CA1069700A - Thermal treatment of glass - Google Patents
Thermal treatment of glassInfo
- Publication number
- CA1069700A CA1069700A CA259,724A CA259724A CA1069700A CA 1069700 A CA1069700 A CA 1069700A CA 259724 A CA259724 A CA 259724A CA 1069700 A CA1069700 A CA 1069700A
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- CA
- Canada
- Prior art keywords
- glass
- bed
- particles
- range
- cal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B27/00—Tempering or quenching glass products
- C03B27/04—Tempering or quenching glass products using gas
- C03B27/0413—Stresses, e.g. patterns, values or formulae for flat or bent glass sheets
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B27/00—Tempering or quenching glass products
- C03B27/04—Tempering or quenching glass products using gas
- C03B27/052—Tempering or quenching glass products using gas for flat or bent glass sheets being in a vertical position
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B29/00—Reheating glass products for softening or fusing their surfaces; Fire-polishing; Fusing of margins
- C03B29/02—Reheating glass products for softening or fusing their surfaces; Fire-polishing; Fusing of margins in a discontinuous way
- C03B29/025—Glass sheets
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mathematical Physics (AREA)
- Re-Forming, After-Treatment, Cutting And Transporting Of Glass Products (AREA)
- Glass Compositions (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
- Glass Melting And Manufacturing (AREA)
Abstract
A B S T R A C T
The thermal treatment of glass is effected by heat tran-sfer between the glass and a gas-fluidised particulate material which is in a quiescent uniformly expanded state of particulate fluidisation. Class sheets are thermally toughened by immersing each glass sheet, which is at a temperature above its strain point, in the gas-fluidised bed which is in said quiescent state prior to the immersion of the glass in the bed.
The thermal treatment of glass is effected by heat tran-sfer between the glass and a gas-fluidised particulate material which is in a quiescent uniformly expanded state of particulate fluidisation. Class sheets are thermally toughened by immersing each glass sheet, which is at a temperature above its strain point, in the gas-fluidised bed which is in said quiescent state prior to the immersion of the glass in the bed.
Description
;97QO
IMæROVEMENTS IN OR RELATING TO THE THERMAL TREATMENT OF GLASS
This invention relates to the thermal treatment of glass, and more especially to the thermal toughening of glass articles, for example flat glass or bent glass sheets. Such thermally toughened glass sheets may be for use singly as a motor vehicle windscreen, or as part of a laminated motor vehicle windscreen, a side light or rear light for a motor vehicle, or for use in the construction of windscreen assemblies for aircraft and railway locomotives, or in the construction of windows for ships, or for architectural uses. Other glass articles such as pressed or blown glass articles may be therm-ally toughened by the method of the invention.
The ultimate tensile strength of a glass article can be increased by a thermal toughening process in which the glass is heated to a temperature approaching its softening point, followed by rapid chilling of the glass surfaces to induce centre-to-surface temperature gradients through the thickness of the glass. These temperature gradients are maintained as the glass is cooled through its strain point. This results in compressive stress in the surface layers of the glass sheet with compensating tensile stress in the central core of the thickness of the glass sheet.
Usually this thermal toughening process is carried out using chilling air directed uniformly at both surfaces of the glass sheet but it is difficult to obtain a high degree of toughening using air flows, particularly when toughening glass sheets of 3 mm thickness or less. Attempts to increase the de-gree of toughening of a glass sheet by increasing the rate of flow of cooling air can give rise to loss of optical quality of the surfaces of the glass and distortion of the shape of the - ' ' 10~9~
glass sheet due to the buffeting action of the chilling air.
In another thermal toughening process a glass sheet at a temperature near to ïts softening poïnt is quenched in a chilling liquid. High stresses can be produced by this method.
The glass sheets have to be cleaned after quenchïng.
Thermal toughenïng of a glass sheet has also been proposed by a method in which a hot glass sheet is immersed in what, in practice, was a freely-bubbling fluidised bed of solid particles, for example sand.
Such a process has not been brought into commercial use hitherto.
The major problem which we have found when attempting to operate such a bed for the thermal toughening of glass is the high incidence of fracture of the glass sheets during their treatment in the fluidised bed. The fracture of a glass sheet while being quenched in a freely-bubbling fluidised bed is thought to be caused by the induction of destructive tensile stresses in the leading edge of the glass sheet due to non-uniform cooling as the leading edge enters the bed of particles in a state of bubbling or aggregative fluidisation.
Loss of glass sheets due to fracture is particularly serious when attempting to toughen thin sheets of gJass, for example of thickness from 2.3 mm to 4.0 mm, to a high stress value, and has been such as to render the process unacceptable for the commercial production of toughened glass sheets for use in car windscreens for example. The problem of fracture also arises to a lesser but still commercially significant extent when seeking to toughen thicker sheets, for example up 106~700 to 8 mm thick.
A freely-bubbling bed in a state of aggregative fluidisation has also been found to damage hot glass sheets immersed in it. This is due to the irregular forces to which the glass is subjected in a freely-bubbling bed. This can give rise both to changes of overall shape and to more localised surface damage, the former occurring particularly with thinner glass sheets such as those of 2 mm to 3 mm thickness. Such damage as changes of shape may give rise to difficulties in lamination, and surface damage may give rise to unacceptable optical quality when the sheet is used as a window or as a component of a laminated window.
The present invention is based on the discovery that the use of a gas-fluidised bed in a quiescent uniformly expanded state of particulate fluidisation unexpectedly produces adequate stresses in glass sheets quenched in it and substantially reduces loss of glass sheets due to fracture in the bed or to change of shape or surface damage so that a successful commercial yield is achieved.
According to the invention there is provided a method of thermally treating glass in which the glass is con-tacted with a gas-fluidised particulate material which is in a quiescent uniformly expanded state of particulate fluidisation, to effect heat transfer between the surfaces of the glass and the fluidised material.
The invention further provides a method of thermally treating glass, comprising heating the glass to a temperature above its strain point and immersing the glass in a gas-fluid-ised bed of particulate material which prior to said immersion is in a quiescent uniformly expanded state of particulate fluidisation.
The inventIon is particularly concerned with the thermal toughening of glass sheets and provides a method of thermally toughening a glass s-heet comprising heating the glass sheet and then lowering the hot glass sheet into the quiescent uniformly expanded bed of particulate material.
Preferably the bed is maintained at a temperature in the range 30C and 150C. This temperature is selected in dependence on the fluidisation characteristics of the particles and the required level of stress in the toughened sheets.
The fluidised bed of particulate material in a quiescent uniformly expanded state of particulate fluidisation, which is employed in carrying out the invention, can be defined in terms of the velocity of gas flow through the bed and the expanded height of the bed. The quiescent uniformly expanded state of particulate fluidisation exists between a lower limit of gas velocity at incipient fluidisation, that is the velocity at which the particles just become suspended in the uniformly distributed upwardly flowing gas, and an upper limit of gas velocity at which maximum expansion of the bed occurs while maintaining a free surface at the top of the bed.
The upper limit of fluidisation gas velocity may exceed by a small amount the velocity at which the first clearly recognisable bubble, for example 5 mm in diameter, is seen to break the calm surface of the bed. One or two such bubbles may be visible at the gas velocity.
A higher gas velocity results in the development of extensive bubbling in the bed and at the onset of such bubbling - 1065~700 there is partial collapse of the bed height.
We believe that by quenching the sheet in a gas-fluid- -ised bed which is in a quiescent uniformly expanded state of particulate fluidisation, any transient tensile stresses in-duced in the leading edge of the glass sheet on entry into the fluidised bed are not so severe as to endanger the glass sheet and to cause it to fracture.
Also the substantially bubble-free nature of the bed ensures that the hot glass is not subjected to irregular forces such as could also give rise to fracture, or to changes in shape of the glass sheet during quenching, or to surface damage.
Previously it has been thougllt that, to obtain a high heat transfer coefficient between a fluidised bed and an article immersed in it, it is desirable to maintain a freely bubbling condition, such that the rapid and continuous movement of the particles can give rise to transfer of heat between the article and the bulk of the bed. This, it was thought, would not occur in a quiescent bed where the particle movement is less. However it has now been found that unexpectedly high heat transfer coefficients are obtained between a hot glass article and a cooler bed of fluidised particulate material in a quiescent uniformly expanded state and having selected characteristics.
It is found that there is thermal agitation of the uniformly fluidised particulate material at the hot glass surfaces when a hot glass sheet is quenched in the bed and there is greater rapidity of movement and turbulence of the fluidised particles in the region of the surfaces of the glass sheet than in the bulk of the bed. This results in a high rate of transfer of heat away from the glass surfaces. It is thought that , ~0697Q(~
particles which become heated by passing in proximity to the glass surfaces then move rapidly away from the glass sheet and lose heat to the fluidising air in the bulk of the bed.
A preferred method according to the invention includes regulating the gas flow to maintain said quiescent state of the fluidised bed by creating a high pressure drop in the fluidis-ing gas flow across a membrane through which fluidising gas enters the bed.
Further according to the invention the particulate material may comprise particles of density in the range 0.3 g/cm3 to 3.97 g/cm3 and mean particle size in the range 5~m to l20~m, the material being selected so as to be fluidised in said uniform quiescent state by fluidising gas flowing uniformly in the bed at a velocity in the range 0.045 cm/s to 5.61 cm/s.
The density of the particles and their mean particle sizes are both important in determining the suitability of a particulate material for consitituting the fluidised bed in a quiescent uniformly expanded state employed in the method of the invention. Generally an appropriate particulate material for fluidisation in a quiescent uniformly expanded state by fluidising air, when the bed is operating in ambient conditions of normal room temperature and pressure, is one for which the numerical product of the particle density, in g/cm3, and the mean particle size inJlm, does not exceed about 220.
The degree of toughening of a glass sheet which is achieved by the method of the invention depends on the heat transfer coefficient between the fluidised particulate material and the hot glass sheet immersed in it. As already described there is thermal agitation on the hot glass surfaces which give rise to transfer of heat rapidly away from those surfaces. How-ever the properties of the particles themselves also affect the magnitude of the heat transfer coefficient.
For thermally toughening flat soda-lime-silica glass of thickness in the range 2.3 mm to 12 mm, the method of the in-vention may comprise heating the glass to a temperature in the range 610C to 680C, immersing the glass in a fluidised bed in said quiescent state which has a thermal capacity per unit volume at minimum fluidisation in the range 0.02 cal/cm3C to 0.37 cal/
cm3C, and maintaining the fluidised bed at a temperature up to 150C to induce in the glass an average central tensile stress in the range 22 MN/m2 to 115 MN/m2.
The maximum magnitude of average central tensile stress which can be achieved varies with the thickness of the glass and the heat transfer coefficient. By selection of a suitable mater-ial the heat transfer coefficient can be made high enough to prod-uce toughened glass sheets having a central tensile stress as high as 40 MN/m2 in glass 2 mm thick, a central tensile stress as high as 50 MN/m2 in glass 3.0 mm thick, and a central tensile stress as high as 104 MN/m2 in glass which is 12 mm thickness. However even higher central tensile stresses than these have been achieved as is shown in some of the Examples.
The particles may be a non-porous powdered a alumina of mean particle size in the range 23,~m to 54~um and particle density 3.97 g/cm3, the thermal capacity per unit volume of the bed at min-imum fluidisation being 0.32 cal/cm3C.
The invention also provides a fluidised bed for use as a quenching medium for thermally toughening a hot glass sheet, 10697Qo comprising particles of mean particle size in the range 5~um to 120~um and having a particle density in the range 0.3 g/cm3 to 3.97 g/cm3, and wherein the particles are so selected that the bed is in a quiescent uniformly expanded state of particulate fluidisation and has a thermal capacity per unit volume at minimum fluidisation in the range 0.02 cal/cm3C to 0.37 cal/cm3C.
The invention also comprehends a method of thermally treating glass in which the glass is contacted with a gas-fluidised particulate material of non-compacted particle structure which is such that the apparent density of the particles is less than the actual density of the material forming the particles and the buoy-ant particles constitute a gas-fluidised bed in a quiescent unif-ormly expanded state of particulate fluidisation, the material forming the particles and the temperature of the bed being so sel-ected that the heat transfer coefficient of the fluidised bed is sufficient to produce a desired thermal treatment of the glass as it cools in the bed.
The invention still further comprehends a method of the-rmally toughening glass, comprising heating the glass and immersing the hot glass in a gas-fluidised bed of particles of non-compacted particle structure which is such that the apparent density of the particles is less than the actual density of the material forming the particles and the buoyant particles constitute a gas-fluidised bed in a quiescent uniformly expanded state of particulate fluid-isation, the material forming the particles and the temperature of the bed being so selected that the heat transfer coefficient of the fluidised bed is sufficient to produce desired toughening stresses in the glass as it cools in the bed.
The use of particles of non-compacted structure permits the selection of a material for the particles to give a fluidised bed having a sufficiently high thermal capacity per unit volume at minimum fluidisation to produce a high amount of toughening stress in the glass whilst avoiding difficulties in fluidisation of such a material in a quiescent uniformly expanded state of particulate fluidisation.
The amount of toughening stress produced in the glass using a fluidised bed comprising particles of a particular non-compacted material can be controlled by selection of the particle density. Particles of low density and of a particular size res-ult in the production of a low amount of toughening stress in the glass, and the amount of toughening stress produced increases with increasing particle density up to the maximum density of particles of such size that they are still fluidised in said quiescent state.
Still further the invention provides a method for therm-ally toughening a glass sheet, comprising immersing a hot glass sheet in a fluidised bed in said quiescent state and constituted by particles of mean particle size in the range 5~m to 120,~m and apparent particle density in the range 0.3 g/cm3 to 2.35 g/cm3, the thermal capacity per unit volume of the bed at minimum fluid-isation being in the range 0.02 cal/cm3C to 0.37 cal/cm3C.
The apparent particle density within a range as set out above is the actual measured density of the particulate material taking into account the cavities within the particles, and is to be distinguished from the true density of the material itself.
By selecting the mean particle size in relation to the apparent particle density, the suitability of particles of non-compacted material for constituting the quiescent uniformly ex-panded fluidised bed can be assessed. Preferably the numerical value of the product of the apparent particle density, in g/cm3, and the mean particle size in ~um, should not exceed about 220.
Still further the invention provides a method of ther-mally toughening glass, comprising heating the glass, and immersing 10697(~0 the hot glass in a gas-fluidised bed of porous particles in a quiescent uniformly expanded state of particulate fluidisation, the material forming the particles and the temperature of the bed being so selected that the heat transfer coefficient of the fluidised bed is sufficient to induce desired toughening stresses in the glass as it cools in the bed.
The particles may be porous particles of ~ alumina of mean particle size 64~m and apparent particle density 2.2 g/cm , the thermal capacity per unit volume of the bed at minimum fluid-isation being 0.21 cal/cm3C.
In yet another embodiment the particles are of a porous form of aluminosilicate material of mean particle size in the range 60~m to 75~m and apparent particle density in the range 1.21 g/cm3 to 1.22 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being in the range 0.11 cal/cm3C
to 0.19 cal/cm3C.
Further the particles may be of porous powdered nickel of mean particle size 5~m and apparent particle density 2.35 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being 0.37 cal/cm3C.
Further according to the invention a method of thermally toughening glass comprises heating the glass, and immersing the hot glass in a gas-fluidised bed of hollow particles in a quies-cent uniformly expanded state of particulate fluidisation, the material forming the particles and the temperature of the bed being so selected that the heat transfer coefficient of the fluid-ised bed is sufficient to induce desired toughening stresses in the glass as it cools in the bed.
The particles may be hollow glass spheres of mean part-icle size in the range 77~m to 120~m and apparent particle density 0.38g/cm3, the thermal capacity per unit volume of the , ., ~
bed at minimum fluidisation being in the range 0.05 cal/cm3C to 0.06 cal/cm3C.
In a further embodiment the particles are hollow carbon spheres of mean particle size 48~m, and apparent particle density 0.3 g/cm3, the thermal capacit-y per unit volume of the bed at minimum fluidisation being 0.02 cal/cm3C.
The invention also comprehends a fluidised bed for use as a quenching medium for thermally toughening a hot glass sheet, comprising particles of non-compacted particle structure which is such that the apparent density of the particles is less than the actual density of the material forming the particles, wherein the mean particle size of the particles is in the range 5~m to 120~um the apparent particle density is in the range 0.03g/cm3 to 2.35 g/cm3, and wherein the particles are so selected that the bed is in a quiescent uniformly expanded state of particulate fluidisa-tion and has a thermal capacity per unit volume of the bed at minimum fluidisation in the range 0.02 cal/cm3C to 0.37 cal/cm3C.
The invention also includes thermally treated glass produced by the method of the invention; in particular a thermally toughened glass sheet produced by the method of the invention.
In order that the invention may be more clearly under-stood some embodiments thereof will now be described, by way of example, with reference to the accompanying drawings in which:-Figure 1 illustrates diagrammatically a verticalsection through apparatus for carrying out the method of the invention, /
~.069700 Figure 2 is a detail in section of part of Figure 1, and Figure 3 is a graph which illustrates a character-istic of a gas-fluidised bed in a quiescent uniformly expanded state of particulate fluidisation, which is employed in carrying out the invention.
Referring to Figure 1 of the drawings, a vertical toughening oven indicated generally at 1 has side walls 2 and a roof 3. The side walls 2 and the roof 3 are made of the usual refractory material and the bottom of the oven is open, being defined by an elongated aperture 4 in a baseplate 5 on which the oven 1 is supported. A movable shutter, not shown, is provided in known manner to close the aperture 4.
A sheet of glass 6 to be bent and subsequently thermally toughened is suspended in the oven 1 by tongs 7 which engage the upper margin of the sheet 6 and are held closed in customary manner by the weight of the glass sheet gripped between the tong points. The tongs 7 are suspended from a tong bar 8 which is suspended from a conventional hoist, not shown, and which runs on vertical guide rails 9 which extend downwardly from the oven to guide the lowering and raising of the tong bar 8.
A pair of bending dies 10 and 11 are located on either side of the path of the glass sheet 6 in a chamber 12, which is heated by hot gas flows through ducts 12a. me interior of the chamber 12 and the dies 10 and 11 are maintained at the same temperature as the temperature of the hot glass sheet 6 as it enters the chamber 12.
- .
The die 10 is a solid male die mounted on a ram 13 and has a curved front face which defines the curvature to be imposed on the hot glass sheet. The die 11 is a ring frame female die carried by struts 14 mounted on a backing plate 15 which is mounted on a ram 16. The curvature of the die frame 11 matches the curvature of the face of the male die 10.
The guide rails 9 extend downwardly through the chamher 12 to either side of the bending dies towards a container for a gas-fluidised bed 17 of particulate refractory material in which the hot bent glass sheet is to be quenched. The container for the fluidised bed comprises an open-topped rectangular tank 18 which is mounted on a scissors-lift platform 19. When the platform 19 is in its raised position the top edge of the tank 18 is just below the bending dies 10 and 11.
A micro-porous membrane 20, which is described in greater detail with reference to Figure 2, extends across the base of the tank 18. The edges of the membrane 20 are fixed between a flange 21 on the tank and a flange 22 on a plenum chamber 23 which forms the base of the tank. The flanges and the edges of the membrane 20 are bolted together as indicated at 24. A gas inlet duct 25 is connected to the plenum chamber and fluidising air is supplied to the duct 25 at a regulated pressure. The membrane is so constructed that fluidising air flows uniformly into the fluidised bed over the whole base of the bed to maintain the bed in a quiescent uniformly expanded state of particulate fluidisation.
Particulate refractory material in the tank 18 is maintained in the quiescent uniformly expanded state of 1069~7QO
particulate fluidisation by the upward flow of air uniformly distributed by the porous membrane 20. The expanded bed is in a substantially bubble-free quiescent state and there are no regions of the bed which are not fluidised.
A preferred construction of micro-porous membrane is shown in Figure 2 and is described in Canadian Application Serial No. 279,877. This membrane comprises a steel plate 26 which has a regular distribution of holes 27. The margins of the plate are drilled to provide passages for bolts 24. A
lQ gasket 28 is located between the lower face of the margins of the plate and the flange 22 on the plenum chamber.
A number of layers 29 of strong micro-porous paper are laid on the plate 26. For example fifteen sheets of paper may be used. The membrane is completed with a woven wire mesh 30, for example stainless steel mesh which is laid on top of the paper. An upper gasket 31 is located between the margins of the wire mesh 30 and the flange 21 on the tank.
A basket for catching cullet may be located near the membrane 20, and is designed so as not to interfere with the uniform flow of fluidising air upwardly from the membrane.
Referring again to Figure 1, the guide rails 9 extend downwardly to a position below the bending dies and terminate in the region of the upper edge of the tank 18. A fixed frame indicated at 32 is mounted in the tank 18 and has upturned feet 33 at its base to receive the lower edge of a glass sheet lowered into the fluidised bed when the tong bar 8 is lowered beyond the bending dies by the hoist.
With the scissors-lift table 19 lowered and the tongs 7 and tong bar 8 in their lowermost position at the bottom of `` 1069700 the guides 9, a cool glass sheet to be bent and toughened is loaded onto the tongs. The hoist then raises the suspended glass sheet into the oven 1 which is maintained at a temper-ature, for example 850C, when toughening soda-lime-silica glass. The glass sheet is rapidly heated to a temperature near~ts softening point for example a temperature in the range 610C to 680C.
When the glass sheet has reached a required temperat-ure uniformly, the shutter closing the aperture 4 is opened and the hot glass sheet is lowered by the hoist into position between the open bending dies 10 and 11. The rams 13 and 16 are operated and the dies close t~ bend the sheet. When the required curvature has been imparted to the sheet the dies open and the hot bent glass sheet is rapidly lowered into the fluidised bed in the tank 18 which has been raised to quenching position by operation of the scissors-lift table 19 while the glass sheet was being heated in the oven 1.
When high quality laminated glass products are to be produced incorporating thermally toughened glass sheets produced by quenching in a fluidised bed an improvement in optical quality has been observed when the surfaces of the glass sheet are subjected to a preliminary air cooling just before the glass is immersed in the fluidised bed. This may be achieved by locating just above the upper edge of the tank 18 shallow blowing frames which direct cooling air onto the surfaces of the bent glass sheet as it leaves the bending dies and enters the fluidised bed.
The preliminary surface cooling is effective to "set-up"
' ' ' ' ' ' ' U`.~! ' '-' 1069700 the surfaces of the glass sheet and thereby avoid minute variations in those surfaces such as have sometimes been observed and which may be due to the thermal agitation of the fluidised particulate material on the glass surfaces.
Such preliminary surface cooling would however only usually be employed when the glass is being used for the production of laminates of high optical quality.
The fluidlsed bed is maintained at a suitable temperat-ure for inducing a required central tensile stress in the glass, -for example 30C to 150C, by the water cooling jackets 34 on the flat longer walls of the tank 18, and by controlling the temperature of the fluidising air supplied to the plenum ;
chamber 23. The jackets 34 act as a heat sink which absorbs heat transferred through the bed from the hot glass sheet.
The lower edge of the hot glass sheet is uniformly ch~lled along its whole length as it enters the horizontal quiescent surface of the expanded fluidised bed so that there is no possibility of diffërent tensile stresses being generated in different areas of the surface of that edge of ~ -- 20 the glass, such as could lead to fracture. During its descent ~-. ~' ' ,' ~
into the bed the lower edge always contacts fluidised material in a quiescent uniformly expanded state of particulate fluid-isation, and this uniform treatment of the lower edge, regard-less of upward flow of particulate material which may be generatedcn the hot glass surfaces immediately after they enter the fluidised bed, largely obviates fracture and the problems of dealing with glass fragments in the bed. This together with the avoidance of losses of glass sheets due to change of shape of the glass sheets and/or damage to the surface quality, ensures a commercially viable yield of toughened glasses.
Localised thermal agitation of the fluidised bed takes place on the hot glass surfaces, perhaps by rapid gas expansion in a manner akin to the boiling of a liquid. The agitation ensures that there is adequate heat transfer away from the glass surfaces into the bulk of the fluidised bed, for example heat transfer coefficients between the bed and the glass sheet in the range 0.003 cal/cm2C sec to 0.02 cal/cm2C sec are obtained. The heat transfer continues until well after the glass has cooled below its strain point, with sufficient severity to ensure that the centre-to-surface temperature gradients are maintained as the glass cools through its strain point, and the toughening stresses are developed thereafter during the continuous cooling of the glass while it is still immersed in the bed.
The agitation of the fluidised material at the glass surfaces sets up currents in the bulk of the bed which ensure continual dissipation to the remoter parts of the bed of the -heat which is extracted from the glass by the thermal agitation of the bed in the region immediately surrounding the glass sheet.
The water cooling jackets 34, acting as a heat sink, keep those remoter parts of the bed cool.
The sheet engages the feet 33 of the frame 32 at the bottom of its descent, thereby releasing ~he tongs 8. The glass sheet then rests on the frame 32 while the glass sheet cools in the fluidised ked. The glass sheet remains in the fluidised bed until it is cooled sufficiently to be handled and the tank 18 is lowered by lowering the scissors-lift platform to expose the fixed frame 32 and the supported toughened glass sheet which is then removed for subsequent cooling to room temperature. .
The nature of the quiescent uniformly expanded state of particulate fluidisation of the fluidised bed is illustrated in Figure 3 which is a plot of plçnum pressure, that is, the pressure in the plenum chamber, against the height of the bed in the tank 18 using ~ alumina particles as described in Example 1 -
IMæROVEMENTS IN OR RELATING TO THE THERMAL TREATMENT OF GLASS
This invention relates to the thermal treatment of glass, and more especially to the thermal toughening of glass articles, for example flat glass or bent glass sheets. Such thermally toughened glass sheets may be for use singly as a motor vehicle windscreen, or as part of a laminated motor vehicle windscreen, a side light or rear light for a motor vehicle, or for use in the construction of windscreen assemblies for aircraft and railway locomotives, or in the construction of windows for ships, or for architectural uses. Other glass articles such as pressed or blown glass articles may be therm-ally toughened by the method of the invention.
The ultimate tensile strength of a glass article can be increased by a thermal toughening process in which the glass is heated to a temperature approaching its softening point, followed by rapid chilling of the glass surfaces to induce centre-to-surface temperature gradients through the thickness of the glass. These temperature gradients are maintained as the glass is cooled through its strain point. This results in compressive stress in the surface layers of the glass sheet with compensating tensile stress in the central core of the thickness of the glass sheet.
Usually this thermal toughening process is carried out using chilling air directed uniformly at both surfaces of the glass sheet but it is difficult to obtain a high degree of toughening using air flows, particularly when toughening glass sheets of 3 mm thickness or less. Attempts to increase the de-gree of toughening of a glass sheet by increasing the rate of flow of cooling air can give rise to loss of optical quality of the surfaces of the glass and distortion of the shape of the - ' ' 10~9~
glass sheet due to the buffeting action of the chilling air.
In another thermal toughening process a glass sheet at a temperature near to ïts softening poïnt is quenched in a chilling liquid. High stresses can be produced by this method.
The glass sheets have to be cleaned after quenchïng.
Thermal toughenïng of a glass sheet has also been proposed by a method in which a hot glass sheet is immersed in what, in practice, was a freely-bubbling fluidised bed of solid particles, for example sand.
Such a process has not been brought into commercial use hitherto.
The major problem which we have found when attempting to operate such a bed for the thermal toughening of glass is the high incidence of fracture of the glass sheets during their treatment in the fluidised bed. The fracture of a glass sheet while being quenched in a freely-bubbling fluidised bed is thought to be caused by the induction of destructive tensile stresses in the leading edge of the glass sheet due to non-uniform cooling as the leading edge enters the bed of particles in a state of bubbling or aggregative fluidisation.
Loss of glass sheets due to fracture is particularly serious when attempting to toughen thin sheets of gJass, for example of thickness from 2.3 mm to 4.0 mm, to a high stress value, and has been such as to render the process unacceptable for the commercial production of toughened glass sheets for use in car windscreens for example. The problem of fracture also arises to a lesser but still commercially significant extent when seeking to toughen thicker sheets, for example up 106~700 to 8 mm thick.
A freely-bubbling bed in a state of aggregative fluidisation has also been found to damage hot glass sheets immersed in it. This is due to the irregular forces to which the glass is subjected in a freely-bubbling bed. This can give rise both to changes of overall shape and to more localised surface damage, the former occurring particularly with thinner glass sheets such as those of 2 mm to 3 mm thickness. Such damage as changes of shape may give rise to difficulties in lamination, and surface damage may give rise to unacceptable optical quality when the sheet is used as a window or as a component of a laminated window.
The present invention is based on the discovery that the use of a gas-fluidised bed in a quiescent uniformly expanded state of particulate fluidisation unexpectedly produces adequate stresses in glass sheets quenched in it and substantially reduces loss of glass sheets due to fracture in the bed or to change of shape or surface damage so that a successful commercial yield is achieved.
According to the invention there is provided a method of thermally treating glass in which the glass is con-tacted with a gas-fluidised particulate material which is in a quiescent uniformly expanded state of particulate fluidisation, to effect heat transfer between the surfaces of the glass and the fluidised material.
The invention further provides a method of thermally treating glass, comprising heating the glass to a temperature above its strain point and immersing the glass in a gas-fluid-ised bed of particulate material which prior to said immersion is in a quiescent uniformly expanded state of particulate fluidisation.
The inventIon is particularly concerned with the thermal toughening of glass sheets and provides a method of thermally toughening a glass s-heet comprising heating the glass sheet and then lowering the hot glass sheet into the quiescent uniformly expanded bed of particulate material.
Preferably the bed is maintained at a temperature in the range 30C and 150C. This temperature is selected in dependence on the fluidisation characteristics of the particles and the required level of stress in the toughened sheets.
The fluidised bed of particulate material in a quiescent uniformly expanded state of particulate fluidisation, which is employed in carrying out the invention, can be defined in terms of the velocity of gas flow through the bed and the expanded height of the bed. The quiescent uniformly expanded state of particulate fluidisation exists between a lower limit of gas velocity at incipient fluidisation, that is the velocity at which the particles just become suspended in the uniformly distributed upwardly flowing gas, and an upper limit of gas velocity at which maximum expansion of the bed occurs while maintaining a free surface at the top of the bed.
The upper limit of fluidisation gas velocity may exceed by a small amount the velocity at which the first clearly recognisable bubble, for example 5 mm in diameter, is seen to break the calm surface of the bed. One or two such bubbles may be visible at the gas velocity.
A higher gas velocity results in the development of extensive bubbling in the bed and at the onset of such bubbling - 1065~700 there is partial collapse of the bed height.
We believe that by quenching the sheet in a gas-fluid- -ised bed which is in a quiescent uniformly expanded state of particulate fluidisation, any transient tensile stresses in-duced in the leading edge of the glass sheet on entry into the fluidised bed are not so severe as to endanger the glass sheet and to cause it to fracture.
Also the substantially bubble-free nature of the bed ensures that the hot glass is not subjected to irregular forces such as could also give rise to fracture, or to changes in shape of the glass sheet during quenching, or to surface damage.
Previously it has been thougllt that, to obtain a high heat transfer coefficient between a fluidised bed and an article immersed in it, it is desirable to maintain a freely bubbling condition, such that the rapid and continuous movement of the particles can give rise to transfer of heat between the article and the bulk of the bed. This, it was thought, would not occur in a quiescent bed where the particle movement is less. However it has now been found that unexpectedly high heat transfer coefficients are obtained between a hot glass article and a cooler bed of fluidised particulate material in a quiescent uniformly expanded state and having selected characteristics.
It is found that there is thermal agitation of the uniformly fluidised particulate material at the hot glass surfaces when a hot glass sheet is quenched in the bed and there is greater rapidity of movement and turbulence of the fluidised particles in the region of the surfaces of the glass sheet than in the bulk of the bed. This results in a high rate of transfer of heat away from the glass surfaces. It is thought that , ~0697Q(~
particles which become heated by passing in proximity to the glass surfaces then move rapidly away from the glass sheet and lose heat to the fluidising air in the bulk of the bed.
A preferred method according to the invention includes regulating the gas flow to maintain said quiescent state of the fluidised bed by creating a high pressure drop in the fluidis-ing gas flow across a membrane through which fluidising gas enters the bed.
Further according to the invention the particulate material may comprise particles of density in the range 0.3 g/cm3 to 3.97 g/cm3 and mean particle size in the range 5~m to l20~m, the material being selected so as to be fluidised in said uniform quiescent state by fluidising gas flowing uniformly in the bed at a velocity in the range 0.045 cm/s to 5.61 cm/s.
The density of the particles and their mean particle sizes are both important in determining the suitability of a particulate material for consitituting the fluidised bed in a quiescent uniformly expanded state employed in the method of the invention. Generally an appropriate particulate material for fluidisation in a quiescent uniformly expanded state by fluidising air, when the bed is operating in ambient conditions of normal room temperature and pressure, is one for which the numerical product of the particle density, in g/cm3, and the mean particle size inJlm, does not exceed about 220.
The degree of toughening of a glass sheet which is achieved by the method of the invention depends on the heat transfer coefficient between the fluidised particulate material and the hot glass sheet immersed in it. As already described there is thermal agitation on the hot glass surfaces which give rise to transfer of heat rapidly away from those surfaces. How-ever the properties of the particles themselves also affect the magnitude of the heat transfer coefficient.
For thermally toughening flat soda-lime-silica glass of thickness in the range 2.3 mm to 12 mm, the method of the in-vention may comprise heating the glass to a temperature in the range 610C to 680C, immersing the glass in a fluidised bed in said quiescent state which has a thermal capacity per unit volume at minimum fluidisation in the range 0.02 cal/cm3C to 0.37 cal/
cm3C, and maintaining the fluidised bed at a temperature up to 150C to induce in the glass an average central tensile stress in the range 22 MN/m2 to 115 MN/m2.
The maximum magnitude of average central tensile stress which can be achieved varies with the thickness of the glass and the heat transfer coefficient. By selection of a suitable mater-ial the heat transfer coefficient can be made high enough to prod-uce toughened glass sheets having a central tensile stress as high as 40 MN/m2 in glass 2 mm thick, a central tensile stress as high as 50 MN/m2 in glass 3.0 mm thick, and a central tensile stress as high as 104 MN/m2 in glass which is 12 mm thickness. However even higher central tensile stresses than these have been achieved as is shown in some of the Examples.
The particles may be a non-porous powdered a alumina of mean particle size in the range 23,~m to 54~um and particle density 3.97 g/cm3, the thermal capacity per unit volume of the bed at min-imum fluidisation being 0.32 cal/cm3C.
The invention also provides a fluidised bed for use as a quenching medium for thermally toughening a hot glass sheet, 10697Qo comprising particles of mean particle size in the range 5~um to 120~um and having a particle density in the range 0.3 g/cm3 to 3.97 g/cm3, and wherein the particles are so selected that the bed is in a quiescent uniformly expanded state of particulate fluidisation and has a thermal capacity per unit volume at minimum fluidisation in the range 0.02 cal/cm3C to 0.37 cal/cm3C.
The invention also comprehends a method of thermally treating glass in which the glass is contacted with a gas-fluidised particulate material of non-compacted particle structure which is such that the apparent density of the particles is less than the actual density of the material forming the particles and the buoy-ant particles constitute a gas-fluidised bed in a quiescent unif-ormly expanded state of particulate fluidisation, the material forming the particles and the temperature of the bed being so sel-ected that the heat transfer coefficient of the fluidised bed is sufficient to produce a desired thermal treatment of the glass as it cools in the bed.
The invention still further comprehends a method of the-rmally toughening glass, comprising heating the glass and immersing the hot glass in a gas-fluidised bed of particles of non-compacted particle structure which is such that the apparent density of the particles is less than the actual density of the material forming the particles and the buoyant particles constitute a gas-fluidised bed in a quiescent uniformly expanded state of particulate fluid-isation, the material forming the particles and the temperature of the bed being so selected that the heat transfer coefficient of the fluidised bed is sufficient to produce desired toughening stresses in the glass as it cools in the bed.
The use of particles of non-compacted structure permits the selection of a material for the particles to give a fluidised bed having a sufficiently high thermal capacity per unit volume at minimum fluidisation to produce a high amount of toughening stress in the glass whilst avoiding difficulties in fluidisation of such a material in a quiescent uniformly expanded state of particulate fluidisation.
The amount of toughening stress produced in the glass using a fluidised bed comprising particles of a particular non-compacted material can be controlled by selection of the particle density. Particles of low density and of a particular size res-ult in the production of a low amount of toughening stress in the glass, and the amount of toughening stress produced increases with increasing particle density up to the maximum density of particles of such size that they are still fluidised in said quiescent state.
Still further the invention provides a method for therm-ally toughening a glass sheet, comprising immersing a hot glass sheet in a fluidised bed in said quiescent state and constituted by particles of mean particle size in the range 5~m to 120,~m and apparent particle density in the range 0.3 g/cm3 to 2.35 g/cm3, the thermal capacity per unit volume of the bed at minimum fluid-isation being in the range 0.02 cal/cm3C to 0.37 cal/cm3C.
The apparent particle density within a range as set out above is the actual measured density of the particulate material taking into account the cavities within the particles, and is to be distinguished from the true density of the material itself.
By selecting the mean particle size in relation to the apparent particle density, the suitability of particles of non-compacted material for constituting the quiescent uniformly ex-panded fluidised bed can be assessed. Preferably the numerical value of the product of the apparent particle density, in g/cm3, and the mean particle size in ~um, should not exceed about 220.
Still further the invention provides a method of ther-mally toughening glass, comprising heating the glass, and immersing 10697(~0 the hot glass in a gas-fluidised bed of porous particles in a quiescent uniformly expanded state of particulate fluidisation, the material forming the particles and the temperature of the bed being so selected that the heat transfer coefficient of the fluidised bed is sufficient to induce desired toughening stresses in the glass as it cools in the bed.
The particles may be porous particles of ~ alumina of mean particle size 64~m and apparent particle density 2.2 g/cm , the thermal capacity per unit volume of the bed at minimum fluid-isation being 0.21 cal/cm3C.
In yet another embodiment the particles are of a porous form of aluminosilicate material of mean particle size in the range 60~m to 75~m and apparent particle density in the range 1.21 g/cm3 to 1.22 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being in the range 0.11 cal/cm3C
to 0.19 cal/cm3C.
Further the particles may be of porous powdered nickel of mean particle size 5~m and apparent particle density 2.35 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being 0.37 cal/cm3C.
Further according to the invention a method of thermally toughening glass comprises heating the glass, and immersing the hot glass in a gas-fluidised bed of hollow particles in a quies-cent uniformly expanded state of particulate fluidisation, the material forming the particles and the temperature of the bed being so selected that the heat transfer coefficient of the fluid-ised bed is sufficient to induce desired toughening stresses in the glass as it cools in the bed.
The particles may be hollow glass spheres of mean part-icle size in the range 77~m to 120~m and apparent particle density 0.38g/cm3, the thermal capacity per unit volume of the , ., ~
bed at minimum fluidisation being in the range 0.05 cal/cm3C to 0.06 cal/cm3C.
In a further embodiment the particles are hollow carbon spheres of mean particle size 48~m, and apparent particle density 0.3 g/cm3, the thermal capacit-y per unit volume of the bed at minimum fluidisation being 0.02 cal/cm3C.
The invention also comprehends a fluidised bed for use as a quenching medium for thermally toughening a hot glass sheet, comprising particles of non-compacted particle structure which is such that the apparent density of the particles is less than the actual density of the material forming the particles, wherein the mean particle size of the particles is in the range 5~m to 120~um the apparent particle density is in the range 0.03g/cm3 to 2.35 g/cm3, and wherein the particles are so selected that the bed is in a quiescent uniformly expanded state of particulate fluidisa-tion and has a thermal capacity per unit volume of the bed at minimum fluidisation in the range 0.02 cal/cm3C to 0.37 cal/cm3C.
The invention also includes thermally treated glass produced by the method of the invention; in particular a thermally toughened glass sheet produced by the method of the invention.
In order that the invention may be more clearly under-stood some embodiments thereof will now be described, by way of example, with reference to the accompanying drawings in which:-Figure 1 illustrates diagrammatically a verticalsection through apparatus for carrying out the method of the invention, /
~.069700 Figure 2 is a detail in section of part of Figure 1, and Figure 3 is a graph which illustrates a character-istic of a gas-fluidised bed in a quiescent uniformly expanded state of particulate fluidisation, which is employed in carrying out the invention.
Referring to Figure 1 of the drawings, a vertical toughening oven indicated generally at 1 has side walls 2 and a roof 3. The side walls 2 and the roof 3 are made of the usual refractory material and the bottom of the oven is open, being defined by an elongated aperture 4 in a baseplate 5 on which the oven 1 is supported. A movable shutter, not shown, is provided in known manner to close the aperture 4.
A sheet of glass 6 to be bent and subsequently thermally toughened is suspended in the oven 1 by tongs 7 which engage the upper margin of the sheet 6 and are held closed in customary manner by the weight of the glass sheet gripped between the tong points. The tongs 7 are suspended from a tong bar 8 which is suspended from a conventional hoist, not shown, and which runs on vertical guide rails 9 which extend downwardly from the oven to guide the lowering and raising of the tong bar 8.
A pair of bending dies 10 and 11 are located on either side of the path of the glass sheet 6 in a chamber 12, which is heated by hot gas flows through ducts 12a. me interior of the chamber 12 and the dies 10 and 11 are maintained at the same temperature as the temperature of the hot glass sheet 6 as it enters the chamber 12.
- .
The die 10 is a solid male die mounted on a ram 13 and has a curved front face which defines the curvature to be imposed on the hot glass sheet. The die 11 is a ring frame female die carried by struts 14 mounted on a backing plate 15 which is mounted on a ram 16. The curvature of the die frame 11 matches the curvature of the face of the male die 10.
The guide rails 9 extend downwardly through the chamher 12 to either side of the bending dies towards a container for a gas-fluidised bed 17 of particulate refractory material in which the hot bent glass sheet is to be quenched. The container for the fluidised bed comprises an open-topped rectangular tank 18 which is mounted on a scissors-lift platform 19. When the platform 19 is in its raised position the top edge of the tank 18 is just below the bending dies 10 and 11.
A micro-porous membrane 20, which is described in greater detail with reference to Figure 2, extends across the base of the tank 18. The edges of the membrane 20 are fixed between a flange 21 on the tank and a flange 22 on a plenum chamber 23 which forms the base of the tank. The flanges and the edges of the membrane 20 are bolted together as indicated at 24. A gas inlet duct 25 is connected to the plenum chamber and fluidising air is supplied to the duct 25 at a regulated pressure. The membrane is so constructed that fluidising air flows uniformly into the fluidised bed over the whole base of the bed to maintain the bed in a quiescent uniformly expanded state of particulate fluidisation.
Particulate refractory material in the tank 18 is maintained in the quiescent uniformly expanded state of 1069~7QO
particulate fluidisation by the upward flow of air uniformly distributed by the porous membrane 20. The expanded bed is in a substantially bubble-free quiescent state and there are no regions of the bed which are not fluidised.
A preferred construction of micro-porous membrane is shown in Figure 2 and is described in Canadian Application Serial No. 279,877. This membrane comprises a steel plate 26 which has a regular distribution of holes 27. The margins of the plate are drilled to provide passages for bolts 24. A
lQ gasket 28 is located between the lower face of the margins of the plate and the flange 22 on the plenum chamber.
A number of layers 29 of strong micro-porous paper are laid on the plate 26. For example fifteen sheets of paper may be used. The membrane is completed with a woven wire mesh 30, for example stainless steel mesh which is laid on top of the paper. An upper gasket 31 is located between the margins of the wire mesh 30 and the flange 21 on the tank.
A basket for catching cullet may be located near the membrane 20, and is designed so as not to interfere with the uniform flow of fluidising air upwardly from the membrane.
Referring again to Figure 1, the guide rails 9 extend downwardly to a position below the bending dies and terminate in the region of the upper edge of the tank 18. A fixed frame indicated at 32 is mounted in the tank 18 and has upturned feet 33 at its base to receive the lower edge of a glass sheet lowered into the fluidised bed when the tong bar 8 is lowered beyond the bending dies by the hoist.
With the scissors-lift table 19 lowered and the tongs 7 and tong bar 8 in their lowermost position at the bottom of `` 1069700 the guides 9, a cool glass sheet to be bent and toughened is loaded onto the tongs. The hoist then raises the suspended glass sheet into the oven 1 which is maintained at a temper-ature, for example 850C, when toughening soda-lime-silica glass. The glass sheet is rapidly heated to a temperature near~ts softening point for example a temperature in the range 610C to 680C.
When the glass sheet has reached a required temperat-ure uniformly, the shutter closing the aperture 4 is opened and the hot glass sheet is lowered by the hoist into position between the open bending dies 10 and 11. The rams 13 and 16 are operated and the dies close t~ bend the sheet. When the required curvature has been imparted to the sheet the dies open and the hot bent glass sheet is rapidly lowered into the fluidised bed in the tank 18 which has been raised to quenching position by operation of the scissors-lift table 19 while the glass sheet was being heated in the oven 1.
When high quality laminated glass products are to be produced incorporating thermally toughened glass sheets produced by quenching in a fluidised bed an improvement in optical quality has been observed when the surfaces of the glass sheet are subjected to a preliminary air cooling just before the glass is immersed in the fluidised bed. This may be achieved by locating just above the upper edge of the tank 18 shallow blowing frames which direct cooling air onto the surfaces of the bent glass sheet as it leaves the bending dies and enters the fluidised bed.
The preliminary surface cooling is effective to "set-up"
' ' ' ' ' ' ' U`.~! ' '-' 1069700 the surfaces of the glass sheet and thereby avoid minute variations in those surfaces such as have sometimes been observed and which may be due to the thermal agitation of the fluidised particulate material on the glass surfaces.
Such preliminary surface cooling would however only usually be employed when the glass is being used for the production of laminates of high optical quality.
The fluidlsed bed is maintained at a suitable temperat-ure for inducing a required central tensile stress in the glass, -for example 30C to 150C, by the water cooling jackets 34 on the flat longer walls of the tank 18, and by controlling the temperature of the fluidising air supplied to the plenum ;
chamber 23. The jackets 34 act as a heat sink which absorbs heat transferred through the bed from the hot glass sheet.
The lower edge of the hot glass sheet is uniformly ch~lled along its whole length as it enters the horizontal quiescent surface of the expanded fluidised bed so that there is no possibility of diffërent tensile stresses being generated in different areas of the surface of that edge of ~ -- 20 the glass, such as could lead to fracture. During its descent ~-. ~' ' ,' ~
into the bed the lower edge always contacts fluidised material in a quiescent uniformly expanded state of particulate fluid-isation, and this uniform treatment of the lower edge, regard-less of upward flow of particulate material which may be generatedcn the hot glass surfaces immediately after they enter the fluidised bed, largely obviates fracture and the problems of dealing with glass fragments in the bed. This together with the avoidance of losses of glass sheets due to change of shape of the glass sheets and/or damage to the surface quality, ensures a commercially viable yield of toughened glasses.
Localised thermal agitation of the fluidised bed takes place on the hot glass surfaces, perhaps by rapid gas expansion in a manner akin to the boiling of a liquid. The agitation ensures that there is adequate heat transfer away from the glass surfaces into the bulk of the fluidised bed, for example heat transfer coefficients between the bed and the glass sheet in the range 0.003 cal/cm2C sec to 0.02 cal/cm2C sec are obtained. The heat transfer continues until well after the glass has cooled below its strain point, with sufficient severity to ensure that the centre-to-surface temperature gradients are maintained as the glass cools through its strain point, and the toughening stresses are developed thereafter during the continuous cooling of the glass while it is still immersed in the bed.
The agitation of the fluidised material at the glass surfaces sets up currents in the bulk of the bed which ensure continual dissipation to the remoter parts of the bed of the -heat which is extracted from the glass by the thermal agitation of the bed in the region immediately surrounding the glass sheet.
The water cooling jackets 34, acting as a heat sink, keep those remoter parts of the bed cool.
The sheet engages the feet 33 of the frame 32 at the bottom of its descent, thereby releasing ~he tongs 8. The glass sheet then rests on the frame 32 while the glass sheet cools in the fluidised ked. The glass sheet remains in the fluidised bed until it is cooled sufficiently to be handled and the tank 18 is lowered by lowering the scissors-lift platform to expose the fixed frame 32 and the supported toughened glass sheet which is then removed for subsequent cooling to room temperature. .
The nature of the quiescent uniformly expanded state of particulate fluidisation of the fluidised bed is illustrated in Figure 3 which is a plot of plçnum pressure, that is, the pressure in the plenum chamber, against the height of the bed in the tank 18 using ~ alumina particles as described in Example 1 -
2, set out below, and with the tank size and fluidisation conditions of Example 2, and the temperature of the bed at 80C.
When the plenum pressure reached 15 kN/m2 eY~pansion of ~`
the bed began, the velocity of the fluidising air-through the bed then being sufficient to produce incipient fluidisation. - ;
That is, at this lower limit of gas velocity the ~ alumina particles just become suspended in,the upwardly flowing,air_ - Because of the use of a high pressure drop and a uniformly micro-porous membrane of the kind illustrated in Figure 2, in which the pressure drop across the membrane is in excess of 60% of the plenum pressure, there is u~iform ~: . . .... . . . . .
10697~0 distribution of fluidising air flowing upwardly from the upper face of the membrane. This high pressure drop across the membrane makes possible sensitive regulation of the velocity of gas flow upwardly through the particulate material, thereby permitting regulation of the state of quiescent fluidisation of the ~ alumina bet~een the minimum fluidisation state just described and a state of maximum expansion of the bed in which dense-phase fluidisation is maintained.
This sensitive regulation of the gas velocity is achieved by regulation of the plenum pressure in the chamber 23, and as the plenum pressure increases there is no sudden or discontinuous change in the state of the bed. Rather the - -q~iesce~t uniformly expanded state of the bed persists, as illustrated in Figure 3, as the plenum pressure is increased to about 25 kN/m2 and the bed expands to a height of about 102 cm in the tank.
At this plenum pressure the first clearly recognisable bubble, for example about 5 mm in diameter, may be observed breaking the surface of the quiescent bed, and this velooity of the fluidising air may be considered as the minimum bubbling velocity.
Because of the use of the high-pressure drop membrane -- -20, it has been possible to observe that this minimum bubbling velocity is not necessarily the gas velocity producing maximum - expansion of the bed, and further regulation of the plenum pressure up to 27 kN/m2 produced a maximum bed height of 105 cm.
While this increase in plenum pressure up to 27 kN/m2 was effected more small bubbles were observed to break the bed surface, but the small random bubbles ~Jere not so significant -as to adversely affect the capacity of the bed for quenching hot sheets of glass, in particular thicker sheets of glass.
With increase of the plenum pressure beyond 27 kN/m2, persistent bubbling of the bed occured and a tendency of the bed to collapse to a height below its ma~imum height of 105 cm, was observed. In this state the bed was unsuitable for tough- ;
ening hot glass sheets.
In this e~amp]e therefore the uniform quiescent expanded ~ state of the fluidised bed of ~ alumina, which was effective for toughening hot glass sheets is represented by the region of the curve of Figure 3 lying between plenum pressures of 15 kN/m and 27 kN/m2, in which region sensitive control of the state of fluidisation was possible, with consequential control of the uniform toughening stresses induced in the glass.
The effective heat transfer coefficient of the fluidised bed relative to the hot glass is determined by the properties of the fluidising~gas, usually air, the gas velocity in the bed, the properties of the particulate refractory material notably the range of sizes of the particles, the mean particle size, the density of the particles and, in the case when the particles ~ contain cavities, that is have a certain porosity or hollow - structure, the density of the material of the particles. The --heat transfer coefficient also depends on the temperatures of the glass and the bed, since if there is only a small difference between these temperatures, there will be little agitation on the surface of the glass and the effective heat transfer coefficient wi~l be comparatively low.
Other factors affecting the heat transfer coefficient are the specific heat of the particles, and their average heat capacity. In each of the following examples the numerical value of the product of the particle density, in g/cm3, and the mean particle size in,~m, is less than 220. This is a criterion which may be used for assessing the suitability of a particulate material, that is its capability of being fluidised by air in a quiescent uniformly expanded state of particulate fluidisation, operating with ambient conditions of normal temperature and pressure.
Some examples of toughening of glass ~heets of thick-ness in the range 2.3 mm to 12 mm, using apparatus as in Figures 1 and 2, and a uniform quiescent expanded bed are set out below.
In each of the following Examples 1 to 11 the edges of the glass sheet are finished by being rounded using a fine diamond grit wheel.
Example ~ The particulate refractory is a ~ form of porous alurnina the properties of which are as follows:- -Mean particle size (d) = 64~1m Particle size range = 20 to 160~m Particle density (~) = 2.2 g/cm3 Material density = 3.97 g/cm3 px d = 14i Material specific heat = 0.2 cal/gC
Thermal capacity per unit volume of bed at minimum fluidisation = ~.21 cal/cm3c Velocity of fluidising air in bed = 0.54 cm/s With the bed maintained at 40C the degree of toughening of glass sheets of thickness in the range 2.3 mm to 12 mm with an initial glass temperature in the range 610C to 670C was as follows:-Initial GlassGlass Thickness Average Central Temperature (mm) Tensile Stress C ~ , _(MN/m2 ) 610 2.3 37 610 12 93.5 630 2.3 42.5 630 6 ',72.5 650 2.3 46 650 6 75.7 650 8 92.7 670 2.3 44 ~
670 6 75 ' 670 10 100 _ The effective heat transfer coefficient between the bed and the glass sheets lay in the range 0.01 cal/cm2C sec to 0.012 cal/cm2C sec.
Example 2 In a particular production run using the same ~ form of porous alumina as in Example 1, bent sheets of glass 2.3 mm thick were toughened. These sheets were subsequently used as a component of a laminated windscreen ~r automobiles.
The properties of the ~ alumina are as follows:- I
Mean particle size (d) = 64~m Particle size range = 30 t-o 150,lm Particle density (~) = 2.2 g/cm3 Material density = 3.9 g/cm ~ d = 141 Size of tank holding 38 cm x 215 cm x fluidised bed = 105 cm deep Plenum pressure = 24 kNtm2 Pressure drop across membrane = 15 kN/m2 Pressure drop across membrane = 60% of plenurn pressure Xate of flow of fluidising air = 0.175 m3/min Velocity of fluidising air in bed = 0.36 cm/s Temperature of fluidised bed = 60C
Temperature of glass: top edge = 650C to 655C
bottom edge = 670C to 675C
Resulting uniform central tensile stress in glass = 38MN/m2 to 40MN/m2 The effecti~e heat transfer coefficient between the bed and the glass sheets lay in the range 0.01 cal/cm2C sec to 0.012 cal/cm2C sec.
Example 3 In another production run, sheets of glass intended as components of laminated aircraft windscreens and of thickness
When the plenum pressure reached 15 kN/m2 eY~pansion of ~`
the bed began, the velocity of the fluidising air-through the bed then being sufficient to produce incipient fluidisation. - ;
That is, at this lower limit of gas velocity the ~ alumina particles just become suspended in,the upwardly flowing,air_ - Because of the use of a high pressure drop and a uniformly micro-porous membrane of the kind illustrated in Figure 2, in which the pressure drop across the membrane is in excess of 60% of the plenum pressure, there is u~iform ~: . . .... . . . . .
10697~0 distribution of fluidising air flowing upwardly from the upper face of the membrane. This high pressure drop across the membrane makes possible sensitive regulation of the velocity of gas flow upwardly through the particulate material, thereby permitting regulation of the state of quiescent fluidisation of the ~ alumina bet~een the minimum fluidisation state just described and a state of maximum expansion of the bed in which dense-phase fluidisation is maintained.
This sensitive regulation of the gas velocity is achieved by regulation of the plenum pressure in the chamber 23, and as the plenum pressure increases there is no sudden or discontinuous change in the state of the bed. Rather the - -q~iesce~t uniformly expanded state of the bed persists, as illustrated in Figure 3, as the plenum pressure is increased to about 25 kN/m2 and the bed expands to a height of about 102 cm in the tank.
At this plenum pressure the first clearly recognisable bubble, for example about 5 mm in diameter, may be observed breaking the surface of the quiescent bed, and this velooity of the fluidising air may be considered as the minimum bubbling velocity.
Because of the use of the high-pressure drop membrane -- -20, it has been possible to observe that this minimum bubbling velocity is not necessarily the gas velocity producing maximum - expansion of the bed, and further regulation of the plenum pressure up to 27 kN/m2 produced a maximum bed height of 105 cm.
While this increase in plenum pressure up to 27 kN/m2 was effected more small bubbles were observed to break the bed surface, but the small random bubbles ~Jere not so significant -as to adversely affect the capacity of the bed for quenching hot sheets of glass, in particular thicker sheets of glass.
With increase of the plenum pressure beyond 27 kN/m2, persistent bubbling of the bed occured and a tendency of the bed to collapse to a height below its ma~imum height of 105 cm, was observed. In this state the bed was unsuitable for tough- ;
ening hot glass sheets.
In this e~amp]e therefore the uniform quiescent expanded ~ state of the fluidised bed of ~ alumina, which was effective for toughening hot glass sheets is represented by the region of the curve of Figure 3 lying between plenum pressures of 15 kN/m and 27 kN/m2, in which region sensitive control of the state of fluidisation was possible, with consequential control of the uniform toughening stresses induced in the glass.
The effective heat transfer coefficient of the fluidised bed relative to the hot glass is determined by the properties of the fluidising~gas, usually air, the gas velocity in the bed, the properties of the particulate refractory material notably the range of sizes of the particles, the mean particle size, the density of the particles and, in the case when the particles ~ contain cavities, that is have a certain porosity or hollow - structure, the density of the material of the particles. The --heat transfer coefficient also depends on the temperatures of the glass and the bed, since if there is only a small difference between these temperatures, there will be little agitation on the surface of the glass and the effective heat transfer coefficient wi~l be comparatively low.
Other factors affecting the heat transfer coefficient are the specific heat of the particles, and their average heat capacity. In each of the following examples the numerical value of the product of the particle density, in g/cm3, and the mean particle size in,~m, is less than 220. This is a criterion which may be used for assessing the suitability of a particulate material, that is its capability of being fluidised by air in a quiescent uniformly expanded state of particulate fluidisation, operating with ambient conditions of normal temperature and pressure.
Some examples of toughening of glass ~heets of thick-ness in the range 2.3 mm to 12 mm, using apparatus as in Figures 1 and 2, and a uniform quiescent expanded bed are set out below.
In each of the following Examples 1 to 11 the edges of the glass sheet are finished by being rounded using a fine diamond grit wheel.
Example ~ The particulate refractory is a ~ form of porous alurnina the properties of which are as follows:- -Mean particle size (d) = 64~1m Particle size range = 20 to 160~m Particle density (~) = 2.2 g/cm3 Material density = 3.97 g/cm3 px d = 14i Material specific heat = 0.2 cal/gC
Thermal capacity per unit volume of bed at minimum fluidisation = ~.21 cal/cm3c Velocity of fluidising air in bed = 0.54 cm/s With the bed maintained at 40C the degree of toughening of glass sheets of thickness in the range 2.3 mm to 12 mm with an initial glass temperature in the range 610C to 670C was as follows:-Initial GlassGlass Thickness Average Central Temperature (mm) Tensile Stress C ~ , _(MN/m2 ) 610 2.3 37 610 12 93.5 630 2.3 42.5 630 6 ',72.5 650 2.3 46 650 6 75.7 650 8 92.7 670 2.3 44 ~
670 6 75 ' 670 10 100 _ The effective heat transfer coefficient between the bed and the glass sheets lay in the range 0.01 cal/cm2C sec to 0.012 cal/cm2C sec.
Example 2 In a particular production run using the same ~ form of porous alumina as in Example 1, bent sheets of glass 2.3 mm thick were toughened. These sheets were subsequently used as a component of a laminated windscreen ~r automobiles.
The properties of the ~ alumina are as follows:- I
Mean particle size (d) = 64~m Particle size range = 30 t-o 150,lm Particle density (~) = 2.2 g/cm3 Material density = 3.9 g/cm ~ d = 141 Size of tank holding 38 cm x 215 cm x fluidised bed = 105 cm deep Plenum pressure = 24 kNtm2 Pressure drop across membrane = 15 kN/m2 Pressure drop across membrane = 60% of plenurn pressure Xate of flow of fluidising air = 0.175 m3/min Velocity of fluidising air in bed = 0.36 cm/s Temperature of fluidised bed = 60C
Temperature of glass: top edge = 650C to 655C
bottom edge = 670C to 675C
Resulting uniform central tensile stress in glass = 38MN/m2 to 40MN/m2 The effecti~e heat transfer coefficient between the bed and the glass sheets lay in the range 0.01 cal/cm2C sec to 0.012 cal/cm2C sec.
Example 3 In another production run, sheets of glass intended as components of laminated aircraft windscreens and of thickness
3 mm, 4 mm~ 6 mrn, 8mm, and 10 mm, were toughened in a uniform quiescent expanded fluidised bed of ~ alumina. The same ~ form of porous alumina was used as in Exarnples 1 and 2.
- ~4 Size of tank holding fluidised bed = 45cm x 245cm x 150cm deep Plenum pressure = 30 kN/m2 Pressure drop across 2 membrane = 19.5 kN/m Pressure drop across membrane = 65% of plenum pressure Rate of flow of fluidising air = 0.34 m3/min Velocity of fluidising air in bed = 0.51 cm/s Temperature of fluidised O
bed = 60 C
Temperature of glass = 645C to 650C
Resulting uniform centraltensile stress induced in the glass was as follows:-Thickness Central Tensile Stress ~ .
3.0 mm 48 MN/m
- ~4 Size of tank holding fluidised bed = 45cm x 245cm x 150cm deep Plenum pressure = 30 kN/m2 Pressure drop across 2 membrane = 19.5 kN/m Pressure drop across membrane = 65% of plenum pressure Rate of flow of fluidising air = 0.34 m3/min Velocity of fluidising air in bed = 0.51 cm/s Temperature of fluidised O
bed = 60 C
Temperature of glass = 645C to 650C
Resulting uniform centraltensile stress induced in the glass was as follows:-Thickness Central Tensile Stress ~ .
3.0 mm 48 MN/m
4.0 mm 53 MN/m 10.0 mm 80 MN/m2 The effective heat transfer coefficient between thebed and the glass sheets lay in thé range 0.01 cal/cm2C sec to 0.012 cal/cm2C ~ec.
Example 4 The particulate refractory material is a porous powdered aluminosilicate material, each particle containing 13% by -weight alumina and 86% silica. The powdered material has the following properties:-Particle size range = up to 150~m Mean particle size (d) = 60,um Particle density (p) = 1.22 g/cm3 - 10697~)0 Material densi~y = 2.3 g/cm3 fx~ = 73 Material specific heat = 0.38 cal/gC
Thermal capacity per unit volume of bed at minimum 3 fluidisation = 0.19 cal/cm C
Velocity of fluidising air in bed = 0.21 cm/s With the bed maintained a-t 40C, the degree of toughening of glass sheets of thickness in the range 2.3 mm to 10 mm was as follows:-Initial Glass Glass ThicknessAverage Central Temperature (mm) Tensile Stress C) (MN/m2) 650 2.3 30.8 650 - 6 62.3 The effec-tive heat transfer coe~ficient between the bed and the glass sheets lay in the range 0.007cal/cm2C sec to 0.009 cal/cm2C sec.
ExamPle 5 Another form of a porous powdered composite alumino-silicate material was used. Each particle is porous and - contains 29% by weight alumina and 69% silica. This porous powder has the following properties:- -Particle size range = up to 150~m Mean Particle size (~) = 75,4m - ~6 10697û0 Particle density (f ) = 1.21 g/cm3 fxd = 91 Material density = 2.3 g/cm3 Material specific heat = 0.2 cal/gC
Thermal capacity per unit volume of bed at minimum fluidisation = 0.11 cal/cm3C
Velocity of fluidising air in bed = 0.33 cm/s With the bed maintained at 40C, and the initial glass temperature in the range 610C to 670C, the degree of toughen-ing of glass sheets of thickness in the range 2.3 mm to 10 mm was as follows:-Initial GlassGlass ThicknessAverage Central l'emperature(mm) Tensile Stress ( C ) (MN~m2 ) 610 10 '74 630 2.3 31.5 650 2.3 33.7 650 4 4~.3 650 8 71.3 670 2.3 32 670 10 81.5 _ ~ . . ~
~06g7~0 The effective heat transfer coeffi,cient between the bed and the glass sheets lay in the range 0.007 cal/cm2C sec to 0.01 cal/cm2C sec.
Example 6 A "Fillite" powder, which comprises the hollow glass spheres derived from pulverised fuel ash from power station boilers, was selected to have the following properties:-Particulate size range = 20 to 160~ m Mean Particle size (~) = 77 ~ m Particle density (~) = 0.38 g/cm3 ~xd = 29 Material density = 2.6 g/cm3 Material specific heat = 0.18 cal/gC
Thermal capacity per unit volume of bed at minimum fluidisation = 0.05 cal/cm3C
the fluidisation velocity of the air in the Fillite = 0.11 cm/s The degree of toughening induced in the glass sheets which were thermally toughened in this fluidised bed can be represented by an average central tensile stress which was measured in conventional manner and the results achieved for a range of glass thickness from 4 mm to 12 mm, with different initial glass temperatures in the range 610C to 670C and with the temperature of the fluidised bed at 40C are as follows:-._. ", _ __ -- ___ Ini-tial Glass Glass Thickness Average Cen~ral Temperature (rnm) Tensile Stress C ) . (MN/m2 ) 650 4 22.4 650 12 48.5 670 10 5o The effective heat transfer coefficient between the bed and the glass sheets lay in the range 0.003 cal/cm2C sec to 0.004 cal/cm2C sec.
Example 7 -Another grade of "Fillite" material was used having the following properties:-Mean particle size (~) = 120~ m Particle density (j) = 0.38 g/cm3 Material density = 2.6 g/cm3 ~ = 45 Material specific heat = 0.18 cal/gC
Thermal capacity per unit 30 volume of bed at = 0.06 cal/cm C
minimum fluidisation Velocity of fluidising air in bed = 0.27 cm/s ~0697~0 With initial glass tempera-tures in the range 630C to 670C and with the bed at about 40C, stresses induced in glass sheets of thickness 6 mm to 10 mm were as follows:-Initial GlassGlass Thickness Average Central Temperature (mm) Tensile Stress ( C ) (MN/m2 ) 650 6 45.5 670 8 . 53 Th.e effective heat transfer coefficient between the bed and the glass-sheets lay in the range 0.005 to 0.006 cal/cm3C sec.
ExamQle 8 The par-ticulate refractory material used was hollow carbon spheres of the ki.nd known as "Carbospheres" having the following properties:-Particle size range - 5 to 150~m Mean particle size (~) = 48~lm Particle density (p) = 0.3 g/cm-' ~x ~ = 14.4 .
Ma-terial density = 2.3 g/cm3 Material specific heat = 0.123 cal/gC
Thermal capacity per unit volume of bed at minimum fluidisation = 0.02 cal/cm3C
Velocity of fluidising air in bed = 0.33 cm/s ~ 30 The degree of toughening of glass sheets quenched in this fiuidised bed maintained at about 40C are as follows:-Initial Glass Glass Thickness Average Central Temperature (mm) Tensile Stress C ) . _ (MN/m2 ) 650 4 26.3 650 6 32.7 The effective heat transfer coefficient between the bed and the gl~-ss sheets~lay in the range 0.0035 cal/cm2C sec to 0.004 cal/cm2Csec.
Exam~le 9 The particulate refractory material was porous powdered nickel having the following properties:-Mean particle size (~) = 5~um -Particle density (~) = 2.35 g/cm3 Material density = 8.9 g/cm3 ~X~ = 12 Material specific heat = 0.106 cal/gC
Thermal capacity per unit vol~me of bed minimum fluidisation state = 0~37 cal/cm3C
Velocity of fluidising air in bed -- 0~045 cm/s - 7~1 _ ~ lass sheets of thickness in the range 2.3 mm to 6 ~m at an initial temperature of 650C were quenched in a fluidised bed of this po~us nickel powder which ~as in a quiescent state and was maintained at about 40C. The degree of toughening represented by average central tensile stress was as follows:-Glass Thickness Average Central Tensile (mm) Stress (M~/m2) 2.3 77 _ _ _ 115 _. .
The effective heat transfer coefficient between the bed and -the glass sheets was 0.02 cal/cm2C sec.
Exan~e _ 10 .
The parliculate material was a non-porous powdered a alumina. A number of a alumina materials of different mean particle size were used. All these materials had the following common properties:-Particle density (p) = 3.97 g/cm3 Material density = 3.97 g/cm3 Material specific heat = 0.2 cal/gC
The a alumina material was available in different graded particle sizes of the material and four different fluidised beds were constituted as follows:-~0697ao Alumina Mean Part- Thermal Cap- Thermal Cap- Fluidis-Bed icle Size pxd acity of acity of mini- ing gas (d)(~m) Particle mum fluidised ~elocity (cal/C)(cal/cm3&) (cm/s~
_ A 23 92 5 X 10 9 0.32 1.02 B 29 116 10 X 10 9 0.32 1.62 C 45 180 38 X 10-9 0.32 3.90 ¦ D 54 216 66 X 10 0.32 5.61 Glass sheets of thickness in the range 2.3 mm to 12 mm were quenched in these fluidised beds which are each at a temperature of 40C. The initial temperature of the glass sheets was in the range 610C to 670C and the degree of toughening of the sheets is represented by an average central tensile stress in the range 42 MN/m to 104 MN/m .
The effective heat transfer coefficient between the bed and the glass sheets was in the range 0.0062 cal/cm2C sec to 0;0086 cal/cm C sec.
Example 11 A bed of small solid glass spheres was fluidised.
Properties of the bed were as follows:-Particle size range = 0 to 75 ~m Mean particle size (~) = 58~ m Particle density (~1 = 2.5 g/cm3 pxd = 145 Thermal capacity per unit volume of bed at minimum fluidisation = 0.34 cal/c3C
Ve]ocity of fluidising 30 air in bed = 0.41 cm/s .
106970~
Sheets of glass of thickness~ in the range 2.3 mm to 10 mm were heated to an initial temperature in the range 630C to 670C and were quenched in the fluidised bed which was maintained at a temperature of about 40C.
The degree of toughening of the glass sheets was as follows:-Initial GlassGlass Thickness Average Central Temperature(mm) Tensile S2tress (C) (~N/m ) 630 2.3 38 650 2.3 40 650 6 74.5 670 2.3 43 The average effective heat transfer coefficient between the bed and the glass sheets was 0.011 cal/cm2C sec.
To illustrate the high yield of unbroken and undistorted glass sheets obtained when using a gas-fluidised bed according to the invention in a quiescent uniformly expanded state of particulate fluidisation, as compared with the yield when using a bed in a bubbling state of fluidisation, a number of similar sheets of glass of size 30 cm x 30 cm and of thickness 2 mm, 6 mm and 12 mm were treated. The glass sheets had an edge finish in which the edges of the glass sheets were cham-fered using a bonded silicon carbide grinding wheel. This gave a rougher edge finish than that of the glass sheets of Examples 1 to 11 which were finished with a diamond grit wheel. The invention made a high yïeld possible even with this rougher, and cheaper, edge finish.
Each sheet was heated to a temperature as set out below and then immersed in a fluidised bed of the ~ form of porous alumina described in Example 1.
For the purpose of these yield tests some hot glass sheets were immersed in a fluidised bed in a quiescent state as described in Example 1. A bubbling state of fluidisation of the bed was then produced by increasing the fluidising gas velocity above the value producing maximum expansion of the bed, and an equal number of hot glass sheets were immersed in the bubbling bed.
The yield of dimensionally acceptable unbroken glass -sheets, as a percentage of the total number of sheets treated, was as follows:-Glass thickness = 2 mm 20Glass Temperature Yield C QUIESCENT BEDBUBBLING BED
645 95% 52~
660 100% 80%
Glass thickness = 6 mm .. .
Glass Temperature Yield C QUIESCENT BEDBUBBLING BED
640 - - -- 80% 40 645 100~ 60 --` 1069700 Glass thickness - 12 mm Glass Temperature Yield C QUIESCENT BED BUBBLING BED
635 80% 40%
645 100% 75%
Although the above examples were obtained using 30 cm x 30 cm square sheets of glass even lower yields with respect to fracture and distortion result when treating large sheets of glass such as of motor vehicle windscreen size in a bubbling fluidised bed. In contrast the yields obtained when treating such larger sheets of glass in a quiescent fluidised bed are at least as good as those of the examples referred to above.
The value of the stresses induced in the glass decreases as the bed temperature increases and in the limit, which may be about 300C or higher, the stresses in the glass are such that the glass is annealed rather than toughened. Heating and/or cooling elements may be provided on the side walls of the tank 18 for controlling the temperature of the fluidised bed. In all theE~amples the sheets of glass were commercial soda-lime-silica glass such as is used in the manufacture of aircraft windscreen panels, automobile windscreens, ship's windows and architectural panels. Glass of other compositions can be toughened or annealed in the same way using the method of the invention. Also articles other than glass sheets, for example pressed glass articles such as insulators or lens blanks, or blown glass articles can be toughened or annealed by the method of the invention.
A fluidised bed according to the invention may be used for other thermal treatments of glass, for example for the heating of a relatively cold glass article prior to a further ao processing step, heat transfer from the fluidised material to the glass which is immersed in the bed being facilitated without damage to the glass, even when the glass has attained a temperature at which it is susceptible to damage by irregular forces.
The invention may also be used for thermally toughening glass sheets which have been heated and bent while supported in a near-vertical position, and advanced along a horizontal path, as described in United Kingdom Patent Application No.
34703/73 (Specification No. 1,442,316). In the apparatus described in that application the bending dies are enclosed in a heated chamber which is tilted from an inclined position to a position in which the bent glass sheet between the bending dies is vertical and can be lowered vertically into a quiescent fluidised bed of the kind described above.
In another process employing the invention a glass sheet may be heated by immersing the sheet in a fluidised bed which is at a sufficiently high temperature to heat the glass to pre-bending temperature. After removal from the hot bed the sheet is bent, and the bent sheet is then toughened by immersing the glass in a fluidised bed which is in a quiescent uniformly expanded state of particulate fluidisation as - described above. The glass sheet could be carried by the same set of tongs throughout the heating bending and toughening, the tongs being adjustably mounted so that they move to follow the bent shape of the glass. In another arrangement each glass sheet is suspended from non-adjustable tongs for heating and is trans-ferred to lower-edge support during bending in the manner des-cribed in United Kingdom Specification No. 1,442,316, the bent glass sheet being engaged by a second set of tongs which are arranged according to the bent shape of the glass, and lowered into the quiescent fluidised bed for quenching.
Example 4 The particulate refractory material is a porous powdered aluminosilicate material, each particle containing 13% by -weight alumina and 86% silica. The powdered material has the following properties:-Particle size range = up to 150~m Mean particle size (d) = 60,um Particle density (p) = 1.22 g/cm3 - 10697~)0 Material densi~y = 2.3 g/cm3 fx~ = 73 Material specific heat = 0.38 cal/gC
Thermal capacity per unit volume of bed at minimum 3 fluidisation = 0.19 cal/cm C
Velocity of fluidising air in bed = 0.21 cm/s With the bed maintained a-t 40C, the degree of toughening of glass sheets of thickness in the range 2.3 mm to 10 mm was as follows:-Initial Glass Glass ThicknessAverage Central Temperature (mm) Tensile Stress C) (MN/m2) 650 2.3 30.8 650 - 6 62.3 The effec-tive heat transfer coe~ficient between the bed and the glass sheets lay in the range 0.007cal/cm2C sec to 0.009 cal/cm2C sec.
ExamPle 5 Another form of a porous powdered composite alumino-silicate material was used. Each particle is porous and - contains 29% by weight alumina and 69% silica. This porous powder has the following properties:- -Particle size range = up to 150~m Mean Particle size (~) = 75,4m - ~6 10697û0 Particle density (f ) = 1.21 g/cm3 fxd = 91 Material density = 2.3 g/cm3 Material specific heat = 0.2 cal/gC
Thermal capacity per unit volume of bed at minimum fluidisation = 0.11 cal/cm3C
Velocity of fluidising air in bed = 0.33 cm/s With the bed maintained at 40C, and the initial glass temperature in the range 610C to 670C, the degree of toughen-ing of glass sheets of thickness in the range 2.3 mm to 10 mm was as follows:-Initial GlassGlass ThicknessAverage Central l'emperature(mm) Tensile Stress ( C ) (MN~m2 ) 610 10 '74 630 2.3 31.5 650 2.3 33.7 650 4 4~.3 650 8 71.3 670 2.3 32 670 10 81.5 _ ~ . . ~
~06g7~0 The effective heat transfer coeffi,cient between the bed and the glass sheets lay in the range 0.007 cal/cm2C sec to 0.01 cal/cm2C sec.
Example 6 A "Fillite" powder, which comprises the hollow glass spheres derived from pulverised fuel ash from power station boilers, was selected to have the following properties:-Particulate size range = 20 to 160~ m Mean Particle size (~) = 77 ~ m Particle density (~) = 0.38 g/cm3 ~xd = 29 Material density = 2.6 g/cm3 Material specific heat = 0.18 cal/gC
Thermal capacity per unit volume of bed at minimum fluidisation = 0.05 cal/cm3C
the fluidisation velocity of the air in the Fillite = 0.11 cm/s The degree of toughening induced in the glass sheets which were thermally toughened in this fluidised bed can be represented by an average central tensile stress which was measured in conventional manner and the results achieved for a range of glass thickness from 4 mm to 12 mm, with different initial glass temperatures in the range 610C to 670C and with the temperature of the fluidised bed at 40C are as follows:-._. ", _ __ -- ___ Ini-tial Glass Glass Thickness Average Cen~ral Temperature (rnm) Tensile Stress C ) . (MN/m2 ) 650 4 22.4 650 12 48.5 670 10 5o The effective heat transfer coefficient between the bed and the glass sheets lay in the range 0.003 cal/cm2C sec to 0.004 cal/cm2C sec.
Example 7 -Another grade of "Fillite" material was used having the following properties:-Mean particle size (~) = 120~ m Particle density (j) = 0.38 g/cm3 Material density = 2.6 g/cm3 ~ = 45 Material specific heat = 0.18 cal/gC
Thermal capacity per unit 30 volume of bed at = 0.06 cal/cm C
minimum fluidisation Velocity of fluidising air in bed = 0.27 cm/s ~0697~0 With initial glass tempera-tures in the range 630C to 670C and with the bed at about 40C, stresses induced in glass sheets of thickness 6 mm to 10 mm were as follows:-Initial GlassGlass Thickness Average Central Temperature (mm) Tensile Stress ( C ) (MN/m2 ) 650 6 45.5 670 8 . 53 Th.e effective heat transfer coefficient between the bed and the glass-sheets lay in the range 0.005 to 0.006 cal/cm3C sec.
ExamQle 8 The par-ticulate refractory material used was hollow carbon spheres of the ki.nd known as "Carbospheres" having the following properties:-Particle size range - 5 to 150~m Mean particle size (~) = 48~lm Particle density (p) = 0.3 g/cm-' ~x ~ = 14.4 .
Ma-terial density = 2.3 g/cm3 Material specific heat = 0.123 cal/gC
Thermal capacity per unit volume of bed at minimum fluidisation = 0.02 cal/cm3C
Velocity of fluidising air in bed = 0.33 cm/s ~ 30 The degree of toughening of glass sheets quenched in this fiuidised bed maintained at about 40C are as follows:-Initial Glass Glass Thickness Average Central Temperature (mm) Tensile Stress C ) . _ (MN/m2 ) 650 4 26.3 650 6 32.7 The effective heat transfer coefficient between the bed and the gl~-ss sheets~lay in the range 0.0035 cal/cm2C sec to 0.004 cal/cm2Csec.
Exam~le 9 The particulate refractory material was porous powdered nickel having the following properties:-Mean particle size (~) = 5~um -Particle density (~) = 2.35 g/cm3 Material density = 8.9 g/cm3 ~X~ = 12 Material specific heat = 0.106 cal/gC
Thermal capacity per unit vol~me of bed minimum fluidisation state = 0~37 cal/cm3C
Velocity of fluidising air in bed -- 0~045 cm/s - 7~1 _ ~ lass sheets of thickness in the range 2.3 mm to 6 ~m at an initial temperature of 650C were quenched in a fluidised bed of this po~us nickel powder which ~as in a quiescent state and was maintained at about 40C. The degree of toughening represented by average central tensile stress was as follows:-Glass Thickness Average Central Tensile (mm) Stress (M~/m2) 2.3 77 _ _ _ 115 _. .
The effective heat transfer coefficient between the bed and -the glass sheets was 0.02 cal/cm2C sec.
Exan~e _ 10 .
The parliculate material was a non-porous powdered a alumina. A number of a alumina materials of different mean particle size were used. All these materials had the following common properties:-Particle density (p) = 3.97 g/cm3 Material density = 3.97 g/cm3 Material specific heat = 0.2 cal/gC
The a alumina material was available in different graded particle sizes of the material and four different fluidised beds were constituted as follows:-~0697ao Alumina Mean Part- Thermal Cap- Thermal Cap- Fluidis-Bed icle Size pxd acity of acity of mini- ing gas (d)(~m) Particle mum fluidised ~elocity (cal/C)(cal/cm3&) (cm/s~
_ A 23 92 5 X 10 9 0.32 1.02 B 29 116 10 X 10 9 0.32 1.62 C 45 180 38 X 10-9 0.32 3.90 ¦ D 54 216 66 X 10 0.32 5.61 Glass sheets of thickness in the range 2.3 mm to 12 mm were quenched in these fluidised beds which are each at a temperature of 40C. The initial temperature of the glass sheets was in the range 610C to 670C and the degree of toughening of the sheets is represented by an average central tensile stress in the range 42 MN/m to 104 MN/m .
The effective heat transfer coefficient between the bed and the glass sheets was in the range 0.0062 cal/cm2C sec to 0;0086 cal/cm C sec.
Example 11 A bed of small solid glass spheres was fluidised.
Properties of the bed were as follows:-Particle size range = 0 to 75 ~m Mean particle size (~) = 58~ m Particle density (~1 = 2.5 g/cm3 pxd = 145 Thermal capacity per unit volume of bed at minimum fluidisation = 0.34 cal/c3C
Ve]ocity of fluidising 30 air in bed = 0.41 cm/s .
106970~
Sheets of glass of thickness~ in the range 2.3 mm to 10 mm were heated to an initial temperature in the range 630C to 670C and were quenched in the fluidised bed which was maintained at a temperature of about 40C.
The degree of toughening of the glass sheets was as follows:-Initial GlassGlass Thickness Average Central Temperature(mm) Tensile S2tress (C) (~N/m ) 630 2.3 38 650 2.3 40 650 6 74.5 670 2.3 43 The average effective heat transfer coefficient between the bed and the glass sheets was 0.011 cal/cm2C sec.
To illustrate the high yield of unbroken and undistorted glass sheets obtained when using a gas-fluidised bed according to the invention in a quiescent uniformly expanded state of particulate fluidisation, as compared with the yield when using a bed in a bubbling state of fluidisation, a number of similar sheets of glass of size 30 cm x 30 cm and of thickness 2 mm, 6 mm and 12 mm were treated. The glass sheets had an edge finish in which the edges of the glass sheets were cham-fered using a bonded silicon carbide grinding wheel. This gave a rougher edge finish than that of the glass sheets of Examples 1 to 11 which were finished with a diamond grit wheel. The invention made a high yïeld possible even with this rougher, and cheaper, edge finish.
Each sheet was heated to a temperature as set out below and then immersed in a fluidised bed of the ~ form of porous alumina described in Example 1.
For the purpose of these yield tests some hot glass sheets were immersed in a fluidised bed in a quiescent state as described in Example 1. A bubbling state of fluidisation of the bed was then produced by increasing the fluidising gas velocity above the value producing maximum expansion of the bed, and an equal number of hot glass sheets were immersed in the bubbling bed.
The yield of dimensionally acceptable unbroken glass -sheets, as a percentage of the total number of sheets treated, was as follows:-Glass thickness = 2 mm 20Glass Temperature Yield C QUIESCENT BEDBUBBLING BED
645 95% 52~
660 100% 80%
Glass thickness = 6 mm .. .
Glass Temperature Yield C QUIESCENT BEDBUBBLING BED
640 - - -- 80% 40 645 100~ 60 --` 1069700 Glass thickness - 12 mm Glass Temperature Yield C QUIESCENT BED BUBBLING BED
635 80% 40%
645 100% 75%
Although the above examples were obtained using 30 cm x 30 cm square sheets of glass even lower yields with respect to fracture and distortion result when treating large sheets of glass such as of motor vehicle windscreen size in a bubbling fluidised bed. In contrast the yields obtained when treating such larger sheets of glass in a quiescent fluidised bed are at least as good as those of the examples referred to above.
The value of the stresses induced in the glass decreases as the bed temperature increases and in the limit, which may be about 300C or higher, the stresses in the glass are such that the glass is annealed rather than toughened. Heating and/or cooling elements may be provided on the side walls of the tank 18 for controlling the temperature of the fluidised bed. In all theE~amples the sheets of glass were commercial soda-lime-silica glass such as is used in the manufacture of aircraft windscreen panels, automobile windscreens, ship's windows and architectural panels. Glass of other compositions can be toughened or annealed in the same way using the method of the invention. Also articles other than glass sheets, for example pressed glass articles such as insulators or lens blanks, or blown glass articles can be toughened or annealed by the method of the invention.
A fluidised bed according to the invention may be used for other thermal treatments of glass, for example for the heating of a relatively cold glass article prior to a further ao processing step, heat transfer from the fluidised material to the glass which is immersed in the bed being facilitated without damage to the glass, even when the glass has attained a temperature at which it is susceptible to damage by irregular forces.
The invention may also be used for thermally toughening glass sheets which have been heated and bent while supported in a near-vertical position, and advanced along a horizontal path, as described in United Kingdom Patent Application No.
34703/73 (Specification No. 1,442,316). In the apparatus described in that application the bending dies are enclosed in a heated chamber which is tilted from an inclined position to a position in which the bent glass sheet between the bending dies is vertical and can be lowered vertically into a quiescent fluidised bed of the kind described above.
In another process employing the invention a glass sheet may be heated by immersing the sheet in a fluidised bed which is at a sufficiently high temperature to heat the glass to pre-bending temperature. After removal from the hot bed the sheet is bent, and the bent sheet is then toughened by immersing the glass in a fluidised bed which is in a quiescent uniformly expanded state of particulate fluidisation as - described above. The glass sheet could be carried by the same set of tongs throughout the heating bending and toughening, the tongs being adjustably mounted so that they move to follow the bent shape of the glass. In another arrangement each glass sheet is suspended from non-adjustable tongs for heating and is trans-ferred to lower-edge support during bending in the manner des-cribed in United Kingdom Specification No. 1,442,316, the bent glass sheet being engaged by a second set of tongs which are arranged according to the bent shape of the glass, and lowered into the quiescent fluidised bed for quenching.
Claims (20)
1. A method of thermally treating glass in which the glass is contacted with a gas-fluidised particulate material which is in a quiescent uniformly expanded state of particulate fluidisation to effect heat transfer between the surfaces of the glass and the fluidised material.
2. A method of thermally treating glass, comprising heating the glass to a temperature above its strain point and immersing the glass in a gas-fluidised bed of particulate material which prior to said immersion is in a quiescent uniformly expanded state of particulate fluidisation.
3. A method according to Claim 2 of thermally toughening a glass sheet, comprising heating the glass sheet and then lowering the hot glass sheet into the quiescent uniformly expanded bed of particulate material.
4. A method according to Claim 3 wherein the bed is maintained at a temperature in the range 30°C to 150°C.
5. A method of thermally treating glass in which the glass is contacted in a bed of a gas-fluidised particulate material which is in a quiescent uniformly expanded state of particulate fluidisation which is maintained by regulating the fluidising gas flow by creating a high pressure drop in the fluidising gas flow across a membrane through which fluidising gas enters the bed.
6. A method of thermally treating glass in which the glass is contacted in a bed of a gas-fluidised particulate material comprising particles of density in the range of 0.3 g/cm3 to 3.97 g/cm3 and mean particle size in the range 5µm to 120µm, the material being selected so as to be fluidised in a quiescent uniformly expanded state of particulate fluidisation by fluidising gas flowing uniformly in the bed at a velocity in the range 0.045 cm/s to 5.61 cm/s.
7. A method according to Claim 6, for thermally toughening flat soda-lime-silica glass of thickness in the range 2.3 mm to 12 mm, comprising heating the glass to a temperature in the range 610°C to 680°C, immersing the glass in a fluidised bed in said quiescent state which has a thermal capacity per unit volume at minimum fluidisation in the range 0.02 cal/cm3°C to 0.37 cal/cm3°C, and maintaining the fluidised bed at a temperature up to 150°C
to induce in the glass an average central tensile stress in the range 22 MN/m2 to 115 MN/m2.
to induce in the glass an average central tensile stress in the range 22 MN/m2 to 115 MN/m2.
8. A method according to Claim 6, wherein the particles are a non-porous powdered .alpha. alumina of mean particle size in the range 23 µm to 54 µm and particle density 3.97 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being 0.32 cal/cm3°C.
9. A fluidised bed for use as a quenching medium for thermally toughening a hot glass sheet, comprising particles of mean particle size in the range 5 µm to 120 µm and having a particle density in the range 0.3 g/cm3 to 3.97 g/cm3, and wherein the particles are so selected that the bed is in a quiescent uniformly expanded state of particulate fluidisation and has a thermal capacity per unit volume at minimum fluidisation in the range 0.02 cal/cm3°C to 0.37 cal/cm3°C.
10. A method of thermally treating glass in which the glass is contacted with a gas-fluidised particulate material of non-compacted particle structure which is such that the apparent density of the particles is less than the actual density of the material forming the particles and the buoyant particles const-itute a gas-fluidised bed in a quiescent uniformly expanded state of particulate fluidisation, the material forming the particles and the temperature of the bed being so selected that the heat transfer coefficient of the fluidised bed is sufficient to produce a desired thermal treatment of the glass as it cools in the bed.
11. A method of thermally toughening glass, comprising heating the glass, and immersing the hot glass in a gas-fluidised bed of particles of non-compacted particle structure which is such that the apparent density of the particles is less than the actual density of the material forming the particles and the buoyant particles constitute a gas-fluidised bed in a quiescent uniformly expanded state of particulate fluidisation, the material forming the particles and temperature of the bed being so sele-cted that the heat transfer coefficient of the fluidised bed is sufficient to produce desired toughening stresses in the glass as it cools in the bed.
12. A method according to Claim 11 for thermally toughening a glass sheet, comprising immersing a hot glass sheet in a fluid-ised bed in said quiescent state and constituted by particles of mean particle size in the range 5 µm to 120 µm and apparent part-icle density in the range 0.3 g/cm3 to 2.35 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being in the range 0.02 cal/cm3°C to 0.37 cal/cm3°C.
13. A method of thermally toughening glass, comprising heating the glass, and immersing the hot glass in a gas-fluidised bed of porous particles in a quiescent uniformly expanded state of particulate fluidisation, the material forming the particles and the temperature of the bed being so selected that the heat transfer coefficient of the fluidised bed is sufficient to induce desired toughening stresses in the glass as it cools in the bed.
14. A method according to Claim 13, wherein the particles are porous particles of ? alumina of mean particle size 64 µm and apparent particle density 2.2 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being 0.21 cal/
cm3°C
cm3°C
15. A method according to Claim 13, wherein the particles are of a porous form of aluminosilicate material of mean particle size in the range 60µm to 75µm and apparent particle density in the range 1.21 g/cm3 to 1.22 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being in the range 0.11 cal/cm3°C to 0.19 cal/cm3°C.
16. A method according to Claim 13 wherein the particles are of porous powdered nickel of mean particle size 5µm and apparent particle density 2.35 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being 0.37 cal/
cm3°C.
cm3°C.
17. A method of thermally toughening glass, comprising heating the glass, and immersing the hot glass in a gas-fluidised bed of hollow particles in a quiescent uniformly expanded state of particulate fluidisation, the material forming the particles and the temperature of the bed being so selected that the heat transfer coefficient of the fluidised bed is sufficient to in-duce desired toughening stresses in the glass as it cools in the bed.
18. A method according to Claim 17, wherein the particles are hollow glass spheres of mean particle size in the range 77µm to 120µm and apparent particle density 0.38 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being in the range 0.05 cal/cm3°C to 0.06 cal/cm3°C.
19. A method according to Claim 17, wherein the particles are hollow carbon spheres of mean particle size 48µm and apparent particle density 0.3 g/cm3, the thermal capacity per unit volume of the bed at minimum fluidisation being 0.02 cal/cm3°C.
20. A fluidised bed for use as a quenching medium for thermally toughening a hot glass sheet comprising particles of non-compacted particle structure which is such that the apparent density of the particles is less than the actual density of the material forming the particles wherein the mean particle size of the particles is in the range 5µm to 120µm, the apparent particle density is in the range 0.03 g/cm3 to 2.35 g/cm3, and wherein the particles are so selected that the bed is in a qui-escent uniformly expanded state of particulate fluidisation and has a thermal capacity per unit volume of the bed at minimum fluidisation in the range 0.02 cal/cm3°C to 0.37 cal/cm3°C.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB35769/75A GB1556051A (en) | 1975-08-29 | 1975-08-29 | Thermal treatment of glass |
| GB3577075 | 1975-08-29 | ||
| GB2412376 | 1976-06-10 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1069700A true CA1069700A (en) | 1980-01-15 |
Family
ID=27258307
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA259,724A Expired CA1069700A (en) | 1975-08-29 | 1976-08-24 | Thermal treatment of glass |
Country Status (29)
| Country | Link |
|---|---|
| JP (1) | JPS5843334B2 (en) |
| AR (1) | AR212453A1 (en) |
| AT (1) | AT365549B (en) |
| BG (1) | BG29719A3 (en) |
| CA (1) | CA1069700A (en) |
| CH (1) | CH615654A5 (en) |
| CS (1) | CS212240B2 (en) |
| DD (1) | DD125942A5 (en) |
| DE (1) | DE2638038C3 (en) |
| DK (1) | DK388976A (en) |
| EG (1) | EG12095A (en) |
| ES (1) | ES451057A1 (en) |
| FI (1) | FI60695C (en) |
| GR (1) | GR61298B (en) |
| IE (1) | IE43523B1 (en) |
| IL (1) | IL50268A (en) |
| IN (1) | IN144840B (en) |
| IT (1) | IT1069700B (en) |
| KE (1) | KE3229A (en) |
| LU (1) | LU75680A1 (en) |
| NL (1) | NL175054C (en) |
| NO (1) | NO762937L (en) |
| NZ (1) | NZ181775A (en) |
| PT (1) | PT65527B (en) |
| RO (1) | RO75206A (en) |
| SE (1) | SE420829B (en) |
| TR (1) | TR19806A (en) |
| YU (1) | YU39246B (en) |
| ZM (1) | ZM11076A1 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1556052A (en) * | 1976-06-10 | 1979-11-21 | Pilkington Brothers Ltd | Fluidised bed methods and apparatus for thermally treating glass |
| IE47509B1 (en) * | 1977-12-09 | 1984-04-04 | Pilkington Brothers Ltd | Method and apparatus for thermally thoughening a glass sheet |
| LU80019A1 (en) * | 1978-07-21 | 1980-02-14 | Bfg Glassgroup | PROCESS AND DEVICE FOR HEAT TREATING GLASS AND PRODUCT OBTAINED |
| JPS61259620A (en) * | 1985-05-14 | 1986-11-17 | 松下電器産業株式会社 | Mixer |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE752981C (en) * | 1935-07-31 | 1953-02-02 | Corning Glass Works | Process for hardening glass |
| US2670573A (en) * | 1950-02-13 | 1954-03-02 | Jr Frederick W Sullivan | Thermal treatment of ceramic objects |
| BE539784A (en) * | 1954-07-16 |
-
1976
- 1976-08-13 IE IE1802/76A patent/IE43523B1/en unknown
- 1976-08-16 IN IN1487/CAL/76A patent/IN144840B/en unknown
- 1976-08-16 IL IL50268A patent/IL50268A/en unknown
- 1976-08-16 NZ NZ181775A patent/NZ181775A/en unknown
- 1976-08-24 ZM ZM110/76A patent/ZM11076A1/en unknown
- 1976-08-24 DE DE2638038A patent/DE2638038C3/en not_active Expired
- 1976-08-24 CA CA259,724A patent/CA1069700A/en not_active Expired
- 1976-08-25 YU YU2074/76A patent/YU39246B/en unknown
- 1976-08-26 GR GR51551A patent/GR61298B/en unknown
- 1976-08-26 NL NLAANVRAGE7609488,A patent/NL175054C/en not_active IP Right Cessation
- 1976-08-26 TR TR19806A patent/TR19806A/en unknown
- 1976-08-26 NO NO762937A patent/NO762937L/no unknown
- 1976-08-26 BG BG7634076A patent/BG29719A3/en unknown
- 1976-08-27 IT IT69105/76A patent/IT1069700B/en active
- 1976-08-27 DD DD194501A patent/DD125942A5/xx unknown
- 1976-08-27 ES ES451057A patent/ES451057A1/en not_active Expired
- 1976-08-27 DK DK388976A patent/DK388976A/en not_active Application Discontinuation
- 1976-08-27 LU LU75680A patent/LU75680A1/xx unknown
- 1976-08-27 AR AR264480A patent/AR212453A1/en active
- 1976-08-27 PT PT65527A patent/PT65527B/en unknown
- 1976-08-27 CH CH1091876A patent/CH615654A5/en not_active IP Right Cessation
- 1976-08-27 SE SE7609544A patent/SE420829B/en not_active IP Right Cessation
- 1976-08-27 CS CS765593A patent/CS212240B2/en unknown
- 1976-08-27 FI FI762468A patent/FI60695C/en not_active IP Right Cessation
- 1976-08-27 AT AT0637076A patent/AT365549B/en not_active IP Right Cessation
- 1976-08-28 RO RO7687398A patent/RO75206A/en unknown
- 1976-08-29 EG EG534/76A patent/EG12095A/en active
- 1976-08-30 JP JP51102724A patent/JPS5843334B2/en not_active Expired
-
1982
- 1982-08-14 KE KE3229A patent/KE3229A/en unknown
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