• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    An orifice plate for use in a drawing assembly of the type wherein the plate has a flat undersurface devoid of nozzles, and bulk gas is directed toward the undersurfaces to cool fibers being drawn through the plate. The plate is characterized in that the orifices therein are arranged in sets with the orifices in the respective sets so spaced relative to one another that, in the event of the breakage of a fiber being drawn from one of the orifices of a set, the glass supplied to the orifice will flood to and join the other of the orifices in the set prior to flooding to the orifices of other sets.
    公开号:SU948287A3
    申请号:SU762387060
    申请日:1976-08-13
    公开日:1982-07-30
    发明作者:Хэйли Коггин Чарльз (Младший)
    申请人:Нитто Босеки Ко,Лтд (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to the building materials industry, in particular to devices for drawing fiberglass. A known spunbond plate for drawing glass fiber, including a perforated plate, the holes of which are grouped, and a current lead 1. In a known plate, it is impossible to ensure guaranteed flow of glass melt within the group and eliminate or minimize glass melt from the holes of one band to the hole of another pipe i.e. it is impossible to provide controlled overflow in order to produce thickened fiber from a pair of adjacent holes when curving glass fiber, which can then be easily divided into a pair of fibers, each of which will feed a single die hole. The purpose of the invention is to increase the efficiency of extrusion. This goal is achieved by the fact that in a spunbond plate for drawing fiberglass, including a perforated plate, the holes of which are grouped, and the current lead, the group includes no more than three holes of the same diameter with a distance between their centers of 1.20-1.45 diameter, the distance between the centers of the extreme holes of adjacent groups is 1.4-1.55 of the diameter of the holes. The number of holes in each group is 3, and their centers are located at the vertices of an isosceles triangle. The groups are arranged in parallel rows, with the distance between the extreme openings of adjacent rows more than the distance between the extreme openings of adjacent groups within the rows. The holes of each row have the same diameter, and the distances between the outer holes of the adjacent rows are 1.55-1.70 times the diameter. FIG. 1 schematically shows an installation for making fiberglass, equipped with the proposed spin plate f in FIG. 2 - one of the sections of the proposed die in an enlarged scale, section; it is shown how self-correcting occurs when one of the holes is drilled in the coupled holes of the spinneret; on fi1. 3 - section A-L in FIG. 1. in an enlarged scale; in fig. 4 section bb in fig. 3 (lower plane of the proposed spin plate, in Fig. 5, the lower cavity of the segment of the spin plate, made in accordance with the first embodiment, on an enlarged scale; Fig. B - section 6 of the segment of the spin plate, shown in FIG. 5, c. Fig. 7 is another embodiment of the lower surface of the proposed filler plate; Fig. 8 is the third embodiment of the filler plate; Fig. 9 is a portion of the filler plate of the third embodiment of the shadow and is shown schematically several Upp holes, one of which is circled in Fig. 9 with a dash-dotted line; bottom view; Fig. 10 shows the dependence of the contact angle of glass equilibrium on the glass temperature, typical of those glass components for which the proposed bushing plate is intended to stretch The installation has a glass-melting furnace feeder 1, on which a removable sleeve 2 is located at the bottom, the design of which includes a spinneret plate 3. The melted glass 4 from the feeder of the furnace 1 enters the sleeve 2 and flows out of the holes of the die 3 as individual fiberglass yarns 5. The fibers pass through the lubricant 6, which deposits a layer of bonding material on them, and the roller 7 and the guide to the winding mechanism B, along which the transverse spreader 9 moves. Due to resistive heating of the filter plate 3 the glass mass inside sleeve 2 is constantly at elevated temperature. The device for resistive heating of the spin plate consists of two tires 10 and 11 that are attached to the conductors 12 located at opposite ends of the spin plate. The arrangement of the tires and the conductors is such that current flows along the spinneret plate in the direction shown by arrows in FIG. 3 and 4. Glass fibers drawn from the openings of the spin plate 3 are cooled by a gas flow directed by the nozzle 13 to the bottom surface of the filter plate. The gas (usually air) flows around the spin plate in the transverse direction, perpendicular to the direction of the current flowing through it in FIG. four). The nozzle 13 is located under the nozzle plate 3 at one of its lateral sides and is fixed on the bracket 14, which allows the nozzle to be adjusted to the lower surface of the nozzle plate. The nozzle plate 3 has ribs 15 with holes located across the plate (Fig. 4 ), and a perforated reinforcing sheet or grid 16, whose area is equal to the area of the working section of the spin plate, and this sheet is connected to the upper edges of the ribs and is parallel to the upper surface of the spin plate. The die plate, ribs and reinforcing mesh itself are made of the same material (for example, an alloy of 90% platinum and 10% of the rod) and form one piece. The sleeve 2 also has a lining 17 formed with it at the same time, located above the spinneret plate, and a reflector 18, which is attached to the cladding 17 and located across the inlet channel 19, through which glass melt flows inside the sleeve. Reflector-18 has a visor and directs the glass mass entering the sleeve to the sides of the spin plate. Holes are made in the reflector, which together with the mesh openings 16 hold solid particles (for example, refractory grains of sand or crystals from falling into the apertures of the Filler plate) Inlet channel 19 is lined from the inside with platinum foil 20, which covers not only the walls of the inlet channel 19, but also and its upper and lower parts (Fig. 4). The proposed spout plate is different in that its openings are grouped into pairs in pairs, and the openings belonging to the group are located in close proximity to the Friend, thanks to When the fiber coming out of one of these holes breaks, the glass from this hole flows and connects with the fiber coming out of the other hole before it reaches the other holes of the spinneret or before it cools so that it does not provide for its connection or If the fiber extends from another opening of this group, the spinning plate is also distinguished by the fact that the distance between the paired holes within the group, designated below as dimension a, is chosen large enough to allow the fibers s group from the pair of apertures, not spliced with each other during normal operation (specifically, during normal gas flow rate). The size a, shown in FIG. 2, characterizes not only the main variant of the proposed construction, but also three additional variants, (figs) and and; ep epc between the centers of a pair of holes combined into a group. The drawings show another series of characteristic sizes. The size b is equal to the distance between the centers of adjacent holes of two groups located in the same row in the direction of the current flowing through the spunbond plate. The size с is equal to the distance between the axes of the holes located in adjacent rows, i.e. in the direction of the gas movement and the direction perpendicular to the direction of flow through the current die plate. Dimension d is equal to the diameter of the holes of the spin plate. The size e is equal to the distance between the centers of the extreme holes of the adjacent enlarged groups. This size does not characterize the device of the spin plate, in which the holes are not joined into larger groups, such as, for example, a spin plate with equally spaced holes (Fig. 7). Size b is made large in size a so that when the fiber breaks, the fiber drawn from one of the holes of the glass mass left in this hole flows into the adjacent pair hole and connects to the fiber being pulled out of it a number of holes in which the breakage occurred. On the other hand, size b is chosen large enough to increase the density of the holes in the spinneret plate. The role played by dimensions a and b can best be understood with reference to fig. 2, which shows a cross section of a row of holes located in the direction of the current flowing through the spinnelate plate, and in particular, paired holes of one group 0-1 and 0-2 and hole 0-3 of the next group are shown. FIG. 2a, the filler plate at the moment of breakage of the fiber pulled out of the holes 0-1, when on the lower surface of the filter plate in the area of this hole an influx of glass melt forms that does not reach the adjacent holes. On -fig. Figure 2b shows the spinneret at that moment when the glass melt from the 0-1 hole to the stigl fiber drawn from the 0-2 hole. Obviously, due to the size difference a and b, the glass mass flowing out of the hole 0-1 will reach hole 0-2 before it reaches no hole 0-3. FIG. 2c, it is shown that the next time the glass mass flowing out of the holes 0-1 completely connects with the fiber drawn from the hole 0-2, resulting in a thickening of the fiber in place of its exit from the holes 0-1 and 0-2 , since both of these holes - will feed this fiberglass thread with glass. At this time, the distance between the fibers drawn from the openings 0-2 and 0-3 will be slightly different than at the moment corresponding to the state of the spin plate shown in FIG. 2b. FIG. Figures 2d and e show how the separation of a single flattened thread drawn from the openings 0-1 and 0-2 (Fig. 2c) into two separate threads fed by glass entering the openings 0-1 and 0-2. FIG. Figure 2 shows the moment of final self-correcting of the die and its normal operation with the extraction of the corresponding single thread from each hole. ideally, the self-correcting process (FIG. 2a) occurs automatically without operator intervention. However, in practice, especially in the case when the operator wants to speed up the self-correcting process of the die plate, he can always do this manually using an air stream to separate the fibers (Fig. 2d, e,). With automatic air supply, it is also possible to speed up the process of self-correcting the spinneret (fiber separation). The size c is chosen larger than the size b, since the section of the spinneret between the holes in the direction of the size c heats up to a greater degree and, consequently, is also more prone to choking than in the direction of size b. This is due to the increased current density flowing through the die in the c direction, and less gas flow in the b direction. The current density is measured in a direction perpendicular to the direction of dimension c, and the gas flow is measured in a direction perpendicular to the direction of dimension b. The relatively large distance between the enlarged groups of paired holes (size e) makes it possible to have on the surface of the spinneret separate clean glass areas not flooded with glass, which creates special advantages when the installation is started and when the relatively loose fibers break relatively thick fibers. Groups of paired holes also contribute to the cleaning of the die plate, as they allow the formation of thickened filaments fed by glass from two or three holes of the group (Fig. 2c). Variants of a die plate with two holes per group are shown in FIG. 5-7, and a variant of the nozzle plate with three holes in the group is shown in. FIG. 8. The advantages of the proposed die can be assessed by considering all the operating conditions of the installation for drawing fiberglass. When the installation is started, the invention allows the operator to properly clean the filler plate. The start of the installation consists in performing the following operations. 1. At the beginning, the die plate is filled with glass melt, which is to cover its surface. 2. The operator separates the glass mass layer into a series of areas separated from each other by free areas of equal size E. 3. The operator separates the areas filled with glass mass into fibers. The same operations are performed when the die is corrected, moreover, this work depends on the extent to which the floater plate was flooded. During normal operation of the installation, when a thread breaks down, usually a complete correction of the filter plate occurs without operator intervention (Fig. 2). If, for any reason, this does not happen, a partial self-correction of the filler plate (Fig. 2c7, accompanied by the formation of fibers) will still occur. The sizes of the holes of the fan plate and the distance between them are determined by the specific conditions of operation of the installation. Tables 1-3 give specific values of NIN indications above dimensions (dimensions in mm with an accuracy of one hundredth) for three different installation modes. In the first version (Figs. 5 and 6), verstily form rhomboid groups, each of which consists of several There are holes in each row with at least two paired holes in each row. In this embodiment, the groups of holes forming one row consist of two holes Restricted with 1 dash-dotted lines in Fig. 5, sections of the Fillier plate form segments similar to the segments shown in Fig. 4. The spinner plate consists of several such segments, the distance between them is larger than the size e. It is preferable to place the stiffening ribs 15 of the blade plate between the segments. In the embodiment shown in FIG. 7 each group of holes of the row also consists of two holes. The distance between these groups is b, and the distance between the rows is c. However, this option is not split. holes for groups that are spaced apart from each other. If desired, this can be done easily by joining the holes into rectangular groups and placing them a distance from each other. In the embodiment shown in FIG. 9, the individual groups of holes are formed by three holes and are located in rows that are spaced apart from each other by a distance c (the distance between the groups of holes within the row is equal to b). The distance between the holes. each group is equal to a. The portion of the filler plate bounded in FIG. 8 dash-dotted line forms one of the sections of the film; Serial plate. The mutual arrangement of these sections is shown in FIG. 9, and as can be seen from this figure, between each pair of reinforcing ribs 15 there are six shown in FIG. 8 sections. The wettability between the spinneret and the molten glass is such that the equilibrium contact angle is in the range of 30-40. This angle is equal to the angle between the lower plane of the die and the tangent to a drop of liquid glass that forms on the lower surface of the fan-plate when choking one of its holes. Complete wetting occurs when the contact angle is zero, and the lack of wetting means that this angle exceeds 90. In FIG. 10 shows the temperature dependence of the equilibrium contact angle for type E glass and a fan plate made of an alloy plate (90%) and rhodium (10%). The cross sections show wetting angles equal to 30 and b o, respectively. From the above graph, it can be seen that the maximum wettability takes place at lOSO-llSO C. It is at these temperatures, as well as at temperatures up to 1300 ° C, that fiberglass is usually drawn. Productivity is 0,2-0,3 g / a hole / min.
    Table 1
    1.12 1.22 1.32 1.42 1.45 1.55 1.55 1.65. 1.22 1.32 1.42 1.52 1.57 1.68 1.68 1.78
    1.27 1.40 1.50 1.60 1.65 1.75 1.75 1.88 Capacity 0.3-0.5 g / hole / min Capacity 0.5-0.7 g / hole / min
    1,982,132,182,342,342,46
    1, .781.98
    2,062,212,292,412,412,46
    1,852.06
    2,132,292,362,512,512,64
    1,912,13
    2,212,362,442,592,592,74
    1,982.21
    权利要求:
    Claims (4)
    [1]
    1. A filler plate for drawing glass fiber, including a perforated plate, the openings of which are grouped, and a current lead, which is different from that, c. In order to increase the efficiency of drawing, the groups include no more than three holes of the same diameter.
    with a distance between their centers of 1.20-1.45 diameter, with the distance between the centers of the extreme holes of adjacent groups being 1.41, 55 of the diameter of the holes.
    [2]
    2. A plate according to claim 1, characterized in that the number of holes in each group is 3, and their centers are located in the balance of an isosceles triangle.
    ., -.-., -
    table 2
    Table 3
    [3]
    3. A plate according to claim 1, characterized in that the groups are arranged in parallel rows, the distance between the extreme holes of the adjacent rows being greater than the distance between the extreme holes of the adjacent groups within the rows. /
    [4]
    4. The plate according to claim 3, is distinguished by the fact that the holes X1 of the XD row have the same diameter, and the distance between the extreme holes of the adjacent rows is 1.555. 1.70 in diameter.
    Sources of information taken into account in the examination
    1. USSR author's certificate 0 tf 419485, cl. From 03 to 37/08, 1972 (prototype).
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    类似技术:
    公开号 | 公开日 | 专利标题
    SU948287A3|1982-07-30|Die plate for drawing glass fiber
    US2335135A|1943-11-23|Manufacture of fibrous glass
    US4033742A|1977-07-05|Method for producing glass fibers
    SE437371B|1985-02-25|PROCEDURE AND DEVICE FOR MOLDING GLASS FIBER
    US3150946A|1964-09-29|Method and apparatus for production of glass fibers
    KR900004380B1|1990-06-23|Method and apparatus for forming glass fibers
    US2706365A|1955-04-19|Feeder for molten thermoplastic material
    US4469499A|1984-09-04|Method and apparatus for the manufacture of fibers
    US4363645A|1982-12-14|Annular bushing for forming glass fibers
    US4391618A|1983-07-05|Process and apparatus for the manufacture of fibers
    US4032314A|1977-06-28|Apparatus for controlling flooding in the drawing of glass fibers
    RU2373159C2|2009-11-20|Draw plate for making fibre, specifically glass fibre and fibre-forming device
    US3345147A|1967-10-03|Method for production of glass fibers
    GB2102787A|1983-02-09|Glass fibre drawing process and apparatus
    JPH068186B2|1994-02-02|Method and bushing for the production of glass fibers
    US3256078A|1966-06-14|Method and apparatus for forming fibers
    DE2735202A1|1978-03-02|METHOD AND APPARATUS FOR MANUFACTURING FIBERGLASS USING A DEFLECTIVE AIR CURTAIN
    US4401451A|1983-08-30|Process and apparatus for the manufacture of discontinuous glass fibers
    US2775850A|1957-01-01|Apparatus for forming mineral fibers
    SU867294A3|1981-09-23|Drawing plate method of producing methyltertiry butyl ether
    SU998399A1|1983-02-23|Apparatus for making fibers from thermoplastic material
    US3309184A|1967-03-14|Method and apparatus for flowing streams of heat-softened material from a supply
    US4202680A|1980-05-13|Fluid flow apparatus in combination with glass fiber forming apparatus
    US3207587A|1965-09-21|Method and apparatus for producing fibers
    KR810000849B1|1981-08-10|Orifice plate for use in glass fiber spinning hearth
    同族专利:
    公开号 | 公开日
    US3982915A|1976-09-28|
    AU499888B1|1979-05-03|
    GB1546204A|1979-05-23|
    FR2334637B1|1981-06-19|
    BE845226A|1976-12-16|
    NL7608882A|1977-06-10|
    SE419437B|1981-08-03|
    LU76114A1|1977-06-08|
    CA1081956A|1980-07-22|
    DE2636998B2|1979-01-25|
    NL165439B|1980-11-17|
    BR7604549A|1978-01-31|
    ZA764415B|1977-07-27|
    DE2636998A1|1977-10-27|
    AU1688476A|1978-02-23|
    NL165439C|1981-04-15|
    JPS5438219B2|1979-11-20|
    FR2334637A1|1977-07-08|
    SE7608701L|1977-06-09|
    JPS5274028A|1977-06-21|
    DE2636998C3|1979-09-13|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3475147A|1966-06-16|1969-10-28|Owens Corning Fiberglass Corp|Method and apparatus for processing heat-softened material|
    US3574581A|1968-09-13|1971-04-13|Ppg Industries Inc|Bushing for use in extruding fibers|
    BE759554A|1969-11-28|1971-05-27|Owens Corning Fiberglass Corp|APPARATUS FOR FORMING GLASS FIBERS AND METHOD FOR MAKING SUCH AN APPARATUS|
    US3920430A|1973-10-09|1975-11-18|Owens Corning Fiberglass Corp|Support for bushing for containing molten mineral material|
    DE2420650A1|1974-01-14|1975-07-24|Edward Thomas Strickland|METHOD AND DEVICE FOR MANUFACTURING FIBER GLASS FIBER|JPS5439499B2|1976-08-20|1979-11-28|
    US4283364A|1977-05-04|1981-08-11|Akzona Incorporated|Melt spinning of synthetic yarns|
    US4141709A|1978-03-14|1979-02-27|Ppg Industries, Inc.|Bushing environmental control|
    US4161396A|1978-03-17|1979-07-17|Owens-Corning Fiberglas Corporation|Method and apparatus for processing heat-softened fiber-forming material|
    US4194895A|1978-08-03|1980-03-25|Owens-Corning Fiberglas Corporation|Fluid flow method and apparatus used in manufacture of glass fibers|
    US4202680A|1978-10-16|1980-05-13|Owens-Corning Fiberglas Corporation|Fluid flow apparatus in combination with glass fiber forming apparatus|
    US4469499A|1979-11-20|1984-09-04|Societe Vetrotex Saint-Gobain|Method and apparatus for the manufacture of fibers|
    FR2470098A1|1979-11-20|1981-05-29|Saint Gobain Vetrotex|METHOD AND APPARATUS FOR THE MANUFACTURE OF GLASS FIBERS|
    US4398933A|1979-11-20|1983-08-16|Societe Vetrotex Saint-Gobain|Method and apparatus for the manufacture of fibers|
    US4437869A|1979-11-20|1984-03-20|Societe Vetrotex Saint-Gobain|Method and apparatus for multifilament glass strand|
    JP2534090B2|1988-02-12|1996-09-11|旭ファイバーグラス株式会社|How to restart work when filament is cut|
    US5219585A|1990-02-23|1993-06-15|Basf Corporation|Monomer exhaust system|
    DE19638056C2|1996-09-18|2000-07-13|Bayer Ag|Glass fiber spinning device|
    US20030221462A1|2002-05-31|2003-12-04|Sullivan Timothy A.|Fiber forming bushing assembly having flange support|
    FR2850964B1|2003-02-12|2006-06-02|Saint Gobain Vetrotex|REINFORCING DEVICE FOR A CHAIN DELIVERING FILAMENTS IN PARTICULAR GLASS|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/638,526|US3982915A|1975-12-08|1975-12-08|Apparatus and method for controlling flooding in the drawing of glass fibers|
    AU33729/78A|AU499888B1|1975-12-08|1978-03-01|Controlling flooding inthe drawing of glass fibers|
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