Process for cold hydrochemical decomposition of sodium hydrogen aluminosilicate

Abstract

A process for cold hydrochemical decomposition of sodium hydrogen aluminosilicate. The process includes decomposing sodium hydrogen aluminosilicate at low temperature with a chelate to form a solution of soluble compounds and insoluble contaminants; separating the insoluble contaminants from the solution with a coagulator and heating to coagulate the silicic acid and form a silicic acid gel; separating the silicic acid gel to form a silicic acid-free solution; decomposing the silicic acid-free solution to form a precipitate of sodium hydrogen carboaluminate and a mother liquor; separating the precipitate from the mother liquor; concentrating, cooling and regenerating the mother liquor and forming sodium hydrogen carbonate; separating the sodium hydrogen carbonate from the regenerated solution; and calcining the sodium hydrogen carboaluminate at a temperature of about 700 to about 900° C. and forming sodium aluminate.

Claims

1. A process for cold hydrochemical decomposition of sodium hydrogen aluminosilicate, comprising: decomposing the sodium hydrogen aluminosilicate at a low temperature of less than about 100° C. with a circulating solution of chelate in the presence of a weak acid to form a solution comprising soluble compounds comprising an aluminum chelate, a silicic acid and a sodium salt of the weak acid, and insoluble contaminants, separating the insoluble contaminants from the solution by adding a coagulator to the solution and heating the solution to a temperature of about 100 to about 120° C. to coagulate the silicic add and form a silicic acid gel, separating the resulting silicic acid gel from the solution to form a silicic acid-free solution; decomposing the silicic acid-free solution by treating with an excess of sodium hydrogen carbonate to form a precipitate of sodium hydrogen carboaluminate and a mother liquor; separating the precipitate of sodium hydrogen carboaluminate from the mother liquor; concentrating the mother liquor by evaporation; cooling the concentrated mother liquor and regenerating the cooled solution by carbonization with gaseous carbon dioxide under a pressure of at least about 16 bar to form a precipitate of sodium hydrogen carbonate; separating the precipitate of sodium hydrogen carbonate from the regenerated solution; and calcining the sodium hydrogen carboaluminate at temperature of about 700 to about 900° C. and forming sodium aluminate.

2. The process according to claim 1, wherein the chelate comprises at least one component selected from the group consisting of sodium salts of ethylenediaminetetraacetic add and ethylenediaminetetraacetic acid.

3. The process according to claim 1, wherein the step of decomposing the sodium hydrogen carboaluminate is at a temperature of about 20 to about 45° C.

4. The process according to claim 1, comprising decomposing the aluminium chelate by treatment with a stoichiometric excess of about 30 to about 100% of sodium hydrogen carbonate.

5. The process according to claim 1, wherein the step of separating the silicic acid gel comprises using a circulating solution of seed crystals of silicic acid gel.

6. The process according to claim 1, wherein the step of separating the precipitate of hydrogen carboaluminate comprises using a circulating solution of seed crystals of hydrogen carboaluminate.

7. The process according to claim 1, comprising regenerating the chelate, the weak acid and the sodium hydrogen carbonate and using the regenerated chelate, weak acid and sodium hydrogen carbonate as circulating products.

8. The process according to claim 1, wherein the separated silicic acid gel is adapted for a commercial product.

9. The process according to claim 1, comprising decomposing the insoluble contaminants to form an iron ore product suitable for smelting pig iron to titanium slag.

10. The process of claim 9, wherein the insoluble contaminants comprise red mud.

11. The process of claim 1, wherein the low temperature is about 25° C.

12. The process of claim 1, wherein the sodium aluminate is supplied to a process for forming alumina.

13. The process of claim 12, wherein the process is a Bayer process.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The accompanying drawings, which are incorporated into and constitute a part of this specification, illustrate one or more example aspects of the present disclosure and, together with the detailed description, serve to explain their principles and implementations.

(2) FIG. 1 shows a method for processing red mud according to various example aspects of the invention;

(3) FIG. 2 shows a method of alkaline hydrochemical processing of clay to form alumina according to various example aspects of the invention;

(4) FIG. 3 shows a method of hydrochemical alkaline processing of clay to form alumina according to various example aspects of the invention.

DETAILED DESCRIPTION

(5) According to various example aspects of the invention, crystalline sodium hydrogen aluminosilicate may be decomposed at low temperature with the help of a circulating chelate, for example, with an aqueous solution of a mixture of the sodium salt of ethylenediaminetetraacetic acid and a weak acid. The decomposition of sodium hydrogen aluminosilicate produces the soluble compounds of aluminium chelate, silicic acid and the sodium salt of a weak acid as follows:
Na.sub.2Al.sub.2ASi.sub.2O.sub.82H.sub.2O+2Na.sub.xH.sub.(4-x)edta+2x/yH.sub.yA.fwdarw.2Na[Al edta]+2H.sub.4SiO.sub.4+2x/yNa.sub.yA+2H.sub.2O   [1]
in which A is the anion of a weak add, x is the degree of substitution of the hydrogen atoms of the carboxyl group of the ethylenediaminetetraacetic acid by the sodium atoms, and may be 1, 2, 3 or 4, y is the basicity of the weak add and may be 1 or 2.

(6) A coagulant may then be added to the resulting solution which may be heated to coagulate the silicic acid and form a gel. The obtained silicic acid gel may then be separated from the solution and aluminium chelate decomposed by treating the solution with excess sodium hydrogen carbonate as follows:
Na[Al dta]+4NaHCO.sub.3⇄NaAl[CO.sub.3](OH).sub.2↓+Na.sub.4edta+3CO.sub.2+H.sub.2O   [2]

(7) Decomposition of the aluminum chelate produces a precipitate of sodium hydrogen carboaluminate and a mother liquor of the chelate. The sodium hydrogen carboaluminate precipitate may then be separated from the mother liquor. The latter may be subsequently evaporated, cooled and regenerated by carbonization under pressure with gaseous carbon dioxide; the sodium hydrogen carbonate crystallizes out and is separated from the solution as follows:
Na.sub.4edta+(4−x)CO.sub.2+(4−x)H.sub.2O.fwdarw.Na.sub.xH.sub.(4-x)edta+(4−x)NaHCO.sub.3↓  [3]
NayA+yCO.sub.2+yH.sub.2O=H.sub.yA+yNaHCO.sub.3η  [4]

(8) The regeneration products, that is, the solution of the chelate and the weak acid as well as the sodium hydrogen carbonate may be circulating products.

(9) The sodium hydrogen carboaluminate may then be calcined to form sodium aluminate as follows:
NaAl[XO.sub.3](OH).sub.2.fwdarw.NaAlO.sub.2+H.sub.2O↑+CO.sub.2↑  [5]

(10) The sodium aluminate may be dissolved in the aluminate solution and then fed back for production of alumina by the Bayer process.

(11) The following schemes illustrate examples for carrying out the invention:

EXAMPLE 1

Red Mud Processing (see FIG. 1)

(12) Composition of a solid phase of the red mud:
Na.sub.2O—12.8%, Al.sub.2O.sub.3—18.6%, SiO.sub.2—19.2%, Fe.sub.2O.sub.3—33.9%, TiO.sub.2—4.3%.

(13) The solid phase of the red mud was decomposed under the following conditions: circulating chelate solution: concentration of the disodium salt of ethylenediaminetetraacetic acid: 120 g/dm.sup.3 and concentration of the acetic acid: 7%, temperature: 25° C., decomposition time: 3 hours, ratio liquid phase: solid phase: 10:1.

(14) The liquid phase of the reaction products was filtered off from the insoluble precipitate.

(15) Composition of the precipitate (iron one product) was as follows: Na.sub.2O—0.31%, Al.sub.2O.sub.3—4.70%, SiO.sub.2—3.40%, Fe.sub.2O.sub.3—75.3%, TiO.sub.2—7.3%.

(16) The extraction of the solid phase of the red mud into the liquid phase produced Na.sub.2O—98.8%, and Al.sub.2O.sub.3—89.0% respectively.

(17) The liquid phase was then held at a temperature of 120° C. for 2 hours in order to coagulate the silicic acid to form a gel.

(18) The resulting silicic acid gel with the following composition: Na.sub.2O—1.5%, Al.sub.2O.sub.3—1.4% and SiO.sub.2—77.9% was filtered off and the silicon-free solution was then decomposed at 90° C. by treatment with a 30% stoichiometric excess of a sodium hydrogen carbonate solution. The decomposition formed a precipitate of sodium hydrogen carboaluminate of the following composition: Na.sub.2O—20.4%, Al.sub.2O.sub.3—34.4%, SiO.sub.2—0.4% und Fe.sub.2O.sub.3—0.03%. This precipitate was then filtered off and calcined at a temperature of 700° C. for 30 minutes. The resulting sodium aluminate had the following composition: Na.sub.2O—36.3%, Al.sub.2O.sub.3—62.2%, SiO.sub.2—0.8% and Fe.sub.2O.sub.3—0.1%.

EXAMPLE 2

Alkaline Hydrochemical Processing of Clay to Alumina (see FIG. 2)

(19) FIG. 2 shows a method for alkaline hydrochemical processing of clay to form alumina, where the weak acid is carbonic acid.

(20) A batch of clay with the composition Na.sub.2O—0.25%, Al.sub.2O.sub.3—37.50%, SiO.sub.2—44.80%, Fe.sub.2O.sub.3—1.59% and TiO.sub.2—2.51% was leached out with a solution of caustic liquor under the following conditions: concentration of Na.sub.2O.sub.ky: 120 g/dm.sup.3, ratio liquid phase: solid phase: 7:1, leaching time: 5 hours, leaching temperature: 102° C.

(21) The solid phase formed during the leaching process was filtered off and washed. The chemical composition of the solid phase of the leaching product from the clay was as follows: Na.sub.2O—19.0%, Al.sub.2O.sub.3—29.70%, SiO.sub.2—36.30%, Fe.sub.2O.sub.3—1.50% and TiO.sub.2—2.50%. Composition of the material constituent was: principally sodium hydrogen aluminosilicate (NA.sub.2Al.sub.2Si.sub.2O.sub.82H.sub.2O).

(22) The sodium hydrogen aluminosilicate was decomposed under the following conditions: circulating chelate solution: concentration of the disodium salt of ethylenediaminetetraacetic acid: 100 g/dm.sup.3, ratio liquid phase: solid phase: 10:1, temperature: 25° C., CO.sub.2 pressure 40 bar, decomposition time: 4 hours.

(23) The liquid phase of the reaction products was separated from the insoluble contaminated precipitate and held under a CO.sub.2 pressure of 16 bar at a temperature of 120° C. for 2 hours in order to coagulate the silicic acid. The resulting silicic acid gel with the composition: SiO.sub.2—84.60%, Al.sub.2O.sub.3—0.63%, Na.sub.2O—1.15% was filtered off and the silicon-free solution was then decomposed at 25° C. by treatment with a 30% stoichiometric excess of a sodium hydrogen carbonate solution.

(24) The sodium hydrogen carboaluminate precipitate was filtered off from the solution. The composition of the precipitate was as follows: Na.sub.2O—21.40%, Al.sub.2O.sub.3—36.80%, SiO.sub.2—0.81%. The sodium hydrogen carboaluminate was calcined at a temperature of 700° C. for 0.5 hours. The resulting sodium aluminate had the following composition: Na.sub.2O—35.80%, Al.sub.2O.sub.3—61.50%, SiO.sub.2—1.40%.

EXAMPLE 3

Hydrochemical Processing of Clay to Alumina (see FIG. 3)

(25) FIG. 3 shows a method for alkaline hydrochemical processing of clay to form alumina, where the weak acid is acetic acid.

(26) The batch of clay was leached out as in Example 2.

(27) The sodium hydrogen alumonate was decomposed under the following conditions: circulating chelate solution: concentration of the disodium salt of ethylenediaminetetraacetic acid 100 g/dm.sup.3 and concentration of acetic acid 7%, temperature: 25° C., decomposition time: 1.5 hours.

(28) The liquid phase of the reaction products was filtered off from the insoluble contaminated precipitate and held at a temperature of 120° C. within 2 hours in order to coagulate the silicic acid. The resulting silicic acid gel with the composition as follows: SiO.sub.2—83.50%, Al.sub.2O.sub.3—0.50%, Na.sub.2O—0.60%, Fe.sub.2O.sub.3—0.05% was filtered off and the silicon-free solution was decomposed at 90° C. by treatment with a 30% stoichiometric excess of a sodium hydrogen carbonate solution.

(29) The sodium hydrogen carboaluminate precipitate was separated from the solution by filtration. Composition of the precipitate was as follows: Na.sub.2O—21.30%, Al.sub.2O.sub.3—36.70%, SiO.sub.2—0.51%. The sodium hydrogen carboaluminate was calcined at a temperature of 700° C. for 0.5 hours. The resulting sodium aluminate had the following composition: Na.sub.2O—35.9%, Al.sub.2O.sub.3—62.0%, SiO.sub.2—0.83%.

(30) In the interest of clarity, not all of the routine features of the aspects are disclosed herein. It win be appreciated that in the development of any actual implementation of the present disclosure, numerous implementation-specific decisions must be made in order to achieve the developer's specific goals, and that these specific goals will vary for different implementations and different developers. It will be appreciated that such a development effort might be complex and time-consuming, but would nevertheless be a routine undertaking of engineering for those of ordinary skill in the art having the benefit of this disclosure.

(31) Furthermore, it is to be understood that the phraseology or terminology used herein is for the purpose of description and not of restriction, such that the terminology or phraseology of the present specification is to be interpreted by the skilled in the art in light of the teachings and guidance presented herein, in combination with the knowledge of the skilled in the relevant art(s). Moreover, it is not intended for any term in the specification or claims to be ascribed an uncommon or special meaning unless explicitly set forth as such.

(32) The various aspects disclosed herein encompass present and future known equivalents to the known modules referred to herein by way of illustration. Moreover, while aspects and applications have been shown and described, it would be apparent to those skilled in the art having the benefit of this disclosure that many more modifications than mentioned above are possible without departing from the inventive concepts disclosed herein.