• 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:
    Disclosed is an orifice plate for use in a bushing for spinning glass fibers having a number of orifices each of which consists of two cascaded coaxial cylindrical bores of different diameters, one of which opens in the upper surface of the orifice plate to constitute a molten-glass inlet-side bore, while the other opens in the lower surface of the orifice plate to constitute a molten-glass outlet-side bore.
    公开号:SU867294A3
    申请号:SU772512202
    申请日:1977-08-18
    公开日:1981-09-23
    发明作者:Соно Хироаки；Нодзи Тосио；Исикава Синзо；Вакаса Исао
    申请人:Нитто Босекико Лтд (Фирма)；
    IPC主号:
    专利说明:

    (54) FILTER PLATE The invention relates to the building materials industry, in particular to the equipment of glass fiber factories. A known perforated plate for drawing glass yarns, each channel of which is made of inlet and outlet sequence and coaxially arranged cylindrical channels 1. However, the threads pulled out of glass passing through the channels to the outermost portions of the perforated plate that are more often torn compared to threads drawn from glass that passes through the channels located inward from the outer channels. Thus, the stretching is often interrupted due to thread breaks on the outermost channels, occurring two or three minutes after the start; stretching. This is due to the fact that the threads obtained on the peripheral channels have a smaller diameter than the threads received from the remaining channels, and,. therefore, the more likely they are to break. . The purpose of the invention is to obtain a diameter of the same diameter and a decrease in the probability of their breakage. The goal is achieved by the fact that in a spunbond plate for drawing glass yarns made with a plurality of coaxially and successively arranged cylindrical inlet and outlet channels, the diameter of the inlet channels being larger than the diameter of the outlet, the diameter and / or height of the inlet channels located along the perimeter of the spinnerette plates, exceeds the diameter and / or height of the remaining inlet channels by an amount determined by the formula .5Tru-0, ebrui where TS and f, / are variables, defined in с; according to the dimensions of the inlet channels, set along the perimeter, and the rest, respectively, and setting c. by the following equations: c. l -ty- 1, U / () tq: u fu-- - - - r / de. X and x are the diameters of the inlet channels, respectively, located along the perimeter and the rest; LX x the lengths of the inlet ducts, respectively, located along the perimeter and the remaining y are the diameter of the outlet ducts, respectively, located along the perimeter and the rest; L and L t are the axial lengths of the exhaust channels, respectively located along the perimeter, and the rest; I is the angle at which the conical intermediate part, through which the coaxial and successive cylindrical channels interconnect, intersects the plane parallel to the spin plate. . Figure 1 shows a slurry layer with a different diameter of inlet channels, a longitudinal section; 2, a die plate with different heights of the inlet channels along the periphery and the rest, is a longitudinal section. Spunner plate contains channels 1 and 1 each of which consists of two sequentially and coaxially arranged cylindrical channels, with the diameter of the inlet channels greater than the diameter of the outlet, connected to each other by a conical intermediate part. The channels (external) 1 and the other channels (internal) 1, located along the perimeter of the die plate, have the same diameter y from the outlet side of the molten glass. The heights L and Lxji of the outer and inner channels 1 and 1 on the exhaust side are the same. In addition, the distance between the adjacent walls of the inner channels on the exhaust side and the distance between the adjacent walls of the outer and inner channels on the outlet side are chosen equal and equal to c. In order to reduce the resistance of the melt glass that the stream undergoes through the external channels, the diameter x of the external channels on the inlet side is chosen larger than the diameter x of the internal channels, then & as the axial lengths of b and in external and. The inner channels on the inlet side are the same. Moreover, not only the outlet parts of the outer and inner channels 1 and l can have the same diameter i, but also the liner diameters of the inlet parts of both holes 1 and 1 can be the same, while the axial length L of the outer channels 1 on the inlet side can be selected longer than the axial length of the C | internal channels l, as a result of which the outlet parts of the external channels 1 may have an axial length Ly, which is smaller than the Lyt exhaust parts of the internal channels l (Fig. 2). There is less friction resistance in the external channels than in internal channels. A similar condition can be obtained by appropriately combining the structures shown in Figures 1 and 2. Thus, the flow rate of molten glass passing through the external channels becomes greater than that through the internal channels, resulting in less friction resistance. Therefore, the increment of the flow rate of the molten glass is. La through external channels compensates for a greater ratio of heat radiation to heat absorption on external channels than on internal ones, thus guaranteeing us the same to obtain glass cones on external channels of the same size as on internal ones. The best results are obtained when there is a relationship between the external and internal channels, which can be represented by the equality: HgGi-o.Gy where fg is variable, which is determined according to the dimensions of the two cylindrical channels of the outer channel; variable, which is determined by the dimensions of the two cylindrical channels of the internal channel. In particular, y and 1f are transient, which satisfy the following equations, respectively:. () tcy9, -. and 4. V (3 Friction resistance, which the flow of molten glass encounters when passing; the gap through the holes increases when these variables and 1l become larger, causing the flow rate to decrease, and vice versa, the resistance to friction decreases, providing a greater flow rate if these variables are smaller. With 8bTi, the feed rate of the molten glass to the outer channels becomes insufficiently thick, with the result that cones of smaller exchanges form on the outer channels than on the inner channels, and consequently, there is a danger of breaking the yarn on external channels.
    At Tg 0, LT and the flow rate of molten glass through the outer channels becomes excessively large, which leads to the connection of the glass cones formed on the outer channels with the cones of the inner channels.
    The perforated plate contains a large number of channels made in small steps, i.e. with a high density, which can lead to a combination of glass cones if appropriate counter measures are not taken. Although the pitch cannot be simply set, it depends on many factors (the amount of molten glass in the EXTRACT field, the composition of the glass, the melting point of the glass, the drawing temperature, the shape of the channels, the drawing speed, the flow rate of the cooling air supplied to perforated plate cooling air velocity, etc.), however, it does not exceed 2.0 mm if measured over a smaller distance between adjacent walls of adjacent channels.
    Assuming that the distance between the more closely spaced walls of adjacent channels is 1.0 mm, the perforated plate provides glass cones on the outer channels, which are the same size as the cones on the inner channels. In addition, since any of the adjacent channels is located with a constant pitch, the possibility of mutual contact of glass cones
    becomes the same throughout the perforated plate, as a result of which sustained continuous stretching can be carried out without merging the glass cones.
    The nozzle can be equipped with a round perforated plate; in this case, the channels can be arranged in the form of several concentric circles on a round perforated plate.
    Example 1. Perforated; the plate was made in accordance with the conditions given in Table 1.
    Table 1
    15
    Indicator
    Value
    Perforated size
    250x46x2 plates, mm
    Material perforated iii OPt + 20Rh Noah plate 2008
    Number of channels
    The distance between neighboring centers
    1.90 channels, mm
    Productivity, 800-1000 g / min
    Drawing speed
    300-1000 m / min
    Table 2 presents the characteristics of 35. tiki internal and external channels.
    I
    .Table 2
    . 1.50
    1.34
    1, OO
    0.51
    o30 x 0.67 0.842
    1.70 1.34
    1.00 0.46
    thirty.
    0.59
    0.90
    0.697
    The ratio of variables is "0.83.
    "U
    A perforated plate was made as a reference one in accordance with the same conditions, but the external and internal channels have the same shape and size as in the conventional design.
    The results of experiments comparing the frequency of thread breakage on the outer holes are given in Table 3.
    Table 3
    Inlet diameters
    channels, mm
    The height of the inlet parts of the channels, mm
    The diameters of the exhaust channels, mm
    The height of the exhaust channels, mm
    The angle at which the conical intermediate part of the channel intersects the plane of the perforated plate, ®
    The ratio of the diameters of the inlet and exhaust parts of the channels
    The distance between the walls of adjacent channels, on the outlet side,
    mm:
    Variable Channel
    Example 2. A perforated plate was made in accordance with the conditions given in Table 4.
    Table 4
    Indicator
    Value
    Perforated size
    plates, mm380 x 52 x 2
    Perforated material
    90Pt + 5Au + 5Pd plate 4000
    Number of channels
    Distance between centers of adjacent channels, mm
    Productivity, g / min
    Drawing speed
    m / min
    25 Table 5 presents the characteristics of internal and external channels.
    Table 5
    1.40 1.60
    0.99 1.33).
    1,100 IjlO 0.92 0.50
    thirty
    thirty
    0.79 0.69
    权利要求:
    Claims (1)
    [1]
    0.75 0.923 0.554 Ratio of variables 0.60. For comparison, a different perforated plate is made in accordance with the same conditions, but in which the external and internal channels have the same shape and size as in a conventional construction. Test results comparing the frequency of thread breaks on both plates and external channels are given in Hubd.6. Table Known Proposed 600 900 The invention significantly reduces the frequency of thread breaks on external channels compared to known designs, thereby guaranteeing a more stable draw and continuous work Claim of the invention Spunner plastics for stretched glass filaments, made with a set of coaxially and sequentially arranged cylindrical inlet and outlet channels, the diameter of the inlet channels being larger than the diameter of the outlet channels, in order to ensure that the threads of the same diameter and reduce their breakage, the diameter and / or height of the inlet channels, is spaced by 10 2 5 with a sieve plate, a meter and / or the height of the axial channels by the value, according to the formula. jlc - 0.86 variables and variables, determined in accordance with the size of the inlet ducts; located along the perimeter, and the others, respectively, and given by the following equations:. ailbl if "4 fexS dippers of inlet channels, respectively located along the perimeter, and the rest; axial lengths of inlet channels, respectively located along the perimeter, and the rest; the diameter of the outlet channels, respectively located along the perimeter, and the rest; axial lengths of exhaust channels, respectively located along the perimeter, and the rest. the angle at which the conic intermediate part, through which the coaxial and successively arranged cylindrical channels interconnect, intersects the plane adjacent to the draw plate. Information officers, understanding during the examination of the USA 3905790, kl.65-2,
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    同族专利:
    公开号 | 公开日
    ES461709A1|1978-05-16|
    PT66943A|1977-09-01|
    NZ184814A|1980-05-08|
    ZA774708B|1978-06-28|
    AU499128B1|1979-04-05|
    CH621584A5|1981-02-13|
    US4119420A|1978-10-10|
    NL167138C|1981-11-16|
    IN147780B|1980-06-28|
    SE7709372L|1978-02-21|
    TR19433A|1979-03-19|
    BR7705521A|1978-07-04|
    DE2736475A1|1978-02-23|
    DE2736475C2|1982-04-01|
    MX143936A|1981-08-04|
    PT66943B|1979-02-07|
    CS207477B2|1981-07-31|
    NL167138B|1981-06-16|
    NL7709045A|1978-02-22|
    FR2362088A1|1978-03-17|
    FR2362088B1|1980-05-16|
    IT1082291B|1985-05-21|
    BE857953A|1977-12-16|
    JPS5324432A|1978-03-07|
    GB1574793A|1980-09-10|
    JPS5439499B2|1979-11-28|
    DK369777A|1978-02-21|
    SE423708B|1982-05-24|
    CA1095724A|1981-02-17|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2618245C1|2016-02-03|2017-05-03|Общество с ограниченной ответственностью "Технология и Оборудование для Стеклянных Структур"|Die for glass rod manufacture |US3468643A|1966-04-20|1969-09-23|Owens Corning Fiberglass Corp|Apparatus for feeding streams of heat-softened material|
    US3526487A|1967-03-01|1970-09-01|Ppg Industries Inc|Apparatus for producing fiber glass|
    US3514841A|1967-05-17|1970-06-02|Owens Corning Fiberglass Corp|Forming a tip section that feeds streams of heat-softened material|
    US3759680A|1970-09-14|1973-09-18|Owens Corning Fiberglass Corp|Method and apparatus for producing fibers from glass|
    JPS483857U|1971-05-26|1973-01-17|
    DE2420650A1|1974-01-14|1975-07-24|Edward Thomas Strickland|METHOD AND DEVICE FOR MANUFACTURING FIBER GLASS FIBER|
    JPS5729422B2|1974-07-09|1982-06-22|
    US3982915A|1975-12-08|1976-09-28|Coggin Jr Charles H|Apparatus and method for controlling flooding in the drawing of glass fibers|JPH02275729A|1989-04-14|1990-11-09|Nitto Boseki Co Ltd|Nozzle plate for glass fiber spinning|
    SG50447A1|1993-06-24|1998-07-20|Hercules Inc|Skin-core high thermal bond strength fiber on melt spin system|
    DE19638056C2|1996-09-18|2000-07-13|Bayer Ag|Glass fiber spinning device|
    AU4112001A|2000-03-14|2001-09-24|Nitto Boseki Co Lt D|Bushing and glass fiber producing method|
    US7018188B2|2003-04-08|2006-03-28|The Procter & Gamble Company|Apparatus for forming fibers|
    US20070144218A1|2005-12-28|2007-06-28|Oakleaf Anthony P|Longlife bushing tip|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    JP9942876A|JPS5439499B2|1976-08-20|1976-08-20|
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