• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Flat glass having superior optical quality is continuously produced by a contiguous float process in which lamellar flows are established in a molten glass conditioner and the flow patterns are maintained in a stream of glass unidirectionally delivered onto a pool of molten metal on which the glass is cooled and unidirectionally attenuated to form a ribbon of glass.
    公开号:SU923362A3
    申请号:SU742006840
    申请日:1974-03-05
    公开日:1982-04-23
    发明作者:Кей Идж Чарльз；Эрасмас Кюнкл Джерельд
    申请人:Ппг Индастриз Инк (Инофирма)；
    IPC主号:
    专利说明:

    one
    . The invention relates to the production of sheet glass on the surface of a molten metal having a wide range of thickness, improved optical properties and adjustable s by width.
    A known method of manufacturing sheet glass, including creating an irrotational flow of glass mass, unloading it through a hole in a closed chamber onto the surface of the molten metal, transporting glass mass to the surface of the molten metal, diverting the glass ribbon from the bath of GP 15
    The closest to the invention to the technical essence is a method of producing sheet glass, including unloading glass mass into a bath onto the surface of the molten metal 20 to form a laminar flow, forming it into a ribbon, advancing the ribbon along the bath and withdrawing from it 2.
    The disadvantage of the known methods is that the glass obtained is
    These methods exhibit significant optical distortion.
    The purpose of the invention is to improve the optical properties of glass.
    The goal is achieved in that according to the method of producing sheet glass, which includes unloading glass mass onto the surface of the molten metal to form a laminar flow, forming glass mass into a ribbon, advancing the ribbon along the bath and withdrawing from it, the glass mass is discharged through a threshold whose upper surface is located at the level of the molten metal, and the formation of glass melt into a ribbon is carried out with a decrease in temperature of 3.6-27.2 ° C per meter of glass melt in the direction of motion.
    In addition, during (1 orbiting of glass melt into a ribbon, it can be further heated by its side parts.  Promotion of the central part of the molten glass along the bath can be carried out at a speed of 39233624 Rdanoy 1-5 times the speed at the lateral ends of the elements in contact with the outlets. glass cooled to a specific method is carried out as follows.  The side elements are provided with an image. means for heating or cooling the melted glass from the source j to regulate the magnitude of the melted glass is fed to the equipment to which they are wetted by the melt for processing, in which it is broken by glass.  In addition, intervolume give irrotational flows.  The glass, melted glass and side windings with uniform vortex free points are supplied with a lubricant, current, discharged through the discharge jubocular elements of sufficient degree into the bath of molten metal insulated from the outside atmosphere.  The discharge device in the cavity, which prevents unwanted cross-section, has an opening, such as glass cooling along its lateral rule, elongated rectangular form-parts, Glass flowing along the sides with a lower boundary created by the 5th sections adjacent to the lateral support element or the threshold Element elements, with sufficient height, with an upper limit, create temperature and low viscosity, my measuring barrier, for example, because it does not turn out to be an over-slide, and lateral sides, measuring braking no.  Therefore, glass-made stands or walls.  20 Received according to the proposed method. The distance between the upper element of the dog has no fir-tree distortion on the lower element and less than the lateral parts.  Standing between the side walls, so the glass tape moving from that molten glass flowing. the space between the side elements through the cross-sectional area, subjected to further cooling, has a width many times greater than the thrust force in its direction.  thickness.  The length of the unloading device-displacement and give it the final property, as a rule, approximately the thickness while maintaining 20% less than its width. the same width as the width of the glass from the discharge device to the point of its exit from the limited fused glass protrudes into the bathing space between the side elements of the molten metal, such as tin.  Variation in width, as rule or alloy containing tin.  If it is less than 5% of the total width of the tape, the melted glass can be moved and the tape experiences a total compression only horizontally or a drop of less than 5 can be lowered during its transport to the molten metal; it lies along the molten metal bath.  In any case, the glass is prevented from being able to, the drowsiness unloading device support falls freely on the molten metal, keeps the refractory element, for example metal, since the free fall of the melted silica, which scatters uniform non-vortex fluxes, is moistened with glass and passes through them that are created. in the device for the rhin of the discharge zone as opposed to.  This destruction, especially in the direction to the upper gauge, is observed near the side edge element.  Molten glass is sheet glass that is molded by svog-leaking, in contact with a refractory glass drop. . support or lubricant, and the width of the flow of the molten glass mer, molten metal or melted is determined by parallel directional-melted salt.  It is possible for the elements to pass through the neutral under, which is allowed to move the glass and is prevented, for example, from an inert metal, in any external flow or ne particular platinum that does not enter the molten glass. em in the reaction of glass.  Such an element Lateral elements can be short-effectively form a short threshold, MI OR long, for example, they can, through which it is possible to unload, to serve the side walls of unloaded-fused glass.  The support can be dispenser.  They consist of setting down some material that is well wetted — from the bottom plane of the flow of glass and with melted glass in the area of the pe-gee can be covered with a bath of molten-displaced glass along their length, but which is of considerable thickness, is slightly wetted by the glass of the bearing. with the main bath of molten metal.  Below, located below the molten metal, can be performed by positioning its edge at the closest distance to the source of molten glass and making it slightly elevated relative to the rest of the hearth in order to prevent molten metal from entering the source of molten glass, or to separate it. molten metal from the source of molten glass can be provided with a threshold or threshold barrier.  The valve, which is hit by the molten glass, may be made of fused silica or reinforced with platinum, at least on one surface facing the molten glass, or of molybdenum.  A mechanical barrier is also possible, located close to the surface of the molten glass and provided with gas extraction nozzles, which are used to create a gas curtain between the source of molten glass and the forming zone.  The width of the flowing glass is supported not more than the width of the glass that comes from the source of the molten glass to the discharge device, which, together with the creation and maintenance of an irrotational flow characteristic, results in the glass having a personal optical property.  The glass flowing through the open surface of the glass in the source, molten glass before exiting: the discharge device is held on or near the upper surface of the glass tape during its molding, and the glass that enters the discharge device in contact with the bottom of the glass forms the bottom surface of the finished glass tape cat Step 8, the molding period is kept in contact with the molten metal.  The glass entering the discharge device on the sides of the flow I of the floating molten glass with respect to the finished ribbon remains in the same position. Such flotation conditions are created and maintained during the process of transporting molten glass from the source of molten glass to and through. forming chamber, improve the optical properties of the sweat glass.  In addition, the proposed method, compared with existing industrial float manufacturing processes: 7 glass, creates advantages that relate to the relationship between the refining zone of the source of molten glass and the float forming zone during the process.  In traditional methods for producing float glass, the telomet forming chamber is separated from the source of molten glass both mechanically and hydrodynamically.  The glass throughout the refiner-source of molten glass or furnace is stretched into a narrow channel, and the dimensions of the stream existing in the refiner are broken.  A relatively narrow stream of molten glass coming out of a conventional channel subsequently falls freely into a bath of molten metal and spreads out in all directions.  In traditional float glass production, the effects of flow and flow of glass created by narrow channels and free fall of glass cause glass to flow into molten molding glass, having flows and conditions that differ significantly from the conditions and flows of existing melting devices in raffin. | re.  In carrying out the invention, the processing device creates non-vortex flows by creating suitable thermal conditions so that: in order to create a large and therefore stable convection cell inside the molten glass in the processing device, the thermal conditions are stable over the zone passing through at least 50 feet upstream to the treatment unit from the opening in the front wall of the treatment unit leading to the discharge zone.  The zone of standing heat conditions will extend 75-120 feet upstream, although it can go on without any harmful effect other than economic costs.  The thermal stress condition is one of the temperature gradients in the molten glass, which can be obtained by measuring with surface radiation pyrometers.  Over the entire length of the specified zone, the temperature should drop by an average of 3i679 per meter, Cooling will be nocf lowering the temperature warm, with an average of 7.21-12.6 C per meter.  Too low temperature will exclude the formation of a completely irrotational flow, too high will lead to the creation of limited local and sporadic mixing, which will lead to structural heterogeneity in the glass, and thus to heterogeneity of the refractive index.  Thermal regulation above the glass of the refiner is used to establish the plane of the lower part of the flow of glass through the discharge device at a level that is significantly higher than the normal flow level in the finer or processing device.  The usual flow plane in the refinery pe is below the open surface of the glass, where there is no translational flow of the glass.  Above the normal glass plane there is an increased glass speed in the direction of the total eHo flow during the whole process, Directly under the usual flat plate, there is a glass flow opposite to the total FLOW) which is created by the natural thermal convection existing in the processing device or refiner.  Cooling in the refiner is provided mainly by refrigerators immersed in glass and by cooling the refractory base of the refiner from below.  By snapping off the top, a part of it is progressively floating:. portions of the glass in the refiner and supplying this glass as a stream through the discharge device to the molten one.  the metal during the entire molding of a continuous ribbon or sheet of glass maintains a vortex-free flow that is created in the molten glass in the refiner. Whatever chemical heterogeneity does not exist in the glass, they are not obvious due to limited sporadic mixing.  The optical distortion near the edges of the glass tape may be limited to less than 1 tape along each edge.  Since glass tape necessarily has thickened edges that need to be removed during subsequent processing, there is no glass loss with this lateral distortion.  The thermal structures according to the proposed method differ from the previously used structures in that the edge temperatures are correspondingly higher, and the temperature in the central part is relatively lower in the forming zone, directly adjacent to the flow from the glass unloading. Temperature rise near limiting ;; elements and an increase in wetting of these elements creates more drag on the glass.  By using appropriate temperature gradients across the width of the glass, the viscosity of the glass near these elements can be significantly reduced compared with the viscosity near the middle part, which reduces braking.  The flow of glass acts as a stream of two immiscible liquids: the main flow of glass ,. most of the width has a relatively flat velocity profile, and a flow near the elements, which has a very sharp velocity profile.  Traces of sand can be used to observe the main flow of glass, and from an assessment of the physical properties of the continuity of a known zero flow at the wall of each element, one can find out the side flow.  The lateral flow acts as a lubricant-FOR the main flow, although taking into account the general characteristics of the glass, this phenomenon is unexpected.  .  In the production of sodium-known "forged-quartz glass according to the proposed method, it is possible to provide boundary zones with a high-speed gradient that make the main flow.  flat over 90 flow widths.  For example, consider the composition, having,%: SiOri 73, 13.5, Cor 0, i, CaO 8.7, MgO 3. eight, . IS, 0, j, 0.3 and, 15.  This glass has the following relationship viscosity - temperature:.  Log temperature.  .  ° C bone, pause 2 When glass is formed having a composition similar to that described in the Hila patent, the temperature of the lateral parts of the glass drops significantly compared with the temperature of the glass in the central part of the stream.  Due to the natural loss of glass through the side walls, the temperature of the side edges of the glass is 38-93 0 (100-200 F) below the temperature of the central part of the glass.  As a result, the speed of glass near the walls is 5–10 times greater than the speed of glass in the central part of the flow.  Significant inhibition occurs and the significant particles of the glass on the sides have repeated angular distortion, the Regular called collective distortion.  When molding this glass according to the Pilkington method, the edges of the glass are approximately the same. the same temperature as the glass in the central part of the stream.  As a rule, only distortion due to free fall and lateral distortion is associated with a decrease in the cross section of the tape in the absence of obstacles to side flow.  This intermittent distortion line is different from the distortion resulting from inhibition.  However, sometimes excessive cooling of the edges leads to spike distortion.  This is because, even in the absence of a sharp decrease in temperature near the edges along the width of the tape, there is an elongated parabolic propel velocity.  This method is to a large extent metastable in terms of excluding spike distortion.  According to the proposed method, the glass flowing in the center is cooled relatively faster compared with the glass flowing along the side c.  This is achieved thanks to the centrally located upper coolers, as well as by applying heat to the side edges of the glass from the top heaters located on the edges or from the heating side elements, or using heat insulating side elements from the side walls of the Forming chamber.  The lateral parts of the glass are held under pressure at temperatures that are equal to the temperatures of the central part 1: flowed and maintained at a temperature of 6210 Vypax above 6, b7-93 C (20-200 F).  As a rule, glass will be discharged at an isothermal temperature in the range of 1093 ° C (2000 ° F); downstream of the discharge device and between the side elements, where the central part of the glass (approximately 90% of the glass) has a temperature of about 982 ° C. (), the side portions of the glass are of the order of temperature); as soon as the downward flow of glass reaches the side elements, the temperature at the center is 871 ° C () and the temperature of the side parts is 888 ° C (1b3 ° C).  The velocity profiles resulting from this magnitude of temperatures are almost horizontal by more than 90% of the stack width. la, at a speed, in the center, approximately 1.1 times the speed at a point at a distance of 5% of the width of any side element.  Typical speed ratio ranges are: 10-20 for a method in which glass is in contact with side walls. open to the ambient atmosphere, t-G for a traditional, industrial process having an iso-thermal width profile; 1-5, and more often 1-3 for the proposed method. Obviously, the flow of glass according to the proposed method is more uniform across the width of the floating glass than that of the glass according to known methods.  Lateral distortion-i; si 3 finished tape reduces the loss of glass.  The elimination of unhindered lateral movement greatly simplifies the management of the tape; of the floating glass down the center of the forming chamber onto the take up rolls and into the annealing furnace.  Eliminating unhindered lateral movement also solves the problem of evenly removing heat from the glass.  In the proposed device, lower total refining temperatures of glass can be used for de-vitrification when transporting glass from the refiner to the shape of the chamber, and they are minimized in the absence of free fall and its reverse flow.  This occurs because, in the implementation of the proposed method, the immobility is reduced to a minimum.  The use of lower temperatures in the refiner provides better performance for a glass melting and refining furnace of a certain volume.  The spike-shaped optical distortion, visible along the lateral parts of the conventional glass tape, is significantly reduced by maintaining relatively uniform velocity gradients across the width of the float glass flow in the proposed device.  The proposed method provides for the production of glass of all useful thicknesses in continuous sheets of the same. thickness, so that for glasses of various thickness, you can use equipment to observe and cut the necessary lateral adjustment of this equipment.  - The invention is useful in the production of glass of any state, which can be molded using the float process, such as soda-lime-silica and borosilicate glass.  FIG.  1 shows a device for producing glass, a longitudinal section; in fig.  2 - section A-L ya.  FIG.  1, in FIG.  3 - unloading device; in fig. K is a device for producing glass, longitudinal section; in FIG. 5, the velocity profiles typical of the traditional float process in the manufacture of glass in FIG. 6 and 7 are the same for molten glass when implementing the proposed method; FIG.  8 - sheet glass, manufactured according to the Pilkington method, cross-section-, fmg.  9 the same, made according to the invention.  The device 1 for processing molten glass 2 is in communication with a discharge device 3, through which c. Molding glass flows through the forming chamber 2.  the forming chamber contains a molten metal bath 5.  glass with density 2, with the upper part of the molten metal adjustable to such a level that glass 2 can flow freely without falling onto the molten metal 5, and it can be pulled unidirectionally on the surface of the molten metal 5 through the forming chamber 6 for lifting from the forming chamber 4 a finished continuous sheet of glass.  The device 1 contains a refractory under 7, side walls 8 and the roof 9.  The zone of the molten metal source, in communication with the discharge device 3, is a cooled refiner with stepped hearth.  The refiner for molten glass or the processing device is designed and operated by Tai that the glass passing through it towards the discharge device is gradually cooled.  The refiner with stepped hearth and cooling from below contributes to the stabilization of the non-vortex flows.  The molten glass 2 is cooled to a temperature at which it is flowable; with continuous additional cooling, it can be molded into a dimensionally stable sheet of glass.  la  For glasses of typical sodium-limestone-silica composition, the temperature of the molten glass in the processing device at the closest point to the discharge device is approximately 9271204 ° C (1700-2200).  The discharge device 3 contains a threshold barrier 10 or other device that forms a support under the molten glass and separates the molten glass in the device for processing o6 from the molten metal 5 in the forming chamber k.  The upper part of the threshold area 10 is located 2-18 inches below the surface of the glass in the processing device.  The support contains a refractory element that can be provided with a device 11 for heating or cooling to control the temperature of the glass flowing in contact with the threshold, and thereby adjust the amount to which the threshold is wetted by the flowing molten glass.  In addition, the discharge device comprises side supports 12, which form the side walls of the channel through which molten glass can flow.  Along with this, the discharging device has an adjustable measuring device 13, which is a movable gate or valve, which passes down into the molten glass.  Depending on the vertical position of the valve 13, the flow of molten glass from the source of molten glass through the discharge gap is fed to the molten tin 5.  A9 At the beginning, the lateral size of this flow is determined by the space between the side supports 12.  This size can be maintained using guide elements or limiting elements I.  Restrictive elements 1 are parallel tracks made of, for example, graphite or alumina, which are wetted with the molten glass to a limited extent.  Limiting elements 14 can be provided with means for temperature control, for example, a device for heating or cooling the limiting elements.  The length of the limiting element co gives a longitudinal temperature gradient, so that there is a relatively greater wetting of the limiting elements with glass near the device for discharging the glass, compared with the wetting of limiting elements at the ends of the glass that are located downstream just before the glass held by limiting elements.  The length of the limiting elements is such that the molten glass can be sufficiently cooled while it is between the two limiting elements, so that inside the glass, after removing all the preventive measures, no outward side flow occurs.  On the molten metal, downstream. from the limiting elements, the molten salt can float so that it hits the glass and limits the sidestream.  For the production of glass that is thicker than traditional equilibrium glass, equilibrium side thresholds 15 are provided in the forming chamber downstream, where the glass is sufficiently cooled, so that stopping the traces or disturbing the glass flow is unlikely, and the layer 16 of molten salt is limited The space created by the side walls of the forming chamber i, pac and the downstream thresholds 15 and the limiting elements H with the tape 17 of the glass that is formed.  The molding chamber 4 is closed by a vault 18, where, in the direction of the upper surface of the floating continuous ribbon of glass 17, a row of heaters is mounted; lei 19 and refrigerators 20.  These devices are provided for controlled heating or cooling of the moving glass belt 17 so that the glass can be cooled and made up to a dimensionally stable ribbon of the required width and thickness to be removed from the forming chamber.  In addition, an inert gas source is connected to chamber i, as well as a source of reducing gas in order to prevent oxidation of the molten metal in the chamber (not shown).  Gas sources are typically used to direct nitrogen and.  hydrogen into the chamber. At the end of the forming chamber, an extracting roller 21 is mounted across the glass path that holds the belt 17 so as to lift it from the bath 5 of the molten metal.  A series of barriers 22 engages with the upper surface of the ribbon of glass 17 in order to isolate the atmosphere in the forming chamber 4 above the surface of the glass from the downstream processing equipment.  The barriers 22 are elastic asbestos sheets mounted and hanging from element 23 of the vault extending from vault 18 of the forming chamber A.  The pulling device, in addition to the pulling roller 21 and the barriers 22, contains a series of rollers 2.  which support the glass and create a longitudinal pulling force from the stack by drawing it out of the forming chamber and feeding it to the latest technological device, for example, to an annealing furnace.  The brushes 25 are in contact with the rollers 24, which additionally serve to separate the forms of the nagging chamber from the subsequent processing equipment.  From the rollers 24, as well as from the upstream rollers to the glass, a sufficient pulling force is exerted so as to unidirectionally reduce the size of the glass to its required final thickness, especially when its final thickness is less than the equilibrium thickness.  It has been established that by appropriately controlling the temperature and temperature gradient along the limiting elements T4, and appropriate application of traction force to the glass from the side of the rolls 24, it is possible to obtain glass that is less than the equilibrium thickness, without additional support from the side retaining elements and without lateral spreading that provides thin glass with a significant optical distortion, especially near its edges, compared with that observed in glass, tovl emom known industrial float form, the process ,,.  However, in order to reduce the size of glass tape while maintaining a constant width of the tape, a forced lateral limitation can be used. For this, vertical rollers 26 are used in combination with the main unit.  In addition, it is also possible to use glass cooling agent in the lower part of the treatment unit, which complements the cooling effect created by the stepped bottom.  The coolant supply pipe 27 can be immersed in glass, and through this immersed coolant a coolant, for example water, is continuously pumped through the pump.  This additionally stabilizes the warm conditions and provides an irrotational flow. While the 19 ° heaters and the refrigerators 20, located above the glass directly in current from the discharge device 3, are designed to provide cooling of the central part of the glass, they can also be used to heat the side windows. parts of glass flowing between equalizers 14. To this end, the guides are provided with a heating device 28.  In the discharge device 3 (FIG.  3) the molten metal 5 passes under the molten glass, flows through the discharge opening through a horizontal slit-like channel formed by the side stakes 12, the measuring device 13 and the molten metal.  Molten metal inside the bath; held by side walls 8 of the source of molten glass and threshold barrier 29 installed in the transverse direction relative to the width of the source of molten CTekna. The threshold barrier is made of an inert material, for example fused silica, or it can be a refractory block coated with platinum, molybdenum, graphite or nitride boron, Threshold (T) the obstacle from the hearth of the forming chamber 216 k is filled with a porous packing, for example, powdered graphite 30, and in order to cool the threshold barrier and bespechenii temperature control is provided in the discharge zone 31, a water crate.  The lower contact surface of the glass refractory is small, as a result of j4ero the possibility of contamination of the glass during the molding process is eliminated. A thin lubricating film of molten metal (Fig.) Molten glass 2 from the molten 1 device is provided between the supporting refractory element forming the lower part of the glass discharge channel. the glass flows through the threshold barrier 32 and through the relatively non-deep part 33 of the molten metal bath, which communicates with the main bath of the molten metal 5 into the molding It is provided with a thin film 3 passing over tray element 35, which forms the lower part of the discharge device 3.  The floating channel of the discharge device 3 is limited by side supports 12, a movable slide 13 which defines an upper limit, and a bottom or bottom tray element 35.  For the purpose of continuously supplying the molten metal to the shallow part 33 of the molten metal bath, in combination with the lower tray element, Bw means are provided for feeding the molten metal.  The flow of glass flowing through the discharging device brakes the molten metal in the shallow part 33 of the molten metal bath, forming a thin film 3 of molten metal and feeding the molten metal to the bulk of the molten metal in the forming chamber.  The formation of a thin lubricant film of molten metal provides a fairly long unloading path of exact cross-sectional dimensions, which ensures the formation of the finished glass sheet of precisely adjustable thickness, without resorting to a carefully designed reduction and thermal regulation in the forming chamber.  Example 1 To compare the flows and temperatures at each node, three separate glass processing and molding units were put into action.  Each of the processing devices has a stepped hearth construction (FIG.  ).  The effective width of each processing unit is 91 cm (3 in.).  One device for processing (FIG.  5) through a channel 102 cm wide (kQ inches) and 30 cm deep (12 inches), the lines of glass or the open surface of the glass inside the treatment device communicate with the traditional float-forming bath.  A second processing device (FIG.  6) communicates with the bath by means of a threshold supply means having an opening of a width of kS7 cm and a depth of 30 cm (180 and 12 inches respectively) below the glass mirror.  The third working device (FIG. 7) is identical to the second device, except for the fact that it has a loading means that is only 15 cm deep (6 inches) below the glass mirror.  R d thermocouple provides :.  Ren in each treatment device at the bottom, on the glass surface and at intermediate points on the centerline of the treatment device immediately against the flow from the discharge device, as well as on the centerline of the channel and the traditional device in -.  center line and near the outer walls or supports of the loading device used in this invention. All these plants operate under the same conditions in order to produce 500 tons of glass per day.  In tab.  1 shows the comparative data inside the glass, made by known. and  the proposed method In table.  Figure 2 shows the inside temperature data of the glass.  2 shows that heat generation from the table is obtained in the device formation.  for processing in carrying out the invention, improved.  A comparison of the velocities and temperatures in the three systems suggests that the invention has velocity profiles along the side width of the processing device, creating a flat and less curved neutral plane in order to make the flow non-vortex inside the outlet area of the processing device.  It is also evident from speeds and temperatures that the glass supplied from the refiner or the processing device according to the proposed method is more fully cooled without experiencing instability, compared with the glass obtained according to the known method.  As a consequence, using this method, it is possible to increase the productivity in comparison with the known method, without additional cooling equipment.  or the large-scale design of the treatment device.  The method is carried out with a small ω-threshold or loading device.  In the known methods, the normal flow plane is located approximately at the same distance from the bottom of the treatment device to the open felling in the midline of the translational flow.  However, in contrast to the traditional practice of implementing the invention, the forced flow over a conventional plane across the entire width of the processing device is much more even.  This improved uniformity of the velocity profile across the width of the processing unit is evidence of the improved vortex-free flow obtained by approaching the flow of glass; to the unloading device.  Example 2  In the device (FIG.  1 and 2) molten glass is fed to a bath of molten tin SQ t per day.  The glass temperature at the time of its supply to tin is about 10–5 ° C (1950 ° F) over the entire width, which is noted by conventional radiation pyrometers installed in the arch of the forming chamber and directed to the glass.  The side bounding elements or guides are located three meters (U ft) from each other and are not heated. wow.  They are insulated from the outer walls of the chamber.  The temperature of each rail in the vicinity of the discharge zone is about (1900 ° F), with the rails having a length of about 1.83 m (6 feet), and the temperature is about 897 ° C (1–50 ° P).  The temperatures of the guides are determined using thermocouples made of 10% platinum, and the guides made from alumina and hot-junction thermocouples approximately 1 inch above and 2 inches laterally from the surface of the molten glass are encased in refractory material.  Two refrigerators are located above the glass in the center of the zone between the rails.  Each of these coolers represents a cooling surface approximately 9 feet wide (1.52 m) (5 ft) wide and about 0.6 m (2 ft) long in the direction of the glass.  These refrigerators are equipped with a sufficient amount. water with a temperature of 2k ° C (), and water leaving the refrigerator has a temperature of about 2 ° C ().  Each refrigerator takes approximately 10,000 British thermal units per minute of heat from the chamber.  Three pyrometers in the chamber arch are directed onto the glass along the line connecting the downstream ends of the guides.  One pyrometer is directed along the centerline of the glass movement, while the others are approximately 6 inches inward from the inner surfaces of the respective guides.  The temperature in the center is about 871 ° C (1600 ° F); each of the two outer / temperatures around ().  A dimensionally stable glass oleite having a thickness of 0.210 inches and a width of 3 m (10 feet and 1 inch) is molded.  No vertical rolls are used for side stretching of glass.  The resulting glass tape has no distortion along its center over 284 cm (112 inches, approximately 10 cm (k inches) of glass on each edge and has visible distortion, and only the outermost parts extending inwards from the edges approximately 5 cm ( 2 inches, have a strong spike distortion.  The proposed method provides a continuous stack of 2 1 tapes, which has an improved optical property as compared to. fiberglass made according to the known float-pro-process.  This improvement is evident when viewed through the glass in a direction perpendicular (when it intersects) to the main plane of the glass.  In the case when the glass obtained according to the invention is examined along the cut width direction, it becomes obvious that the structures inside the glass are different from the known ones.  structures.  Glass manufactured according to a known method exhibits a characteristic, figurative shape near the convex end.  This structure destroys the continuity of the resulting layered structure, appearing noticeably in glass obtained by the method of the company Pilke ngton.  In contrast, the glass obtained according to the invention has an embedded laminated structure extending to the edges of the tape. While the known glass has a characteristic distortion line corresponding to the visible surface of unexpectedly appearing continuity in the T-shaped structure, the glass does not have continuous lateral distortion line.  The application of the proposed method will allow to obtain glass having a wide range of thickness with improved optical properties.  Table 1
    Surface 7 13 55
    25 32 38 27
    51
    .b
    0
    15.8
    12.2
    15.8
    15.8 15.8
    12
    9.2
    0 0
    5.6
    Q
    about
    Continued table. one
    23
    1118
    1135
    Proposed: Claim 1, A method of making sheet glass, including unloading glass onto the surface of molten metal to form a laminar flow, forming glass mass into ribbon, advancing a belt along a bath and withdrawing from it, characterized in unloading of the glass mass is carried out through a threshold, the top surface of which is located at the level of the molten metal, and the glass mass is molded into a ribbon with a decrease in temperature by 3.6-27, for each met glass in the direction of its advance. i 2, Method pop. 1, differing from the fact that when molding glass mass into a ribbon, it is carried out up to 923362
    table 2
    1185 1169
    1101 additional heating of its side sections to the temperature of the central part. 3. Method PP.1 and 2, that is, so that when the glass mass is molded into a ribbon, its central part is further cooled to its lateral temperature. . V, The method according to PP, 1-3, about tl and h and n and so that the promotion of the central part of the molten glass along the bath is carried out with a speed equal to 1-5 times the speed on its side portions. Sources of information taken into account in the examination 1. The author's certificate of the USSR tr 212866, cl. C 03 B 18/02, 1966. 2. German Patent No. 1i7l829, 32a 18/02 1970.

    l (rf f III LP
    - MB 20 / figure.$
    13
    17
    权利要求:
    Claims (4)
    [1]
    1, A method of manufacturing sheet glass, including unloading the glass melt onto the surface of the molten metal to form a laminar flow, forming glass melt into tape *, moving the tape along the bath and output from it, characterized in that, in order to improve the optical properties of the glass, unloading the glass melt carried out through a threshold, the upper surface of which is located at the level of the molten metal, and the formation of molten glass into a tape is carried out with a decrease in temperature by 3.6-27,
    2 in C for each meter of glass in the direction of its advancement.
    i
    [2]
    2. The method according to claim 1, with the fact that when molding molten glass B, additional heating of its side sections is carried out to a temperature of the central part.
    [3]
    3. 'The method according to claims 1 and 2, which includes the fact that when molding the glass melt into a tape, additional cooling of its center of the alt part to the temperature of its side parts is carried out.
    [4]
    . 4. The method according to claims 1-3, with the fact that the central part of the molten glass along the bath is carried out at a speed equal to 1-5 times the speed on its side sections.
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    同族专利:
    公开号 | 公开日
    GB1469283A|1977-04-06|
    GB1469285A|1977-04-06|
    ES423917A1|1976-06-01|
    IE39156B1|1978-08-16|
    BE811088A|1974-08-16|
    NL162884C|1980-07-15|
    BR7401588D0|1974-12-24|
    FR2220485B1|1978-07-13|
    JPS593408B2|1984-01-24|
    ZA74732B|1975-09-24|
    DK150648C|1987-11-30|
    IT1009209B|1976-12-10|
    NZ173324A|1978-04-28|
    NL162884B|1980-02-15|
    SE408789B|1979-07-09|
    JPS5029624A|1975-03-25|
    FR2220485A1|1974-10-04|
    CA1035955A|1978-08-08|
    IE39156L|1974-09-06|
    AR200911A1|1974-12-27|
    DE2408867B2|1977-03-03|
    ES446052A1|1977-06-01|
    NL7402307A|1974-09-10|
    DK150648B|1987-05-11|
    SE7402870L|1974-09-09|
    CS174233B2|1977-03-31|
    US3843346A|1974-10-22|
    AU6532374A|1975-08-07|
    IN141332B|1977-02-12|
    DE2408867A1|1974-09-19|
    ES423918A1|1976-10-16|
    引用文献:
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US00338497A|US3843346A|1973-03-06|1973-03-06|Manufacture of sheet glass by continuous float process|
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