Method of reducing the amount of lithium in glass production

Information

  • Patent Grant
  • 6531421
  • Patent Number
    6,531,421
  • Date Filed
    Monday, June 11, 2001
    23 years ago
  • Date Issued
    Tuesday, March 11, 2003
    21 years ago
Abstract
A method is provided for producing a glass batch. The method involves use of a calcium magnesium silicate as a batch component substitution for a lithium melting aid. The amount used is effective to produce a beneficial viscosity character and reduced batch free time.
Description




FIELD OF THE INVENTION




The present invention relates to glass batch forming methods. In particular, it relates to a method wherein a calcium magnesium silicate is substituted for lithium as a melting aid in glass batches.




BACKGROUND




Glass batches can contain certain materials as melting aids. These aids assist in creating a homogeneous batch having complete reactions and performed at lower melting temperatures or times. One such melting aid is lithium, which while effective is relatively expensive to use. There remains a need to further develop useful melting aids which can be used in conjunction with or in the absence of lithium compounds.




SUMMARY




One object of the present invention is a method of producing a glass batch composition having favorable viscosity characteristics. Another objective is to provide a melting aid for a glass batch which can work in conjunction with or as a partial or total replacement for lithium melting aids. These and other objectives are achieved by a method of forming a glass batch composition by the admixing of a calcium magnesium silicate composition.




DESCRIPTION OF PREFERRED EMBODIMENTS




One embodiment of the present invention is a method of producing a glass batch composition composed of a calcium magnesium silicate and other glass components to produce a glass batch. The glass batch composition is then melted to form a melted glass batch composition. The amount of said calcium magnesium silicate used is selected effectively to produce a viscosity character and batch free time in the glass batch composition less than or equal to that which results from use of an equivalent amount of a lithium compound in a comparative glass batch. An equivalent amount is the use of the same mass percent of the calcium magnesium silicate or lithium compound in the total glass batch before heating.




The calcium magnesium silicate of the present invention can be a natural resource or one attained by synthetic production. A preferred calcium magnesium silicate compound is that described in U. S. Pat. No. 6,211,103 B1 (Fairchild, et al.). A more preferred calcium magnesium silicate has an empirical formula of Ca


x


Mg


y


SiO


2


, and the values of x and y are independently from about 0.1 to about 0.6 and z is a value to balance the oxidation state of the compound.




The respective amounts of the calcium magnesium silicate compound and other glass components is dependent upon the glass formula being produced. As used herein, the term “comparative glass batch” or “comparative glass product” means a glass batch or product which is equivalent in oxide values, except that the value of boron oxide equivalent is less for an embodied glass product made with the present invention than that made with known processes which do not use a calcium magnesium silicate compound as described herein. It has been unexpectedly discovered that by using the calcium magnesium silicate compound described herein that less lithium values are needed to attain the same or better result as the amount used in known methods. Accordingly, a preferred method is one in which the other batch components comprise less than about one percent by total batch weight of lithium. It was further unexpectedly found that in the method using calcium oxide silicate compounds to reduce the amount of lithium needed for a particular purpose, that the use of an embodied calcium magnesium silicate compound enabled as a preferred method to reduce the amount of said magnesium oxide compound to about zero.




The amount of the calcium magnesium silicate compound used can be adjusted so that the viscosity of the formed glass batch is at least about ten percent less than that of the comparative glass batch. Similarly, the amount of the calcium magnesium silicate compound used can be adjusted so that the batch free time of the formed glass batch is at least about ten percent less than that of the comparative glass batch.




In a preferred method, an amount of feldspathic compound can be combined with the calcium magnesium silicate compound to achieve similar results. In another preferred embodiment, the above method is modified by the additional mixing of a feldspathic component. Such feldspathic material can be of one of any of the numerous material or synthetic forms of feldspar or feldspar-type material. Such feldspathic material is an aluminosilicate with barium, calcium, potassium, or sodium component preferably is a potassium aluminosilicate having the formula KAlSi


3


O


8


with little sodium values.











The following examples are intended to illustrate, but not limit, the invention herein.




An inventive sample is made by adding together feldspar, calcium magnesium silicate and other glass forming components. The calcium magnesium silicate is Synsil® silicate, from Synsil Products Inc., and has the following composition:



















Oxide Component




Mass Percent



























CaO




24.5







MgO




17.8







SiO


2






53.5







Al


2


O


3






3.4







Fe


2


O


3






0.12







Na


2


O




0.40















The feldspar is a potassium aluminosilicate. Of the glass produced from the glass batch, the Synsil® silicate is 13 mass percent, the feldspar is 3 mass percent, and the other glass forming components are 84 mass percent. A comparative batch is produced using 7 mass percent dolomite, 5 mass percent spodumene, and the balance being the other glass forming components. A comparison of the glasses produced show that the experimental glass is produced with reduced batch free time while retaining similar glass properties as the comparative glass.



Claims
  • 1. A method of producing a glass batch composition, said method comprising forming a glass batch, said glass batch comprising a calcium magnesium silicate wherein the calcium magnesium silicate has an empirical formula of CaxMgySiO2, and the values of x and y are independently from about 0.1 to about 0.6 and z is a value to balance the oxidation state of the compound, and other glass components to produce said glass batch, and then melting said batch to form a melted glass batch composition, wherein the amount of said calcium magnesium silicate is effective to produce a viscosity and batch free time in said melted glass batch composition less than or equal to that which results from use of an equivalent amount of a lithium composition in a comparative glass batch.
  • 2. The method of claim 1 wherein said other batch components comprises less than about one percent by total batch weight of lithium.
  • 3. The method of claim 2 wherein the lithium amount is about zero.
  • 4. The method of claim 1 wherein the viscosity of the melted glass batch composition is at least about ten percent less than that of the comparative glass batch.
  • 5. The method of claim 1 wherein the batch free time of the melted glass batch composition is at least about ten percent less than that of the comparative glass batch.
  • 6. The method of claim 1 further comprising adding feldspathic minerals.
US Referenced Citations (32)
Number Name Date Kind
3001884 Slayter Sep 1961 A
3381064 Yamaguchi Apr 1968 A
3458331 Kroyer Jul 1969 A
3520705 Shido et al. Jul 1970 A
3802901 Robertson et al. Apr 1974 A
3817776 Gringas Jun 1974 A
3875288 Hoffman et al. Apr 1975 A
3883364 Robertson et al. May 1975 A
3926647 Wuhrer Dec 1975 A
3941574 Melkonian et al. Mar 1976 A
3956446 Eirich et al. May 1976 A
3967943 Seeley Jul 1976 A
3969100 Kuna et al. Jul 1976 A
4023976 Bauer et al. May 1977 A
4026691 Lovett et al. May 1977 A
4028131 Pons Jun 1977 A
4110097 Chevallier et al. Aug 1978 A
4252754 Nakaguchi Feb 1981 A
4474594 Lazet Oct 1984 A
4519814 Demarest, Jr. May 1985 A
4612292 Richard Sep 1986 A
4634461 Demarest, Jr. et al. Jan 1987 A
4920080 Demarest, Jr. Apr 1990 A
5004706 Dickinson Apr 1991 A
5100840 Urabe et al. Mar 1992 A
5422320 Adams, Jr. et al. Jun 1995 A
5900052 Nakajima et al. May 1999 A
6211103 Tomaino et al. Apr 2001 B1
6271159 Fairchild et al. Aug 2001 B1
6287378 Fairchild et al. Sep 2001 B1
6287997 Fairchild et al. Sep 2001 B1
6336346 Tomaino et al. Jan 2002 B2
Foreign Referenced Citations (10)
Number Date Country
42 28 500 Sep 1992 DE
53-139621 Dec 1978 JP
55 149122 May 1979 JP
59 64563 Apr 1984 JP
2 141454 May 1990 JP
10 291852 Nov 1998 JP
644 731 Jan 1979 RU
823 285 Apr 1981 RU
981 217 Dec 1982 RU
340 257 May 1983 RU
Non-Patent Literature Citations (3)
Entry
“Glass”, Kirk-Ohmer, Encyclopedia of Chemical Technology, 4th Edition 1994, vol. 12, pp. 555-569, 593-601.
Mirkovich, V.V.; “Utilization of Diopside in the Manufacture of Glass,” Mines Branch Technical Bulletin TB 192; Dept. of Energy, Mines and Resources (Ottawa, Canada 1974).
Mirkovich, V.V. et al; “Utilization of Diopside in the Manufacture of Glass, Part II”; Journal of the Canadian Ceramic Society; vol. 44, pp. 43-47; (1975).