Process for Melting and Refining Soda-Lime Glass
A process for making soda-lime glass includes forming and refining sodium silicate glass in liquid phase. At least one other material is dissolved in the refined liquid phase sodium silicate glass to produce a liquid phase soda-lime glass melt. Formation of sodium silicate glass as an intermediate product before mixing with at least one other glass-forming material has the advantage of promoting release of gaseous reaction products from the sodium silicate glass during the refining step due at least in part to the relatively low viscosity of the sodium silicate glass. One or more steps in the process can be carried out under reduced pressure to promote release of gases and to reduce bubble formation.
The present disclosure relates to a process for melting and refining soda-lime glass, and particularly to such a process that employs sodium silicate glass as an intermediate product.
BACKGROUND AND SUMMARY OF THE DISCLOSURESoda-lime glass, also called soda-lime-silica glass, is prevalent in the manufacture of glass containers and other glass products. Formation of the raw glass melt typically involves mixing the various glass-forming components at elevated temperature. The glass typically has a residence time in a furnace on the order of twenty-four hours to refine the glass by driving off gases and dissolving solids. The gases must be driven off ultimately to produce a solidified glass product without entrained gas bubbles; the process of removing bubbles in molten glass is called “refining.” In addition to being undesirably slow, this in-furnace process involves a large amount of space and high energy input.
A general object of the present disclosure is to provide a process for making soda-lime glass, which is more rapid and requires less energy input than conventional processes.
The present disclosure embodies a number of aspects that can be implemented separately from or in combination with each other.
A process for making soda-lime glass, in accordance with one aspect of the present disclosure, includes (a) forming sodium silicate glass in liquid phase and in the absence of water while releasing gaseous reaction products, and (b) mixing the sodium silicate glass reaction product of step (a) with other materials to form a soda-lime glass melt. The low viscosity of the molten sodium silicate glass (relative to or as compared with soda-lime glass at the same temperature) enables and promotes release of gaseous reaction products such as carbon dioxide.
A process for making soda-lime glass, in accordance with another aspect of the disclosure, includes calcining calcium carbonate in solid phase and at elevated temperature to form calcium oxide and release gases such as carbon dioxide. Sodium silicate glass is formed separately in liquid phase while releasing gaseous reaction products. The calcined calcium carbonate and sodium silicate glass intermediate products are mixed to form a soda-lime glass melt. Formation of sodium silicate glass as an intermediate product before mixing with the calcium oxide has the advantage of promoting release of gaseous reaction products in the sodium silicate glass due at least in part to the low viscosity of the sodium silicate glass (relative to or as compared with soda-lime glass at the same temperature). Thus, the calcium oxide intermediate product and/or the sodium silicate glass intermediate product is at least partially if not entirely refined, and at least partially if not entirely free of gases and gas bubbles, prior to the mixing stage. This greatly reduces the time and energy required for the final mixing stage to produce the soda-lime glass melt. The calcination step and/or the sodium silicate glass-forming step and/or the final mixing step can be carried out under reduced pressure further to promote release of gases and reduce bubble formation.
In one embodiment, the sodium silicate glass is formed by melting soda ash in the presence of silica, releasing carbon dioxide gas. In another embodiment, the sodium silicate glass is formed by melting sodium chloride in the presence of silica and steam to form the sodium silicate and release hydrogen chloride gas.
The disclosure, together with additional objects, features, advantages and aspects thereof, will best be understood from the following description, the appended claims and the accompanying drawings, in which:
A second stage of the process involves melting, reacting and refining input materials and production of sodium silicate glass in liquid (molten) phase. This sodium silicate glass is a “dry” glass in the sense that it is not dissolved in water. In one embodiment 20 in
At a third stage 30 of
Although stages 10 and 10a are illustrated in
The entire process illustrated in the drawings can be carried out in about three to four hours, as compared with the twenty-four hour residence time typically needed in the prior art, and at a theoretical estimated energy input of about 1.5 megajoules per ton versus an estimated theoretical energy of 2.2 megajoules per ton typical of the prior art.
There thus has been disclosed a process for making soda-lime glass that fully achieves all of the objects and aims previously set forth. The disclosure has been presented in conjunction with presently preferred embodiments, and alternatives and modifications have been discussed. Other alternatives and modifications readily will suggest themselves to persons of ordinary skill in the art in view of the foregoing description. The disclosure is intended to embrace all such modifications and variations as fall within the spirit and broad scope of the appended claims.
Claims
1. A process for making soda-lime glass, which includes the steps of:
- (a) forming sodium silicate glass (Na2O-SiO2) in liquid phase;
- (b) refining the liquid phase sodium silicate glass of step (a); and
- (c) after completion of step (b), dissolving at least one other material in the refined liquid phase sodium silicate glass of step (b) to produce a liquid phase soda-lime glass melt.
2. The process set forth in claim 10 wherein step (b) is carried out under reduced pressure to promote release of a gaseous reaction product from the liquid phase sodium silicate glass of step (a).
3. The process set forth in claim 1 wherein said step (a) includes:
- melting and reacting soda ash (Na2CO3) and silica (SiO2) with each other, but without addition of water (H2O), to produce carbon dioxide (CO2) as and form the sodium silicate glass (Na2O-SiO2) in liquid phase.
4. The process set forth in claim 3 wherein the soda ash and the silica are melted and reacted with each other at a molar ratio of about 1:1 to about 1:5.
5. The process set forth in claim 1 wherein said step (b) is carried out at a temperature in the range of 900° C. to 1700° C.
6. The process set forth in claim 1 wherein said step (a) includes:
- melting and reacting sodium chloride (NaCl) with silica (SiO2) and steam (H2O) to produce hydrogen chloride (HCl) as and form the sodium silicate glass (Na2O-SiO2) in liquid phase.
7. The process set forth in claim 1 wherein the at least one other material of said step (c) is selected from the group consisting of: calcium oxide (CaO), silica (SiO2), cullet, and combinations thereof.
8. The process set forth in claim 13 wherein step (c) includes mixing to promote dissolution of the at least one other solid phase material in the refined liquid phase sodium silicate class of step (b).
9. The process set forth in claim 1 wherein step (c) is carried out at a temperature greater than about 900° C.
10. The process set forth in claim 1 wherein said step (a) includes:
- reacting a sodium-containing compound with silica (SiO2) to form the sodium silicate glass (Na2O-SiO2) in liquid phase.
11. The process set forth in claim 3 wherein step (b) is carried out under reduced pressure to promote release of carbon dioxide (CO2) gas from the liquid phase sodium silicate glass of step (a).
12. The process set forth in claim 6 wherein step (b) is carried out under reduced pressure to promote release of hydrogen chloride (HCl) gas from the liquid phase sodium silicate glass of step (a).
13. The process set forth in claim 1 wherein the at least one other material of said step (c) is in solid phase prior to being dissolved in the refined liquid phase sodium silicate glass of step (b).
14. The process set forth in claim 7 wherein the liquid phase soda-lime glass melt produced in step (c) has a higher concentration of silica (SiO2) than the refined liquid phase sodium silicate glass of step (b).
15. The process set forth in claim 1 wherein step (c) includes dissolving silica (SiO2) in the refined liquid phase sodium silicate glass of step (b) such that the liquid phase soda-lime glass melt produced in step (c) has a higher concentration of silica than the sodium silicate glass of step (b).
16. The process set forth in claim 1 wherein the refined liquid phase sodium silicate glass of step (b) has a relatively low viscosity at a temperature in the range of 900° C. to 1700° C., and the liquid phase soda-lime glass melt produced in step (c) has a higher viscosity than the sodium silicate glass of step (b) at the same temperature.
Type: Application
Filed: Apr 13, 2015
Publication Date: Oct 22, 2015
Inventors: Dawid Dewet-Smith (Perrysburg, OH), Carl L. Fayerweather (Maumee, OH), Brett E. Hixson (Adrian, MI)
Application Number: 14/684,923