This invention relates to a lime glass batch composition and, especially to a lime glass batch comprising silicon, calcium, magnesium and aluminium, as well as a process for manufacturing flat lime glass sheets by melting the same composition.
There is known by U.S. Pat. No. 6,287,997 a method of producing a glass by mixing silica sand with a synthetic silicate and heating at about 1300-1400° C. to obtain molten glass. The synthetic silicate is a preheated mixture of a source of calcium and/or magnesium with a source of silicon dioxide.
In that known method, no glass comprising aluminum is obtained.
According to a first aspect, the invention provides a lime glass batch composition as defined in claim 1.
According to a second aspect, the invention provides a process for the manufacture of flat lime glass sheets as defined in claim 16.
Dependent claims define further preferred embodiments of the invention.
The present invention may provide one or more of the following advantages:
The lime glass batch composition according to the invention comprises batches suitable for the manufacture of any glass comprising calcium. Examples of those glasses are: soda-lime glass, boron glass, special glasses comprising arsenic, barium, strontium and/or zirconium, like those used for optical mirrors and lenses, for flat displays, etc.
The lime glass batch composition according to the invention is a mixture of silica sand, limestone, dolomite and a source of alumina wherein at least part of at least one of the limestone and the dolomite is replaced by a synthetic aluminosilicate of calcium and magnesium (hereafter referred to as “Ca—Mg—Al silicate”). The composition of that Ca—Mg—Al silicate, expressed in weight % of dry synthetic Ca—Mg—Al silicate, is as follows:
In that batch composition, the source of alumina may comprise various Al containing compounds. Those Al compounds may be found in the nature as Al ores, like feldspar, nepheline and aluminum oxide. They may as well be synthetic compounds, resulting from a chemical treatment or being a by-product of another chemical or industrial process, like aluminum hydroxide and slag providing from steel factories. The source of alumina may consist of one single member of those Al compounds. Alternatively, it may as well comprise a mixture of two or more of those members.
In an advantageous embodiment of the invention, the source of alumina may as well be replaced, at least in part, by the synthetic Ca—Mg—Al silicate. Batch compositions wherein only part of the source of alumina has been replaced by synthetic Ca—Mg—Al silicate are preferred.
In another embodiment, which is compatible with the previous one, the synthetic Ca—Mg—Al silicate is a mixture of tri-Ca silicate Ca3SiO5 (or 3CaO.SiO2), bi-Ca silicate Ca2SiO4 (or 2CaO.SiO2), tri-Ca aluminate Ca3Al2O6 (or 3CaO.Al2O3) and a small proportion of MgO not exceeding 3 wt. % of the mixture. Generally, Ca3SiO5, Ca2SiO4 and/or Ca3Al2O6 are present into their crystallised form.
In that embodiment, especially preferred are the synthetic Ca—Mg—Al silicates wherein tri-Ca aluminate Ca3Al2O6 is present both as a crystallised product and as an amorphous product. Most preferred are the batches wherein the crystallised weight proportion of the Ca3Al2O6 is at least 60% of the total weight of the Ca3Al2O6.
In another interesting embodiment of the invention, which is as well compatible with the previous embodiments, part of the aluminum may be replaced by iron. In that embodiment, no more than 50 weight % of the aluminum may preferably be replaced by iron. According to that embodiment, iron may be present under the form of tetra-Ca alumino-ferrite Ca4Al2Fe2O10, or 4CaO.Al2O3.Fe2O3. In the batch composition, Ca4Al2Fe2O10 may be present into a crystallised form and/or an amorphous form. The weight proportion of the crystallised form may vary from 20 to 90% of the total Ca4Al2Fe2O10 weight.
In any of the previous embodiments, each one of the Ca3SiO5, Ca2SiO4, Ca3Al2O6 and Ca4Al2Fe2O10 species may be anhydrous, i.e. that they are not linked with any chemical water or do not physically retain any absorpted water on their surface. Each species may as well be present under both anhydrous and hydrated form. Preferably, all the species carry only a tiny content of water with them in the composition, not more than 10% of their total dry weight. Most preferably, all the species in the composition are anhydrous and completely free of water.
According to another preferred embodiment, the synthetic Ca—Mg—Al silicate in the batch composition is a cement clinker.
According to another embodiment, compatible as well with the previous ones, the batch composition comprises a flux. Preferably, the flux present into the composition is selected from sodium, potassium, lithium, boron, barium, arsenic, phosphorus and vanadium compounds. A mixture of several of those compounds may as well be selected as flux into the composition.
A preferred flux is soda ash, under the form of anhydrous Na2CO3. That flux is most preferred for the manufacture of soda-lime glass.
Besides the components detailed above, the batch composition according to the invention may also comprise common glass additives. Those additives are well known compounds used in glass making and fulfil the functions of colorants, oxidants, reductors, viscosity modifiers and fining agents. They are generally present in the batch mixture in minor proportions, lower than 4 wt. % each, and preferably lower than 2 wt. % each. Examples of those additives are, non-limitatively: Na2SO4, NaNO3, Fe2O3, TiO2, a rare earth oxide, C, a salt of Co, of Cr, of Cu, of Se, of Mn, of a rare earth, Mn oxides, V2O5 and Se. Several additives may be used together in the batch composition. Preferably, coloring additives are selected from at least one of a cobalt compound, a vanadium compound, a chromium compound, a manganese compound, a selenium compound and a rare earth compound.
In a second aspect, the invention provides a process for the manufacture of flat lime glass sheets by melting the batch composition according to the invention in a glass furnace, refining the melted batch, floating a ribbon of the melted glass composition on a liquefied tin bath to form a continuous flat glass ribbon, cooling it progressively, solidifying and annealing it, and finally cutting the solidified flat glass ribbon into separated flat glass sheets.
In that process, the synthetic aluminosilicate of calcium and magnesium may be added together with the other components. Alternatively, this Ca—Mg—Al silicate may be added to the batch separately, at least one particular location of the furnace. Ca—Mg—Al silicate is preferably introduced into the furnace under the form of particles of up to about 4 mm of diameter.
The invention relates as well to a flat soda-lime glass sheet manufactured by the process comprising the batch composition according to the invention.
The single FIGURE is a graph comparing rates of melting (time in minutes and % unmelted).
The invention will now be illustrated below by examples aiming at better describing the invention, without by no means trying to limit its scope.
Melting experiments have been performed in a laboratory electrical furnace using transparent quartz crucibles. A digital CCD camcorder has continuously recorded a melting materials area picture through the crucible walls and the pictures taken have been analysed with the aid of LUCIA software, from the Czech Laboratory Imaging company, in order to compute the percentage amount of the observed area which was not already melted into glass.
Three different batch compositions have been tested, results of which are given in Table 2 and
Raw materials components and calculated chemical compositions of the two batches 1R and 2 are given in Table 1 below and show that experiments have been designed so as to keep constant that composition across the batches.
It can be seen from Table 2 and
Number | Date | Country | Kind |
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06114866.4 | Jun 2006 | EP | regional |
This application is the entry into the United States of PCT Application number PCT/EP2007/055401 filed Jun. 1, 2007 and claims priority from European application EP 06114866.4 filed Jun. 1, 2006, the entirety of each of which is hereby incorporated by reference.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP2007/055401 | 6/1/2007 | WO | 00 | 11/26/2008 |