de¬ riving from the manufacture of aluminium fluoride on the basis of
5 aluminium hydroxide and fluosilicic acid, characterized by adding alkali metal ions in the form of an alkali metal salt to collected mother liquors and washing water obtained in the manufacture of alu¬ minium fluoride and being contaminated with aluminium, silica, and fluorine, and adjusting the hydrogen ion concentration-of said col-
10 lected solution to a pH of 2.0 to 3.0 by adding an alkali metal base while maintaining a temperature of said collected solution of above about 50°C, isolating the alkali metal fluoroaluminate thereby pre¬ cipitated by filtration, whereafter the filtrate comprising mainly silica, and minor amounts of aluminium and fluorine is optionally
15 passed to a second step for the recovery of one or more of said compounds.
2. A method according to claim 1, characterized in that sodium hy¬ droxide and a sodium salt, preferably sodium sulfate and/or sodium
20 chloride are used in forming a sodium fluoroaluminate.
3. A method according to claim 1, characterized in that the pH is 2.0-2.5.
25. 4. A method according to claim 1, characterized in that the molar ratio of A1:6F in the collected solution is 1-1.25:1. .
– 5. A method according to claim 1, characterized in that the alumi¬ nium content of the reaction mixture is adjusted after addition of 30 the base and the alkali metal salt.
6. A method according to claim 5, characterized in that the alumi¬ nium content is increased after a first precipitation of fluoroalu- ‘ minate, to precipitate further fluoroaluminate from fluorine set 35 . free at said increase.

7. A method according to claim 1, characterized in that pH of the collected solution is controlled to be about pH 1 prior to adjusting it to pH 2.0-3.0.
8. A method according to claim 1, characterized in that the temper¬ ature is held between 50 and 90°C, preferably 60 to 80°C.
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<4> WIrO

AU10441/83A
1982-01-07
1982-12-21
A method for recovering useful products from waste products obtained when manufacturing aluminium hydroxide

Ceased

AU551374B2
(en)

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1982-01-07

SE8200045A

SE437015B
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1982-01-07
1982-01-07

PROCEDURE FOR THE RECOVERY OF APPLICABLE PRODUCTS FROM WASTE PRODUCTS CONCERNING MANUFACTURING ALUMINUM FLUORIDE

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1983-07-28

AU551374B2
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AU551374B2
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1986-04-24

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1982-01-07
1982-12-21
A method for recovering useful products from waste products obtained when manufacturing aluminium hydroxide

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CA1196173A
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SE439477B
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1982-10-13
1985-06-17
Boliden Ab

PROCEDURE FOR PRODUCING THE MAIN PURE SILICAR ACID FROM WASTE SILICON ACID

SE453078B
(en)

1986-09-09
1988-01-11
Alufluor Ab

PROCEDURE FOR IMPROVING CEMENT USE AND CONCRETE PROPERTIES

US5242670A
(en)

1992-07-02
1993-09-07
Gehringer Ronald C
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Assignee
Title

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(en)

1944-02-05
1950-02-20

GB762635A
(en)

1953-10-29
1956-11-28
Vaw Ver Aluminium Werke Ag
Process of producing cryolite from washing and waste liquors containing sodium fluoride

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1956-09-14
1959-12-08
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Artificial cryolite process

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1961-12-19
1965-03-30
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1966-11-22
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Process for the simultaneous production of Na3A1F6 and active SiO2

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1971-05-07
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Process for the co-deposition of aluminum and fluorine from aqueous solutions containing dilute silica

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1971-09-17
1974-04-10
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PROCEDURE FOR RECOVERING USEFUL PRODUCTS FROM WASTE PRODUCTS FROM ALUMINUM FLUORIDE PRODUCTION

1982

1982-01-07
SE
SE8200045A
patent/SE437015B/en
not_active
IP Right Cessation

1982-12-21
DE
DE8282850262T
patent/DE3272494D1/en
not_active
Expired

1982-12-21
AU
AU10441/83A
patent/AU551374B2/en
not_active
Ceased

1982-12-21
WO
PCT/SE1982/000434
patent/WO1983002444A1/en
active
IP Right Grant

1982-12-21
BR
BR8208048A
patent/BR8208048A/en
unknown

1982-12-21
US
US06/534,464
patent/US4560540A/en
not_active
Expired – Fee Related

1982-12-21
JP
JP83500171A
patent/JPS58502201A/en
active
Pending

1982-12-21
EP
EP82850262A
patent/EP0085287B1/en
not_active
Expired

1982-12-21
AT
AT82850262T
patent/ATE21238T1/en
not_active
IP Right Cessation

1982-12-30
CA
CA000418755A
patent/CA1196173A/en
not_active
Expired

1983

1983-01-06
YU
YU00018/83A
patent/YU1883A/en
unknown

1983-09-01
NO
NO833137A
patent/NO833137L/en
unknown

1983-09-06
FI
FI833184A
patent/FI71113C/en
not_active
IP Right Cessation

Also Published As

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Publication date

NO833137L
(en)

1983-09-01

BR8208048A
(en)

1983-11-22

FI71113C
(en)

1986-11-24

EP0085287B1
(en)

1986-08-06

SE437015B
(en)

1985-02-04

FI71113B
(en)

1986-08-14

SE8200045L
(en)

1983-07-08

AU1044183A
(en)

1983-07-28

JPS58502201A
(en)

1983-12-22

US4560540A
(en)

1985-12-24

FI833184A0
(en)

1983-09-06

DE3272494D1
(en)

1986-09-11

CA1196173A
(en)

1985-11-05

WO1983002444A1
(en)

1983-07-21

ATE21238T1
(en)

1986-08-15

YU1883A
(en)

1986-02-28

FI833184A
(en)

1983-09-06

EP0085287A1
(en)

1983-08-10

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