PROCESS FOR MANUFACTURING GLASS

Abstract: Process comprises the following steps, (1) heating a silicon dioxide powder in the presence of a phase conversion promoter to form a sinter that has a cristobatile crystal phase, (2) moulding or re-pulverising the sinter, (3) placing the moulded sinter in a vessel of desired shape or, if step (2) was re-pulverisation, collecting sinters in the shaped vessel, (4) heat-melting in vacuo to effect vitrification. The vessel used in step (1) can have a comparatively small dia..

Description: [Technical Field] The present invention relates to a process for the production of a glass product by a vacuum melting method using silica as a raw material. [Background Technology] In general, glasses as industrial products are produced by heating raw material powders prepared in a prescribed mixing proportion in a crucible or a tank furnace at temperatures higher than the liquids temperature to form a homogeneous mixture in the melting state and then cooling the mixture. In the production of a glass, the glass is usually made transparent, for example, by a means in which the bubbles in the melt formed from the adsorbed gas in the raw materials and the gas generated during the reaction are removed by elevating the temperature of the melt to reduce its viscosity sufficiently thereby allowing the gases and bubbles to float to its surface. However, in the case of producing a glass from silica as the raw material, because of its high melting point, the temperature cannot be elevated to an extent effective for removing bubbles from the restrictions such as high viscosity of the melt, refractoriness required for the crucible or furnace and for other reasons and if the temperature is elevated excessively, gases are generated by the volatilization of the raw material per se and the reaction between the raw material and the crucible to thereby form all the more bubbles. Therefore, the above-described method cannot be employed. For the reasons set forth above, a method for the production of a transparent quartz glass using silica as the raw material is restricted to any one of the following methods: (1) A method in which a silica powder is gradually fed into an argon-oxygen plasma flame or an oxygen-hydrogen flame and melted for glass formation and the resulting melt is deposited onto a stand. The generated gases are dissipated from the surface (Verneuil method); (2) A method in which a porous body composed of silica fine particles is prepared and melted from one end thereof in the band-like state for glass formation. The generated gases leave from the unmelted porous body (zone melting method); and (3) A method in which rock crystal powders prepared to have particle diameter of about 100 µm is placed in a crucible and melted in a vacuum furnace for glass formation. The generated gases are removed off by force (vacuum melting method). However, with respect to the method (1) and method (2), it is well known that an extremely long period of time is required for producing one glass block and its productivity is poor, and especially in the case of the Verneuil method, the yield is extremely as low as 30% to 40%. Further, in the case that the argon-oxygen plasma flame is employed as a heat source, though a glass having a small number of residual OH groups and a relatively small number of bubbles can be obtained, the energy costs are high, whereas in the case that the oxygen-hydrogen flame which is low in the energy cost is employed, the problem is that a product has a large number of residual-OH groups. Still further, since the shape of ingots which can be produced is restricted to cylindrical and slender shapes, there is a disadvantage to the subsequent processings. According to the vacuum melting method (3), though a relatively large-sized ingot having a small number of residual OH groups and a high viscosity at high temperatures can be obtained, since the raw material powder filled in a vessel such as a crucible is melted for glass formation, not only there is a difficulty in degassing but also a reaction gas caused by the contact with the vessel is generated, the resulting glass has a relatively large number of bubbles. Therefore, those having a high quality cannot be obtained. Further, since the rock crystal powders are used, bubbles not only tend to ge generated due to low purity of the raw material per se, but also there is a concern in the raw material supply due to exhaustion of the resources. Under such a background, the present applicant has developed a process by which a transparent of functional, high-quality glass can be readily produced at low production costs. This process is characterized in that a silica powder is filled in a suitable vessel, heated in the presence of an accelerator for phase conversion such as an alkali metal component etc. to form a porous body having continuous open pores unified in a crystal phase right below the melting point, and then melted in vacuo for glass formation (see Japanese Patent Aplication Nos. 181586/84, 181587/84, 181588/84, 170663/85, and 170664/85). In the Soviet Journal of Glass Physics and Chemistry the manufacture of glass is disclosed by heading silica powder in the presence of an accelerator for phase-conversion to convert it into a cristobalite powder which is thereafter molten in high vacuo to degas and thereafter molten in vacuo. It is known that crystalline silica causes phase conversion from a quartz phase at low temperatures to a tridymite phase and further to a cristobalite phase, depending upon the heating temperature in the heating step. This phase conversion hardly takes place when silica is used alone, but Li₂O, Na₂O, K₂O, MgO, CaO, P₂O₅ and B₂O₃ are known to be useful as an accelerator for phase conversion. Since amorphous silica is sintered for glass formation without being crystallized when used alone, in order to crystallize it into a cristobalite phase, the addition of the above-described metal additives is required. Accordingly, in the process of the present invention, the above described metal components are used in the step for crystallizing the silica powder into the cristobalite phase. However, as will be understood from the foregoing explanation concerning the prior art technologies, in the conventional production methods of glasses, if such a metal component is present in the raw material, such metal component, if any, is likely to cause deterionation in purity of a final product as in the case of OH groups or the like and this is not desirable. That is, in the conventional production methods of glasses, there is a conflicting relation between obtaining a high-quality quartz glass and adding of impurities to the raw material or employing a raw material containing impurities. In view of the foregoing fact, it can be said that the process of the present invention in which an accelerator for phase conversion is added to silica or silica containing an effective component for the phase conversion is selectively used as the raw material is a method not available with the conventional concept. The reasons why this process can readily obtain a high-quality glass as compared with the conventional methods is that the characteristics available with a sintered body consisting of a cristobalite phase produce many effects coupled with employment of the vacuum melting method. In other words, as is well known, since the melting point of the sintered body is uniquely determined by the cristobalite phase, the sintered body can be heated up to the temperature right below the melting point and subjected to the degassing processing. Further, since the sintered body consisting of a cristobalite phase is a porous body having continuous open pores, it can be degassed thoroughly and readily. Accordingly, if a metal component, such as Na, which is readily decomposed and vaporized at temperatures below the melting point of the sintered body, are employed as an accelerator for phase conversion, a transparent quartz glass from which the impurities (including the accelerator for phase conversion) have almost completely been removed can be obtained. On the other hand, if an accelerator which is not decomposed and removed at said melting point is selected, an functional glass containing only the accelerator but free from other impurites can be obtained. The process for the production of a glass with which the present invention is concerned could provide high-quality glass ingots with good productivity through an organic combination of a crystallization process in which an accelerator for phase conversion is used with a glass forming process by the vacuum melting method but involved a drawback in obtaining glass ingots having desired shape. This is because in the case that a glass ingot having a desired shape such as a plate-like shape or a cylindrical shape is intended to obtain, there was involved a factor that it is difficult to produce a satisfactory sintered body having a desired shape with good productivity. Furthermore, though a process for the production of a glass with which the present invention is concerned has an effect that a relatively large-sized glass ingot can be obtained, in order to obtain a larger ingot, it is inevitable to previously enlarge the size of a container for the sintered body, and the manufacture of such container becomes difficult, for heat resistibility and others are required for such container. Much more, since silica powder to be used as the raw material is low in both bulk density and heat conductivity, in the case that a large-sized sintered body is intended, problems may occur either in production efficiency or quality of the ingot. In view of the foregoings, an object of the present invention is, therefore, to provide a process for the production of a glass product comprising a crystallization process and a vacuum melting process, whereby a high-quality glass ingot having a desired shape or a larger glass ingot can be readily produced without reduction in productivity. [Disclosure of the Invention] In order to solve the above-described problems, the present invention relates to a process for the production of a glass comprising filling the silica powder and an accelerator for phase-conversion into a container, heating the silica powder in the presence of the accelerator to convert it to a sintered body having cristobalite phase and a shape corresponding to that of the container, processing the thus obtained sintered body into a desired shape, charging the thus processed sintered body into a container having a shape identical or similar to the desired shape and heating it for melting in vacuo for glass formation. The invention relates further to a process for the production of a glass product comprising filling the silica powder and an accelerator for phase-conversion into a plurality of containers, heating the silica powder in the presence of the accelerator to convert it to a plurality of sintered bodies having cristobalite phase and a shape corresponding to that of the containers, processing the sintered bodies into an accumulated sintered body of a desired shape and heating it integrally for melting in vacuo for glass formation. Additionally, the invention relates to a process for the production of a glass product comprising filling the silica powder and an accelerator for phase-conversion into a container, heating the silica powder in the presence of the accelerator to convert it to a sintered body having a cristobalite phase, powdering the sintered body, filling the resultant powder in a desired container and then heating and melting it in vacuo for glass formation. In the process for the production of a glass product according to the present invention, if production of glass ingots having a desired shape such as a plate-like shape or a cup-like shape or a larger product is required, it is apparent that the sintered body having a desired shape or larger sintered body is obtained in the crystallization process. However, it is not easy to obtain such sintered body by the crystallization process because not only the process is closely related to the subsequent glass forming process but also organically related thereto, since high-quality glass can be obtained only when a number of requirements are met. The requirements that the sintered body must meet, for example, are that the pore size is to be so large as to allow to leave the residual gas but sufficiently small to stand shrinkage in melting and that it is to be free from formation of even small cracks in size. Accordingly, many problems are left to be solved in order to meet these requirements, for raw material powders need to be filled in a container in this means in which raw material powders are initially envolved in obtaining sintered body. This is because silica powder as raw material has poor heat efficiency due to low bulk density and low heat conductivity, but more because silica powders are difficult to achieve uniform heating thereby cracks become to be most likely to be caused. Thus with a plate-like ingot, due to the contact surface between the container and the powder being large and its thickness being small, the problem becomes all the more serious. Further, in the case that a cup-like ingot is intended to obtain, since a core is necessarily used, cracks are likely to be caused for the same reasons as those described above. Still further, in the case that a larger glass ingot is intended to obtain, a reduction in productivity is unavoidable. Taking into account the fact that the process for the production of a glass product including the above-described crystallization process has characteristic effects that are not available with the conventional methods, the present inventors have made further researches on the subject process and found a means for obtaining a glass ingot having a desired shape or larger glass ingots by molding or repowdering the resulted sintered body and putting or filling it in a container of a desired shape for glass formation, or by accumulating a plurality of the sintered bodies into a desired shape for glass formation. Filling simply the raw material in a container can produce characteristic effects that a sintered body which meets the aforesaid requirements can be readily obtained, the thus obtained sintered body is excellent in workability, and that sintering is unified in crystal phase right below the melting point and that the melting point is unique etc. As is clear from the foregoing explanation, the process for the production of a glass product with which the present invention is concerned has effects that it can not only solve the poor yields in raw materials or poor productivity from a long operation time for glass formation required which have been unavoidable in the conventional methods inclusive of the Verneuil method etc. but also give products at inexpensive costs because the present process does not require a particularly expensive heat source. Such effects can further be accelerated by the process of the present invention, that is, in the conventional methods it was impossible to readily obtain a glass ingot identical or similar to a final product, or a larger glass ingot or the quality was not satisfactory, whereas in the process of the present invention, since a step for obtaining the crystallized sintered body can be effectively used, a product having a satisfactory quality can be obtained. Further, since the sintered body has such characteristic properties that its workability is excellent, there is not encountered any problem in productivity. A method for using powders of cristobalite phase gives definite differences in effect over the conventional method in which quartz powders are heated and melted in vacuo for direct glass formation. That is, in the conventional method, melting partly occurs in glass forming process to cause insufficient degassing, whereby the probability of impurities to remain increases, resulting in problems of quality. On the other hand, in the process of the present invention, since the sintered body is of porous powders unified into crystal phase right below the melting point which is unique, it is possible to degass at relatively high temperatures until melting occurs, whereby high-quality products can be obtained. [Best Mode to Carry Out Invention] The embodiments of the present invention are now described in the followings. In the first embodiment thereof wherein a glass ingot having a desired shape is obtained is described. For example, to amorphous silica powder obtained by oxidizing silicon tetrachloride, an Na component is added as an accelerator for phase conversion in a weight ratio of about 1,000 ppm. As a means for addition, since it is desirable to granulate the silica powder into large particles without substantially changing the specific surface area thereof, a preferred method is that the silica powder is added to an NaOH aqueous solution and stirred for mixing, followed by dehydrating and drying. The thus obtained Na component-containing silica powder is filled in a container of a shape indentical or similar to that of a final product and then heated. Any heating means can be optionally used. When the silica powder is heated at 1,100°C or higher, a sintered body having cristobalite phase and a shape corresponding to that of the filling container is obtained. The thus obtained sintered body is processed into a desired shape by cutting and excising (including by boring). Accordingly, for example, when a glass ingot of a rectangular plate-like shape is required, the silica powder may be processed with a square pillar container form a sintered body which is then sliced into a plurality of rectangular plates. Further, when a sintered body of cylindrical shape is required, a columnar sintered body may be processed and then bored. The thus processed sintered body is charged in a container having a shape identical or similar to the desired shape and, after placing a core in it, if necessary, is heated for melting in vacuo for glass formation. In this case, the heating is carried out under a reduced pressure of 0.5 mb or less at a temperature of 1,750°C or higher, whereby a high-quality glass ingot is obtained wherein contaminated impurities and the accelerator for phase conversion added have been almost completely removed. Since the obtained ingot has a shape identical or similar to that of a final product, subsequent processing can be omitted or minimized. In the second embodiment of the present invention whose object is similar to that of the above-described first embodiment of the invention, the object is to be achieved by repowdering the sintered body and filling the thus obtained powder in a container having a desired shape, followed by glass formation. That is, the silica powder containing an accelerator for phase conversion is converted into a sintered body having a cristobalite phase by a suitable heating means. In this case, though it is not always necessary to perform heating after filling the silica powder) in a container, it is preferred that the heating is performed after filling the silica powder in the container for prevention of contamination by impurities or for the post-treatment. Thereafter, the thus obtained sintered body is repowdered to prepare a powder having a bulk density of about 1.1 g/cm³, and the power is filled in a container having a desired shape and, after placing a core in it, if necessary, is then subjected to glass formation in vacuo in the same manner as described above. While this method has a disadvantage that the resulted product is inferior in quality to the molded sintered body, it has advantages that the workability is good and that no care is necessary for crack formation thereon. The third embodiment of the present invention is concerned with the case in which a larger glass ingot is intended to obtain, in which a plurality of the sintered bodies obtained in the same manner as in the first embodiment of the invention are processed into an accumulated sintered body having a desired shape. For accumulation, shapes such as piled shape or a gathered shape may be used along with any other optional sizes. However, in order to attain the desired shape and dimension of the ingot, it is necessary to previously determine the shape and dimension of the sintering container. Further, while it is required to mold so that the sintered bodies have contact surfaces free from unevenness, molding can be readily performed because the sintered bodies have good workability. The thus obtained sintered body in accumulation is transferred into a vacuum furnace and heated under a reduced pressure of 0.5 mb or less at a temperature of 1,750°C or higher, to thereby integrate a plurality of the sintered bodies for glass formation. EXAMPLE 1 A silica powder containing an Na component in a weight ratio of 1,000 ppm was heated to obtain a sintered body having cristobalite phase and outer diameter of 265 mm and height of 390 mm. This sintered body was sliced to thickness of 70 mm by means of a metal saw to prepare five disks each having outer diameter of 265 mm and thickness of 70 mm. These disks were placed in a graphite container having inside diameter of 265 mm and height of 70 mm and transferred into a vacuum furnace, followed by subjecting to glass formation. There were thus obtained five glass sheets weighing about 4.4 kg and having outer diameter of 265 mm and thickness of 37 mm. EXAMPLE 2 The same procedures as in Example 1 were followed to obtain a sintered body having outer diameter of 265 mm and height of 390 mm. Thereafter, using a drill, a hollow portion having inside diameter of 50 mm was formed in the central portion of the sintered body. The resulted sintered body was placed in a graphite container having inside diameter of 265 mm and height of 400 mm, and a graphite-made core having outer diameter of 50 mm was inserted into the hollow portion, followed by subjecting to glass formation in vacuo. There was thus obtained a cylindrical glass weighing about 24 kg and having outer diameter of 265 mm, inside diameter of 50 mm, and height of 200 mm. EXAMPLE 3 A silica powder containing an Na component in a weight ratio of 1,000 ppm was filled in a container and heated to obtain a sintered body having a cristobalite phase. This sintered body was repowdered by grinding to obtain a powder having a bulk density of about 1.1 g/cm³. Thereafter, the powder was uniformly filled in a thickness of 200 mm in a rectangular container having inner size of 300 mm × 300 mm × 300 mm. At this time, the filled powder was weighed about 20 kg. The container was placed in a vacuo furnace for glass formation. There was thus obtained a plate-like glass ingot weighing about 19 kg and having a size of 300 mm × 300 mm × 100 mm. EXAMPLE 4 25 kg of silica powder containing an Na component in a weight ratio of about 1,000 ppm was filled in each of two mullite containers each having inside diameter of 420 mm and height of 620 mm and then heated in a heating furnace. The heating was carried out for 75 hours to elevate the temperature to 1,100°C and the temperature was kept 5 hours at 1,100°C. There was thus obtained a sintered body having a cristobalite phase, outer diameter of 265 mm and height of 390 mm. The two sintered bodies thus obtained were processed by excising the peripheral face thereof with a knife, etc. and then molded into an accumulated sintered body having outer diameter of 265 mm and height of 750 mm, followed by heating and melting in vacuo. The heating was carried out for 12 hours to elevate the temperature to 1,730°C and the temperature was kept for 3 hours at 1,730°C. There was thus obtained an integrated transparent quartz glass weighing 49 kg and having outer diameter of 265 mm and height of 400 mm. [Possibility of Use in Industry] The present invention can be used as a process for the production of a glass product which is used in tools for apparatus of producing semiconductors, instruments for physics and chemistry, optical materials, etc.

Claims: 1. A process for the production of a glass product comprising filling a silica powder and an accelerator for phase-conversion into a container, heating the silica powder, in the presence of the accelerator, to convert it to a sintered body having cristobalite phase and a shape corresponding to that of the container, processing the thus obtained sintered body into a desired shape, charging the thus processed sintered body into a container having a shape identical or similar to the desired shape and heating it for melting in vacuo for glass formation. 2. A process for the production of a glass product comprising filling a silica powder and an accelerator for phase-conversion into a plurality of containers, heating the silica powder, in the presence of the accelerator, to convert it to a plurality of sintered bodies having cristobalite phase and a shape corresponding to that of the containers, processing the sintered bodies into an accumulated sintered body of a desired shape and heating it integrally for melting in vacuo for glass formation. 3. The process for the production of a glass product as claimed in claim 2, characterized in that the outer peripheral face of the sintered body is processed prior to the accumulation. 4. A process for the production of a glass product comprising filling a silica powder and an accelerator for phase-conversion in a container, heating the silica powder, in the presence of the accelerator, to convert it into a sintered body having a cristobalite phase, powdering the sintered body, filling the resultant powder in a container having a desired shape and then heating and melting it in vacuo for glass formation.

Inventors: IMAYOSHI, TERUKAZU, KIKUCHI, HITOSHI, MORISHITA, HIROSHI, NAKAMURA, AKIHIRO
Applicants: JAPAN OXYGEN CO. LTD.
Application year: 1987
Main classification: C03B20
IPC codes: C03B20, C03C3, C03C10