US2624475A - Method and apparatus for feeding glass furnaces - Google Patents
Method and apparatus for feeding glass furnaces Download PDFInfo
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- US2624475A US2624475A US108554A US10855449A US2624475A US 2624475 A US2624475 A US 2624475A US 108554 A US108554 A US 108554A US 10855449 A US10855449 A US 10855449A US 2624475 A US2624475 A US 2624475A
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- 239000011521 glass Substances 0.000 title description 21
- 238000000034 method Methods 0.000 title description 15
- 230000000979 retarding effect Effects 0.000 description 27
- 239000006060 molten glass Substances 0.000 description 18
- 230000000903 blocking effect Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- PCTMTFRHKVHKIS-BMFZQQSSSA-N (1s,3r,4e,6e,8e,10e,12e,14e,16e,18s,19r,20r,21s,25r,27r,30r,31r,33s,35r,37s,38r)-3-[(2r,3s,4s,5s,6r)-4-amino-3,5-dihydroxy-6-methyloxan-2-yl]oxy-19,25,27,30,31,33,35,37-octahydroxy-18,20,21-trimethyl-23-oxo-22,39-dioxabicyclo[33.3.1]nonatriaconta-4,6,8,10 Chemical compound C1C=C2C[C@@H](OS(O)(=O)=O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2.O[C@H]1[C@@H](N)[C@H](O)[C@@H](C)O[C@H]1O[C@H]1/C=C/C=C/C=C/C=C/C=C/C=C/C=C/[C@H](C)[C@@H](O)[C@@H](C)[C@H](C)OC(=O)C[C@H](O)C[C@H](O)CC[C@@H](O)[C@H](O)C[C@H](O)C[C@](O)(C[C@H](O)[C@H]2C(O)=O)O[C@H]2C1 PCTMTFRHKVHKIS-BMFZQQSSSA-N 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
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- 230000036461 convulsion Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000005816 glass manufacturing process Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
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- 239000011819 refractory material Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B3/00—Charging the melting furnaces
Definitions
- An object of .thisinvention is to make it'possi- .ble to vary the direction .of the said sheet of batch, either in order to correctdeviations due to .accidental causes. or in order tobring thesheet at each instant to that point ofthe furnace at which the melting conditions are. the best.
- the present invention relates to a method and .apparatus by means of which it is possible to guide the sheet of batch in its progressat will.
- theprogress of the sheet isretarded over all or part of its length when, after having been distributed over the bath, the sheet advances under the action of the feeding arrangement.
- This retarding action is exerted :by 40118 or .more elements penetrating. more orless deeply into the sheet, at the.necessaryapointsfor imparting the required direction thereto.
- jIt .is-xthus possible to act on the sheet of batch in: proximity to the feeding arrangement before it hasbeen subjected to the action of theflames and" thus to controlfroma distance. its displacement over its entire length.
- Fig. 1 is a plan view of the rear of atankfurna-ce and of the head thereof, onxwhich-there is fitted a feeding arrangement of the type. described in applicants Belgian Patent'No. 466,139 of the 22nd June 1946,
- Fig. 2 is a vertical section along the lineII-II of. Fig. 1,
- Fig. 3 is across-section along the line III- III of Fig. 1,
- Fig. l is a plan view; similar to .that of Fig. 1, showing another formv of embodiment of the method,
- Fig. 5 is a cross-section along the-line 1V--V:of Fig. 4,
- FIG. 6 is asection similar to Fig. 5, but showing a variant of the arrangementof-Figs. 4 and5,
- Fig. 7 is-a plan view similar to Fig. 1, showing :another form of theinvention
- Fig.8 isa longitudinal section along the line VIII-VIII ofiFig. '7, and
- Fig. 9 illustrates the application of the method according to .the invention to a'furna-ce equipped .witha feeding arrangement different from that :of 2 the :preceding figures.
- The.furnace-feeding arrangement 3 here shown is the .bladedroller of the arrangement forming the. subjectof applicants Belgian Patent No. 466,139, but it will be understood that it may be replaced-by any other arrangement for feeding .the batchin sheet form into the furnace. 20
- the sheet ofbatch 5 is deposited at '1": by a distributby the feeding'arrangementii, which also imparts thereto an impulse causing it to progress continuously towardsthe interior of the furnace.
- The, glass ingredients which arehandled by the apparatus and method of the present invention have been referred to as batch and may here- These terms of limitation.
- the method and apparatus of the invention are adaptable for use with substantially alluingredients'used in glass making and with a wide range of particle sizes.
- the use of these .phrases is not intended to limit the invention to .the use of any specific material nor to any specific particle size or range of sizes.
- a partial or differential retarding action is exerted on its movement.
- a resistant element which can be constructed of refractory material, or which may be constituted by a metal pipe in which water circulates, as shown at 1.
- the said pipe may be curved as shown in Fig. 3 and it is so inclined as to touch the sheet of batch 5, and even to penetrate into the said sheet over a part of its length.
- the position of the said pipe may be controlled so as to vary the position and the length of its zone of contact with the sheet of batch and the strength of its action thereon.
- the force which moves the batch downwardly is a resultant force derived from the driving force acting on the sheet and the reactive force acting through the pipe I.
- the reactive force of the pipe I has a component acting in opposition to the forward movement of the sheet.
- the friction of the batch against the pipe also tends to retard the movement of the sheet and the underlying layer of molten glass.
- the reac tive force opposing the forward movement of the sheet and the friction of the sheet against the pipe 1 both increase as the pipe I is lowered. Consequently the retarding effect increases as the pipe is lowered. In the construction shown in Fig. 3, the retarding effect also varies from one edge of the sheet to the other.
- the height and the inclination of the pipe with respect to the sheet may be varied by adjusting the height and the inclination of the pipe with respect to the sheet, as also the length of pipe brought into contact with the batch.
- This adjustment is effected by means known per se, for example by raising or lowering one or both of the supports I4, IS.
- the retarding effect of the pipe 1 produces either a compression of the batch in the direction of the forward movement of the sheet, or a relative sliding of the furnace feeding member with respect to the sheet, this sliding taking place on the part of the sheet which is aligned with the portion in contact with the pipe and being proportional to the strength of the action of the said pipe.
- the initial speed imparted by the feeding arrangement to the sheet which speed was constant at all points- is modified proportionally to the strength of the retardation.
- the resultant speed is therefore variable from one edge of the sheet to the other, being lowest at the point 8 and highest at the point 9. It follows that the sheet of batch undergoes a rotational movement and spreads out fanwise, its edges following paths such as CDE and AFGI-I (Fig. l).
- the pipe I may also be given other forms, for example that shown in Fig. 5.
- the retarding action is highest on the edges of the sheet and lowest or even zero at the centre, according to whether the pipe emerges in the neighbourhood of the axis of the sheet or not.
- the speed therefore varies from one edge to the other, being lowest on the edges and highest at the centre.
- the sheet is then spread out fanwise in the form shown in Fig. 4, the edges following paths such as AEF and CMN, so that it eventually covers all the surface of the bath in th tank of the furnace, thus enabling a continuous sheet of batch to be set up, which extends over the entire width of the tank I, while the head 4 through which it is introduced is of substantially smaller width than the actual tank.
- the dotted lines represent the evolution of the 7 form of a generatrix AC in proportion as it progresses.
- the retarding device is located, not on the output side of the feeding arrangement 3, but well in front of it, between the point at which the sheet of batch is deposited on the molten glass and that at which it receives its impulse from the feeding machine 3 for the purpose of feeding it towards the interior of the furnace.
- Tests carried out by the applicants have in fact proved that if the differential retarding action is exerted on the sheet of batch slightly before it receives the said impulse, it behavesby reason of its cohesionin-the same manner as if the retarding actionwere applied on -the output side of the feeding arrangement.
- a method of feeding batch in granular form into a glass furnace comprising feeding the batch onto the surface of the molten glass as a floating sheet of substantially uniform thickness, imparting an impulse to the sheet to move it into the furnace, and applying a retarding action to a portion only of said sheet adjacent the upper surface thereof and having a substantial depth, while leaving a laterally adjacent portion unretarded, so that the unretarded portion moves faster than and is turned toward the retarded portion.
- a method of feeding batch in granular form into a glass furnace comprising feeding a floating sheet of batch onto the surface of the molten glass near one end of the furnace, impelling said sheet towards the opposite end of the furnace, and blocking the movement in the direction of said opposite end of a portion of said sheet adjacent the upper surface thereof and having a substantial depth which varies across the width of the sheet, so that the speed of the sheet is varied in proportion to the depth of the blocking and the less blocked portions move faster than and are turned toward the more blocked portions.
- a method of feeding batch in granular form into a glass furnace comprising feeding the batch onto the surface of the molten glass near one end of the furnace, spreading the batch over the glass to form a floating sheet of substantially uniform thickness, impelling said sheet towards the opposite end of said furnace, applying a retarding action to said sheet over only part of its width, and varying the direction of progress of said sheet by regulating said retarding action.
- a method of feeding batch in granular form into a glass furnace comprising feeding the batch onto the surface of the molten glass near one end of the furnace, spreading the batch over the glass to form a floating sheet of substantially uniform thickness, impelling said sheet towards the opposite end of said furnace, and applying a controllable retarding action to the upper surface of the marginal portions only of said sheet.
- a method of feeding batch in granular form into a glass furnace comprising feeding the batch onto the surface of the molten glass as a floating sheet interrupted in the center, impelling the two parts of said sheet side by side towards said furnace, and applying a retarding action to the outer marginal portions only of said sheet.
- An apparatus forfeeding batch" into a glass the progress of of its width, said retarding means comprising. at
- At least one member reachin'g below the surface of said sheet but above the surface of the glass.
- the means for producing a retarding action on the sheet of batch comprises a tube extending across said sheet and inclined downwardly on at least one side thereof.
- An apparatus for feeding granular batch into a glass furnace comprising in combination with a furnace, means for feeding side by side two floating half-sheets of batch onto the surface of the molten glass at the inlet end of said furnace, means for impelling said half-sheets towards the opposite end of said furnace, and means for producing a retarding action on the progress of said half sheets, said means engaging said half-sheets only near the outer edges thereof.
- An apparatus for feeding pulverulent batch into a glass furnace comprising in combination with a furnace having a head narrower than the main furnace, means for distributing a floating sheet of pulverulent batch over the surface of the molten glass and extending substantially the whole width of said head, means for impelling said sheet towards and into said furnace, and means in contact with the marginal portions only of the upper surface of said sheet to retard the progress of said marginal portions and cause said sheet to spread laterally into the furnace.
- a method of feeding batch in granular form into a glass furnace comprising the steps of feeding the batch onto the surface of the molten glass as a floating sheet of substantially uniform thickness, applying to said sheet a driving force which is substantially uniform over the width of the sheet, and blocking the movement in the direction of said force of a portion of said sheet adjacent the upper surface thereof and having a thickness which varies along the width of the sheet, so that the speed of the sheet is varied along its width and the faster moving portions are turned toward the slower moving portions, thereby diverting at least part of the sheet from the direction of movement imparted by said driving force.
- Apparatus for feeding batch into a glass furnace comprising means for feeding onto the surface of the molten glass a floating sheet of batch in granular form, said sheet being of substantially uniform thickness, means for diverting at least part of the sheet from the direction of movement imparted by the feeding means comprising means projecting downwardly into the path of travel of the sheet a distance which varies along the width of the sheet, said downwardly projecting means being effective to retard the speed of the portions of the sheet engaged thereby.
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Description
Jan. 6,-1953 6. 1.. HENRY ET AL 2,624,475
METHOD AND APPARATUS-FOR FEEDING GLASS FURNACES Filed Aug. 4, 1949 2 SHEETS-SHEET 1 Jan. 6, 1953 G 1... HENRY ETAL ,6
METHOD AND APPARATUS FOR FEEDING GLASS FURNACES Filed Aug. 4, 1949 2 SHEETS-SHEET 2 INVENTORS (fear 4 Z. Henry m inward Patented Jan. 6, 1953 UNITED STATES PATENT OFFICE METHOD AND APPARATUS FOR -FEEDING GLASS FURNACES Georges Leon Henry and EdgardBrichard, Jumet,
Belgium, assignors to Union 'des Verreries Mecaniques Belges S. A., Charleroi, Belgium, a
Belgian company Application August 4, 1949, Serial No. 108,554 In Belgium August 20, 1948 14 Claims. 1
It is known to feed vitrifiable materials into glass tank furnaces by introducing the mixture of the. said materials-knownv asthe batchinto the furnace in the form of a substantially continuous sheet orxlayer of uniform thickness, which floats on the molten bath andmelts in proportion as it progresses into thefurnace.
An object of .thisinvention is to make it'possi- .ble to vary the direction .of the said sheet of batch, either in order to correctdeviations due to .accidental causes. or in order tobring thesheet at each instant to that point ofthe furnace at which the melting conditions are. the best.
The present invention relates to a method and .apparatus by means of which it is possible to guide the sheet of batch in its progressat will. To this end, theprogress of the sheet isretarded over all or part of its length when, after having been distributed over the bath, the sheet advances under the action of the feeding arrangement. This retarding action is exerted :by 40118 or .more elements penetrating. more orless deeply into the sheet, at the.necessaryapointsfor imparting the required direction thereto. jIt .is-xthus possible to act on the sheet of batch in: proximity to the feeding arrangement before it hasbeen subjected to the action of theflames and" thus to controlfroma distance. its displacement over its entire length.
In order that the invention may be readily understood, reference will be made to the.following figures, which show by way of example a number of forms of embodiment thereof: 7
Fig. 1 is a plan view of the rear of atankfurna-ce and of the head thereof, onxwhich-there is fitted a feeding arrangement of the type. described in applicants Belgian Patent'No. 466,139 of the 22nd June 1946,
Fig. 2 is a vertical section along the lineII-II of. Fig. 1,
Fig. 3 is across-section along the line III- III of Fig. 1,
Fig. lis a plan view; similar to .that of Fig. 1, showing another formv of embodiment of the method,
Fig. 5 is a cross-section along the-line 1V--V:of Fig. 4,
"Fig. 6 is asection similar to Fig. 5, but showing a variant of the arrangementof-Figs. 4 and5,
Fig. 7 is-a plan view similar to Fig. 1, showing :another form of theinvention,
Fig.8 isa longitudinal section along the line VIII-VIII ofiFig. '7, and
Fig. 9 illustrates the application of the method according to .the invention to a'furna-ce equipped .witha feeding arrangement different from that :of 2 the :preceding figures.
.inafter be described as granular. .are employed in. a. generic sense and not by way .the liquid mass. ithe interiorof the furnace, it carries with it a ilnlthezexampleillustratedin Figs. 1 to. 3, the
itank .l of the tank furnaces is extended rear- .wardly by aheadt of a width generally smaller .thanthat of the tank. The molten glass 2 fills the tank I and thehead 4 to a certainheight.
The.furnace-feeding arrangement 3 here shown is the .bladedroller of the arrangement forming the. subjectof applicants Belgian Patent No. 466,139, but it will be understood that it may be replaced-by any other arrangement for feeding .the batchin sheet form into the furnace. 20
:ing hopper'll and distributed over the head t The sheet ofbatch 5 is deposited at '1": by a distributby the feeding'arrangementii, which also imparts thereto an impulse causing it to progress continuously towardsthe interior of the furnace.
The, glass ingredients which arehandled by the apparatus and method of the present invention have been referred to as batch and may here- These terms of limitation. The method and apparatus of the invention are adaptable for use with substantially alluingredients'used in glass making and with a wide range of particle sizes. The use of these .phrases is not intended to limit the invention to .the use of any specific material nor to any specific particle size or range of sizes.
When the sheet of batch is deposited on the surface of the molten glass, it floats there, with :thelower portion of the sheet sunk slightly into As they sheet is pushed toward portion of the liquid near the surface thereof,
.creatingqa current which transmits the driving force ,to other parts of the sheet. Some driving force-is also transmitted through the sheet itself. Thesheet and the adjacent portion of the liquid act asa more or less cohesive mass.
Under-this impulse, the sheet assumes a certain speed "which is constant at all points, and. advances regularly .without deformation, the
3 edges thus following the straight paths AB and CD. In this way, a practically continuous sheet is obtained, which covers the surface ABCD which melts in proportion as it progresses into the zone of action of the flames from the hearth of the furnace.
To vary the direction of the sheet, according to the present invention, a partial or differential retarding action is exerted on its movement.
To this end, a resistant element is employed which can be constructed of refractory material, or which may be constituted by a metal pipe in which water circulates, as shown at 1. The said pipe may be curved as shown in Fig. 3 and it is so inclined as to touch the sheet of batch 5, and even to penetrate into the said sheet over a part of its length. The position of the said pipe may be controlled so as to vary the position and the length of its zone of contact with the sheet of batch and the strength of its action thereon.
In the case of Fig. 3, it will be seen that the pipe I, which hardly touches the layer of batch 5 on its edge 9, is so inclined that its contact with the sheet is progressively more pronounced in the direction towards the edge 8, without however reaching the level of the molten glass. As it passes below the pipe I, the batch is compressed between the said pipe and the molten glass 2 on which the sheets floats. The sheet of batch is forced downwardly against the buoyant force which tends to keep the sheet floating on the molten glass. As the sheet is pushed farther down by the pipe I, the buoyant force acting upwardly increases and consequently the friction between the pipe 1 and the surface of the batch also increases. The force which moves the batch downwardly is a resultant force derived from the driving force acting on the sheet and the reactive force acting through the pipe I. The reactive force of the pipe I has a component acting in opposition to the forward movement of the sheet. The friction of the batch against the pipe also tends to retard the movement of the sheet and the underlying layer of molten glass. The reac tive force opposing the forward movement of the sheet and the friction of the sheet against the pipe 1, both increase as the pipe I is lowered. Consequently the retarding effect increases as the pipe is lowered. In the construction shown in Fig. 3, the retarding effect also varies from one edge of the sheet to the other. As hereinbefore explained, it may be varied by adjusting the height and the inclination of the pipe with respect to the sheet, as also the length of pipe brought into contact with the batch. This adjustment is effected by means known per se, for example by raising or lowering one or both of the supports I4, IS.
The retarding effect of the pipe 1 produces either a compression of the batch in the direction of the forward movement of the sheet, or a relative sliding of the furnace feeding member with respect to the sheet, this sliding taking place on the part of the sheet which is aligned with the portion in contact with the pipe and being proportional to the strength of the action of the said pipe.
Owing to this retarding effect, the initial speed imparted by the feeding arrangement to the sheet which speed was constant at all points-is modified proportionally to the strength of the retardation. The resultant speed is therefore variable from one edge of the sheet to the other, being lowest at the point 8 and highest at the point 9. It follows that the sheet of batch undergoes a rotational movement and spreads out fanwise, its edges following paths such as CDE and AFGI-I (Fig. l).
The pipe I may also be given other forms, for example that shown in Fig. 5. In this case, the retarding action is highest on the edges of the sheet and lowest or even zero at the centre, according to whether the pipe emerges in the neighbourhood of the axis of the sheet or not. The speed therefore varies from one edge to the other, being lowest on the edges and highest at the centre. The sheet is then spread out fanwise in the form shown in Fig. 4, the edges following paths such as AEF and CMN, so that it eventually covers all the surface of the bath in th tank of the furnace, thus enabling a continuous sheet of batch to be set up, which extends over the entire width of the tank I, while the head 4 through which it is introduced is of substantially smaller width than the actual tank.
The dotted lines represent the evolution of the 7 form of a generatrix AC in proportion as it progresses.
This effect is further accentuated if the feeding arrangement is adapted to interrupt the sheet at its centre as shown in Fig. 6. Two separate sheets are then formed; one on the left turning to the left, and one on the right turning to the right, and these two sheets, can by reason of the rotational movements, reach the side walls of the furnace, and thus cover the entire surface of the bath, in the rear part of the tank.
The result of these various arrangements will be to spread out the batch fanwise over the entire width of the tank of the furnace. The molten glass bath will therefore be practically covered over its entire surface in the melting zone, which will impart maximum efficiency to the said zone. In this way, also, the batch will be prevented from travelling too rapidly forward under the action of the feeding arrangement alone, which would be likely to promote too rapid a passage, through the melting zone, of portions of batch which might thus escape the effect of the high temperatures before having melted completely.
The same result can also be obtained by exerting the retarding action on the sheet of batch, not by means of a continuous element, but by means of a series of retarding elements In disposed as diagrammatically indicated in Figs. 7 and 8. These retarding elements-which consist of retractory materials or are constituted by metal members cooled by water circulation are mounted on a support [6 by known means, and are adapted to be individually adjusted so as to be able to exert a progressive retarding action from one edge of the sheet to the other, and to produce discontinuously a variation of the retarding action similar to that which is continuously obtained in the arrangements hereinbefore described.
It is further to be noted from Figs. '7 and 8 that the retarding device is located, not on the output side of the feeding arrangement 3, but well in front of it, between the point at which the sheet of batch is deposited on the molten glass and that at which it receives its impulse from the feeding machine 3 for the purpose of feeding it towards the interior of the furnace. Tests carried out by the applicants have in fact proved that if the differential retarding action is exerted on the sheet of batch slightly before it receives the said impulse, it behavesby reason of its cohesionin-the same manner as if the retarding actionwere applied on -the output side of the feeding arrangement.
It will readily be understoodthatthemethod according to the invention is applicable to a sheet of batch regardless of the type of feeding apparatus from which it receives the impulse necessary to cause it to progress towards the furnace. In Fig. 9, there'is-shown the application of the invention to a glass furnace equipped with an apparatus comprising a push member:
from the hopper H is deposited on the bath.
In its forward movement, the push member l3 forces the batch before it, thus forming a practically continuous sheet which progresses in jerks. The pipe 1 exerts its action on the sheet thus formed, in the same way as in Figs. 1 to 6.
Other modifications in the form of the arrangements described are obviously possible without departing from the scope of the invention.
We claim:
1. A method of feeding batch in granular form into a glass furnace, comprising feeding the batch onto the surface of the molten glass as a floating sheet of substantially uniform thickness, imparting an impulse to the sheet to move it into the furnace, and applying a retarding action to a portion only of said sheet adjacent the upper surface thereof and having a substantial depth, while leaving a laterally adjacent portion unretarded, so that the unretarded portion moves faster than and is turned toward the retarded portion.
2. A method of feeding batch in granular form into a glass furnace, comprising feeding a floating sheet of batch onto the surface of the molten glass near one end of the furnace, impelling said sheet towards the opposite end of the furnace, and blocking the movement in the direction of said opposite end of a portion of said sheet adjacent the upper surface thereof and having a substantial depth which varies across the width of the sheet, so that the speed of the sheet is varied in proportion to the depth of the blocking and the less blocked portions move faster than and are turned toward the more blocked portions.
3. A method of feeding batch in granular form into a glass furnace, comprising feeding the batch onto the surface of the molten glass near one end of the furnace, spreading the batch over the glass to form a floating sheet of substantially uniform thickness, impelling said sheet towards the opposite end of said furnace, applying a retarding action to said sheet over only part of its width, and varying the direction of progress of said sheet by regulating said retarding action.
4. A method of feeding batch in granular form into a glass furnace, comprising feeding the batch onto the surface of the molten glass near one end of the furnace, spreading the batch over the glass to form a floating sheet of substantially uniform thickness, impelling said sheet towards the opposite end of said furnace, and applying a controllable retarding action to the upper surface of the marginal portions only of said sheet.
5. A method of feeding batch in granular form into a glass furnace, comprising feeding the batch onto the surface of the molten glass as a floating sheet interrupted in the center, impelling the two parts of said sheet side by side towards said furnace, and applying a retarding action to the outer marginal portions only of said sheet.
6. An apparatus forfeeding batch" into a glass the progress of of its width, said retarding means comprising. at
least one member reachin'g below the surface of said sheet but above the surface of the glass.
'7. An apparatus for feeding batch into-a. glass furnace comprisingin combinationwith afurnac'e,= mea'n's for'feeding the batch in the formof a floating sheet of granular material onto the surface ofthe molten glass" at the head of said furnace, ineans for impelling the sheet of batch towards the opposite end of the furnace, and means engaging the upper surface of said sheet for producing on the progress of said sheet a nonuniform retarding action which varies from one side edge of the sheet to the other.
8. An apparatus as claimed in claim '7, wherein the retarding means for producing a retarding action on the sheet of batch comprises an element extending over the entire width of the sheet of batch and penetrating into the sheet by unequal depths at different points of said width.
9. An apparatus as claimed in claim '7, wherein the means for producing a retarding action on the sheet of batch comprises a plurality of adjustable elements arranged side by side.
10. An apparatus as claimed in claim 7, wherein the means for producing a retarding action on the sheet of batch comprises a tube extending across said sheet and inclined downwardly on at least one side thereof.
11. An apparatus for feeding granular batch into a glass furnace, comprising in combination with a furnace, means for feeding side by side two floating half-sheets of batch onto the surface of the molten glass at the inlet end of said furnace, means for impelling said half-sheets towards the opposite end of said furnace, and means for producing a retarding action on the progress of said half sheets, said means engaging said half-sheets only near the outer edges thereof.
12. An apparatus for feeding pulverulent batch into a glass furnace, comprising in combination with a furnace having a head narrower than the main furnace, means for distributing a floating sheet of pulverulent batch over the surface of the molten glass and extending substantially the whole width of said head, means for impelling said sheet towards and into said furnace, and means in contact with the marginal portions only of the upper surface of said sheet to retard the progress of said marginal portions and cause said sheet to spread laterally into the furnace.
13. A method of feeding batch in granular form into a glass furnace, comprising the steps of feeding the batch onto the surface of the molten glass as a floating sheet of substantially uniform thickness, applying to said sheet a driving force which is substantially uniform over the width of the sheet, and blocking the movement in the direction of said force of a portion of said sheet adjacent the upper surface thereof and having a thickness which varies along the width of the sheet, so that the speed of the sheet is varied along its width and the faster moving portions are turned toward the slower moving portions, thereby diverting at least part of the sheet from the direction of movement imparted by said driving force.
14. Apparatus for feeding batch into a glass furnace, comprising means for feeding onto the surface of the molten glass a floating sheet of batch in granular form, said sheet being of substantially uniform thickness, means for diverting at least part of the sheet from the direction of movement imparted by the feeding means comprising means projecting downwardly into the path of travel of the sheet a distance which varies along the width of the sheet, said downwardly projecting means being effective to retard the speed of the portions of the sheet engaged thereby.
GEORGES LEON HENRY. EDGARD BRICHARD.
REFERENCES CITED The following references are of record in the file of this patent:
Number UNITED STATES PATENTS
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BE2624475X | 1948-08-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2624475A true US2624475A (en) | 1953-01-06 |
Family
ID=3895965
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US108554A Expired - Lifetime US2624475A (en) | 1948-08-20 | 1949-08-04 | Method and apparatus for feeding glass furnaces |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US2624475A (en) |
| BE (1) | BE484466A (en) |
| DE (1) | DE816127C (en) |
| NL (1) | NL147813B (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2926458A (en) * | 1955-12-13 | 1960-03-01 | Owens Illinois Glass Co | Colored glass frit feeder |
| US2934225A (en) * | 1953-03-24 | 1960-04-26 | Pittsburgh Plate Glass Co | Method and apparatus for feeding batch materials |
| US3074568A (en) * | 1958-02-05 | 1963-01-22 | Libbey Owens Ford Glass Co | Method of and apparatus for feeding glass batch materials |
| US3077273A (en) * | 1957-10-28 | 1963-02-12 | Libbey Owens Ford Glass Co | Apparatus for feeding glass batch materials |
| US3193119A (en) * | 1963-09-25 | 1965-07-06 | Libbey Owens Ford Glass Co | Method and apparatus for feeding batch materials to a glass-melting furnace |
| US4004903A (en) * | 1975-06-05 | 1977-01-25 | Libbey-Owens-Ford Company | Method of and apparatus for increasing the melting rate of glass making materials |
| FR2455567A1 (en) * | 1979-05-01 | 1980-11-28 | Central Glass Co Ltd | DEVICE FOR PRODUCING WINDOW GLASS |
| US4319904A (en) * | 1980-09-08 | 1982-03-16 | Ppg Industries, Inc. | Method and apparatus for guiding glass batch in a glass melting furnace |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1083511B (en) * | 1958-02-05 | 1960-06-15 | Libbey Owens Ford Glass Co | Method and apparatus for feeding fine particles of glass-forming material into the entrance end of a furnace |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1623057A (en) * | 1925-05-14 | 1927-04-05 | Mississippi Glass Co | Batch feeding to glass tanks |
| US2281050A (en) * | 1940-04-11 | 1942-04-28 | Pittsburgh Plate Glass Co | Batch feeding apparatus |
-
0
- NL NL666611475A patent/NL147813B/en unknown
- BE BE484466D patent/BE484466A/xx unknown
-
1949
- 1949-08-04 US US108554A patent/US2624475A/en not_active Expired - Lifetime
-
1950
- 1950-04-27 DE DEU217A patent/DE816127C/en not_active Expired
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1623057A (en) * | 1925-05-14 | 1927-04-05 | Mississippi Glass Co | Batch feeding to glass tanks |
| US2281050A (en) * | 1940-04-11 | 1942-04-28 | Pittsburgh Plate Glass Co | Batch feeding apparatus |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2934225A (en) * | 1953-03-24 | 1960-04-26 | Pittsburgh Plate Glass Co | Method and apparatus for feeding batch materials |
| US2926458A (en) * | 1955-12-13 | 1960-03-01 | Owens Illinois Glass Co | Colored glass frit feeder |
| US3077273A (en) * | 1957-10-28 | 1963-02-12 | Libbey Owens Ford Glass Co | Apparatus for feeding glass batch materials |
| US3074568A (en) * | 1958-02-05 | 1963-01-22 | Libbey Owens Ford Glass Co | Method of and apparatus for feeding glass batch materials |
| US3193119A (en) * | 1963-09-25 | 1965-07-06 | Libbey Owens Ford Glass Co | Method and apparatus for feeding batch materials to a glass-melting furnace |
| US4004903A (en) * | 1975-06-05 | 1977-01-25 | Libbey-Owens-Ford Company | Method of and apparatus for increasing the melting rate of glass making materials |
| FR2455567A1 (en) * | 1979-05-01 | 1980-11-28 | Central Glass Co Ltd | DEVICE FOR PRODUCING WINDOW GLASS |
| US4319904A (en) * | 1980-09-08 | 1982-03-16 | Ppg Industries, Inc. | Method and apparatus for guiding glass batch in a glass melting furnace |
Also Published As
| Publication number | Publication date |
|---|---|
| NL147813B (en) | |
| BE484466A (en) | |
| DE816127C (en) | 1951-10-08 |
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