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| United States Patent | 6043175 |
| Link to this page | http://www.wikipatents.com/6043175.html |
| Inventor(s) | Kulev; Gennady Ivanovich (Pskov, RU); Malinovski; Leonid Glebovich (Moscow, RU); Shvarev; Ivan Pavloivich (Loboya, RU); Miroevsky; Piotr Ravelevich (Moscow, RU) |
| Abstract | Disclosed is a binding solution comprising silicon dioxide fines in an
aqueous medium, the fines being substantially spherical in shape. The
binding solution has a pH from about 9.5 to about 11. A grinder, which may
be used to prepare the binding solution and a product, which may be
prepared from the binding solution are also disclosed. |
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Title Information  |
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Drawing from US Patent 6043175 |
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Method and apparatus for producing a silicon based binding composition
and product prepared therefrom |
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| Publication Date |
March 28, 2000 |
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| Priority Data |
Dec 08, 1992
[RU]
92010795
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Title Information  |
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References  |
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Market Review  |
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Technical Review  |
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Claims  |
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It is claimed:
1. A binding solution comprising silicon dioxide fines, orthosilicic acid sol and water, a majority of said fines being generally spherical in shape, said orthosilicic acid sol
surrounding said fines, said solution having an alkaline pH, said orthosilicic acid sol being present at a level of concentration of at least about 10 g/l, and said binding solution being substantially free of iron.
2. The binding solution as claimed in claim 1 wherein said pH varies from about 9.5 to about 11.
3. The binding solution as claimed in claim 1 wherein said pH varies from about 9.8 to about 10.5.
4. The binding solution as claimed in claim 1 wherein said concentration is greater than about 20 g/l.
5. The binding solution as claimed in claim 2 wherein a majority of said fines have a diameter less than about 0.30 mm.
6. The binding solution as claimed in claim 5 wherein a majority of said fines have a diameter less than about 0.17 mm.
7. A method for preparing the binding solution of claim 1, the method comprising subjecting a feedstock containing silicon dioxide to at least one shearing force in the presence of an aqueous alkaline medium containing free hydroxyl ions at an
elevated temperature to produce silicon dioxide particles that are generally spherical in shape, said elevated temperature being at least about 55 degrees C.
8. The method as claimed in claim 7 wherein said shearing force comprises a shearing force to smooth the exterior surface of the silicon dioxide.
9. The method as claimed in claim 8 wherein said shearing force comprises two shearing forces to smooth the exterior surface of the silicon dioxide, the first shearing force being a tangential shearing force, and the second shearing force being
substantially perpendicular to said tangential shearing force.
10. The method as claimed in claim 7 wherein the pH of said alkaline medium is from about 9.5 to about 11.
11. The method as claimed in claim 8 wherein the pH of said alkaline medium is from about 9.8 to about 10.5.
12. The method as claimed in claim 7 wherein said temperature is from about 60.degree. to about 80.degree. C.
13. The method as claimed in claim 7 wherein, when said feedstock containing silicon dioxide and said aqueous alkaline medium are first subjected to said shearing force, said feedstock and medium have a humidity of from about 20% to about 30%.
14. The method as claimed in claim 12 wherein said feedstock comprises more than about 75% silicon dioxide.
15. The method as claimed in claim 14 wherein said feedstock comprises more than about 85% silicon dioxide.
16. The method as claimed in claim 14 wherein said fines are generally spherical in shape and a majority of said fines have a diameter less than about 0.3 mm.
17. The method as claimed in claim 16 wherein a majority of said fines have a diameter less than about 0.17 mm.
18. The method as claimed in claim 7 wherein said binding solution comprises discrete particles of an orthosilicic acid sol surrounding silicon dioxide particles.
19. The method as claimed in claim 18 wherein the concentration of said orthosilicic acid sol is greater than about 10 g/l.
20. A ceramic product prepared by:
(a) preparing a mixture of a filler and a binding solution comprising silicon dioxide fines, orthosilicic acid sol and water, a majority of said fines being generally spherical in shape, said orthosilicic acid sol surrounding said fines, said
solution having an alkaline pH, said orthosilicic acid sol being present at a level of concentration of at least about 10 g/l, and said binding solution being substantially free of iron;
(b) mixing said solution and said filler;
(c) shaping said mixture; and
(d) curing said mixture at an elevated temperature to remove water from said mixture, said curing being sufficient to bring the pH of said product within the range of between about 6 and about 7.5.
21. The ceramic product as claimed in claim 20 wherein the step of shaping said mixture comprises introducing said mixture into a mould.
22. The ceramic product as claimed in claim 21 wherein said mixture contains less than about 5 wt % water.
23. The ceramic product as claimed in claim 20 wherein said mixture comprises about 1.5 wt % water.
24. The ceramic product claimed in claim 22 wherein said mixture comprises from about 20 to about 35 wt % binding solution based on the weight of the filler.
25. The ceramic product as claimed in claim 22 wherein said mixture comprises up to about 50 wt. % binding solution based on the weight of said filler.
26. The ceramic product as claimed in claim 22 wherein said mixture is cured by subjecting said mixture to microwave energy.
27. The ceramic product as claimed in claim 25 wherein said mixture is compacted in a mould prior to curing step (d).
28. The ceramic product as claimed in claim 25 wherein said mould comprises the extruder port of an extruder.
29. A method of producing a ceramic product comprising:
(a) preparing a mixture of a filler and a binding solution comprising silicon dioxide fines, orthosilicic acid sol and water, a majority of said fines being generally spherical in shape, said orthosilicic acid sol surrounding said fines, said
solution having an alkaline pH, said orthosilicic acid sol being present at a level of concentration of at least about 10 g/l, and said binding solution being substantially free of iron;
(b) shaping said mixture; and
(c) curing said mixture at an elevated temperature to remove water from said mixture, and bringing the pH of said mixture to a substantially neutral level.
30. The method of producing a ceramic product as claimed in claim 29 wherein the step of shaping said mixture comprises introducing said mixture into a mould.
31. The method of producing a ceramic product as claimed in claim 30 wherein said mixture contains less than about 5 wt % water.
32. The method of producing a ceramic product as claimed in claim 31 wherein said mixture comprises about 1.5 wt % water.
33. The method of producing a ceramic product as claimed in claim 31 wherein said mixture comprises from about 20 to about 35 wt % binding solution based on the weight of the filler.
34. The method of producing a ceramic product as claimed in claim 31 wherein said mixture comprises up to about 50 wt % binding solution based on the weight of said filler.
35. The method of producing a ceramic product as claimed in claim 34 wherein said mould comprises the extruder port of an extruder.
36. The method of producing a ceramic product as claimed in claim 34 wherein mixture is cured by subjecting said mixture to microwave energy.
37. The method of producing a ceramic product as claimed in claim 34 wherein said mixture is compacted in said mould prior to curing step (d). |
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Claims  |
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Description  |
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FIELD OF THE INVENTION
This invention relates to the manufacture of silicon based binding compositions from silica. In particular, the invention relates to binding compositions which are prepared by the wet grinding of silica in an alkaline medium and products which
may be prepared from the binding composition. In addition, this invention relates to the apparatus which may be used to prepare the binding composition.
BACKGROUND OF THE INVENTION
Ceramics may generally be defined as products manufactured by the action of heat on earthy raw materials in which silicon with its oxide and silicates occupy a predominant position. Various types of products are made from ceramics including
structural clay products (such as brick, tile, terra cotta and glazed architectural brick); whitewares (such as dinnerware, chemical and electrical porcelain, sanitary ware and floor tile); glass products of all types; porcelain enamels; refractories;
Portland cement, lime, plaster and gypsum products; abrasive materials such as fused alumina, silicon carbide and related products; and, aluminum silicate fibres.
Clay based ceramic products have become a staple in many areas of industry including the construction industry. In particular, structural clay products are used extensively in the construction of buildings.
Accordingly, one disadvantage of structural clay products is that an extensive amount of time is required to produce a single product. Further, large amounts of energy must be utilized during the baking process in the kiln. Typically, in order
for a manufacturing plant to be economically efficient, kilns having a capacity to simultaneously bake a large quantity of bricks are required. In addition, manufacturing plants tend to be located near the source of the clay, thus increasing the cost of
transporting the bricks to the construction site where they will be used.
More recently, silicate based material has been utilized to produce bricks. For example, calcium silicate bricks may be prepared by grinding lime together with sand to produce a lime-silica bonding adhesive, mixing this adhesive with sand,
pressing the mixture of sand and bonding adhesive into a mold and baking the mixture in an autoclave. Calcium silicate bricks may be utilized in place of more conventional clay bricks in the construction industry.
One disadvantage with calcium silicate bricks is the amount of time required to produce a single brick. In addition, a large amount of processing equipment and power input is required to produce calcium silicate bricks.
Binding compositions have also been prepared by the wet grinding of sand in an alkaline medium. According to the method disclosed in U.S.S.R. Author's Priority Certificate No. 992487, sand is ground in a ball mill in an alkaline medium (pH
9.0-10.5) to produce a silica based binding composition. The feedstock is divided into three portions. The first portion, which comprises 50% of the feedstock of sand, is milled for 6 hours. In the presence of a waterglass having a pH of 10.5. The
second portion, which comprises 25% of the initial feedstock, is then combined with the milled feedstock and the mixture is milled for 7 hours. The third portion, which comprises 25% of the initial feedstock, is added to this milled product and this
mixture is then milled for an additional 12 hours. One disadvantage of this method is that each batch requires 24 hours of milling time. This reduces the potential throughput of the process. In addition, the lengthy grinding time increase the wear of
the components of the ball mill and substantially decrease the lifetime of the ball mill. In addition, the product produced by this method may not have sufficient compressive strength for use in some applications.
SUMMARY OF THE INVENTION
According to the instant invention, a binding composition comprising silica is prepared by fractionating a silicon feedstock in the presence of an alkaline medium to produce fines that are substantially spherical in shape. The fines are
surrounded by a layer of orthosilicic acid sol. Preferably, the binding solution has no or substantially no iron therein. The binding solution may contain from about 25 to about 0 ppm iron, more preferably from about 15 to about 0 and, most preferably,
from about 10 to about 0 ppm iron.
The binding solution may be prepared by passing the silica through one or more grinders. Preferably, at least two grinders are utilized. In the first grinder, preliminary grinding of the silica feed material is undertaken and a dispersed mass
of silica in an alkaline medium is formed. This dispersed mass is continuously fed into a second grinder where the silica particles are ground to the required level of fineness and the binding solution in produced. The grinding is conducted so as to
shear the silicon dioxide and to achieve a high degree of fractionation of the silica particles so as to produce a highly uniform binding solution.
In accordance with the instant invention, the binding solution may be prepared in a grinder having first and second frusto conical sections. The second frusto conical section is coaxially mounted within the first frusto conical section. The
second frusto conical section rotates relative to first frusto conical section. The binding solution is passed through the work zone between the first and second frusto conical sections. During its passage through this work zone, the silica is ground
to the desired size. As will be appreciated by those skilled in the art, each grinder has an optimum size reduction of particles which may be achieved. Accordingly, depending upon the feed size of the feed material, one, two or more grinders may be
required.
If more than one grinder is required, then the final grinder may have a plurality of conical spindles positioned in the working zone of the grinder. The apex of the conical spindles is positioned adjacent the discharge end of the grinder. The
work zone of the grinder narrows from the entrance to the work zone to the discharge end of the work zone. The work zone narrows at a greater rate than the conical spindles. Accordingly, the apex of the conical spindles is in contact with the grinding
surfaces of the first and second conical sections while the end of the conical spindles distal to the apex of the spindles will not be in contact with both of these surfaces. The conical spindles act as additional grinding surfaces to fracture the
silica particles as they pass through the work zone.
One advantage of the instant invention is that a binding solution is prepared in a substantially shorter amount of time than has been achieved using a ball mill. In particular, a binding solution may be prepared in about one to two hours whereas
approximately twenty-four hours have been required utilizing ball mills.
The binding solution of the instant invention may also be utilized to produce a finished product such as a brick. According to the process, the binding solution is intimately mixed with a filler. Preferably, the filler is sheared in the
presence of the binding solution such as by passing the filler and binding solution through a grinder similar to the final grinder described above wherein the spindles have been removed. The prepared mixture is then compacted into a mould and cured. By
varying the filler or mixture of fillers, a variety of products having a wide range of performance characteristics including high compressive strength, high yield strength, good acid r | | |