• 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 apparatus for radially quenching melt spun filaments features a quenching chamber having a foraminous distribution cylinder between the filaments and the gas supply chamber with areas of decreasing porosity from a location immediately below the spinneret toward the exit of the quench chamber.
    公开号:SU1748653A3
    申请号:SU874203827
    申请日:1987-12-14
    公开日:1992-07-15
    发明作者:Раст Броддас Кларк；Джей Голлхардт Брэдли
    申请人:Е.И.Дюпон Де Немур Энд Компани (Фирма)；
    IPC主号:
    专利说明:

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    The invention relates to melt-spun synthetic yarns, in particular to devices for radial cooling of the yarns.
    A device and method for melt-forming synthetic filaments and cooling these filaments is known by continuously supplying a flow of cooling gas at a constant speed radially inward from all directions to the filaments through a cylindrical perforated hollow element surrounding the filaments. Such radial cooling systems provide a radial flow constant velocities from above (approximately from the die) to the exit from the cooling chamber,
    When higher performance was achieved with the use of a radial cooling system, and especially when producing yarns with pores, a deterioration in yarn quality, porosity and uniformity due to inadequate cooling of the yarns was found.
    The purpose of the invention is to increase the performance properties by improving the gas distribution conditions.
    Figure 1 shows the proposed device, the cut; figure 2 - cooling distribution element; in FIG. 3, a cooling chamber.
    The device comprises a spinneret 10 through which the strands 12 are extruded, then guided through a hollow cylindrical cooling chamber 14 to a guide device (not shown) that forms part of a typical feeding system. A hollow cooling chamber 14 is mounted immediately below the die. The chamber 14 is provided with a lower annular chamber 18 with a nozzle 20 for supplying cooling gas 21, as well as an upper annular chamber 22 for distributing the cooling gas into the inner chamber 24 to the threads 12. The chambers 18, 22 are separated by a perforated plate 26 entering the chamber 22. The inner wall 23 of the chamber 22 is made of a cylindrical perforated material, for example of a cylindrical metal plate having openings 28 of varying diameter to obtain regions of decreasing Porosity, starting directly below the die 10 and further in the direction of the exit end of the cylindrical plate 23. In addition, there is a coating 30 of foam material for dispersing the air flow.
    In operation, gas 21 enters chamber 18 through nozzle 20, then passes through
    distribution plate 26 into the chamber 22. After that, the gas passes through the perforated cylinder 23 and comes into contact with the filaments (figures 1 and 2), and the profile
    the speed reduction is shown in FIG. 3, where the length of the arrows 21 corresponds to the speed, Test methods.
    The relative viscosity of the solution (LRV). The relative viscosity of the solution is the ratio of the flow time of the solution and the solvent in a capillary viscometer at 25 ° C. The solution consisted of 4.75 wt.% Polymer in a solvent. The solvent was hexafluoroisopropanol with
    content of 100 parts per million H2S04.
    Determination of porosity in percent. Porosity in percent is usually determined by measuring flotation density as follows.
    A variety of solutions are obtained.
    density by combining appropriate amounts of CCU with a density of 1.60 g / cm and n-heptane with a density of 0.684 g / cm3. The density of these solutions can be accurately determined by measuring it with a hydrometer. The solutions are then set in the order of increasing density. The apparent density of the hollow fiber is determined as follows: a small piece of fiber (100-150 mm) is cut off, a very tight knot is tied from it and immersed in turn in each of the solutions in order to determine in which solution the fiber barely floats and in which it barely sinks. The average of the two densities obtained is the apparent fiber density. Then the porosity for the formed or melted fiber is:
    For molded fiber, the porosity is 1,345 - apparent with a dense.
    1,345
    -x 100%;
    for drawn carbon fiber porosity
     1.39 - apparent density, pppo / 100 / ,,
    where 1,345 - the density of the polymer in no coiled (amorphous) polyester fiber;
    1,39 - the density of the polymer in the tatted (crystalline) polyester fiber.
    PRI me R 1. The apparatus used is a typical melt molding apparatus, where the molten polymer is fed into a molding unit equipped with a gear pump,
    filter and a set of dies. The extruded yarns pass through the device shown in Fig. 1, and the cooled yarns are unwound or bundled and fed into a collection assembly of a typical design.
    A 5.5-inch die contains 212 capillaries arranged in four concentric circles with an outer circle diameter of 4.5 inches.
    The inner wall 23 (Fig. 1) of the cooling unit is a cylinder of 7 inches in diameter, containing equally spaced 24 horizontal rows of 117 holes each. Eight rows of spinnerets have an orifice diameter of 0.076 inch, average 8. The rows have a hole diameter of 0.067 inches and the 8 farthest from the spinneret rows have a hole diameter of 0.055 inches.
    Polyethylene terephthalate with a relative viscosity of a solution of 20.4 molding from a solution at a molding block temperature of 270 ° C was cooled and coiled at a speed of 700 rds per minute to obtain yarn consisting of porous filaments having four continuous non-circular parallel pores throughout length. The fiber weight number (denier) was 45. The resulting yarn sample was encoded with A2.
    The experiment was repeated under the same conditions on the same apparatus, except that the size of the holes in the inner perforated wall 23 of the cooling unit was the same. The total air flow was adjusted so that it was equal to the value used in the manufacture of A2 yarn. The resulting control yarn of porous fibers was designated A1.
    Then the porosity was measured in percent of samples A1 and A2. The porosity of sample A1 is 20.5, while the porosity of sample A2 is 25.9. It is obvious that the use of the proposed device provided an increase in porosity by 26.3%.
    At the same time, a visual study of the micrographs of the cross section of the obtained yarn types showed a significant improvement in the uniformity of yarn A2.
    EXAMPLE 2 The procedure of example 1 was repeated, with the exception that a die was used with 388 capillaries located in five concentric circles, and the winding speed was 1205 rds per minute. The cooling device was similar to that used in the preparation of sample A2. The yarn produced consists of yarns with a weight number of freshly formed fiber 14.5 and was designated B2,
    The control yarn was obtained under the same conditions and on the same equipment as the yarn B2, except for the fact that the cooling unit was similar to the one used to obtain the control yarn A1.
    Measurement of the porosity of two hollow fibers showed that the control yarn 5 B1 yarns have a porosity of 16.4, while the B2 yarn has a porosity of 23.8. Thus, the use of the device provided an increase in closed porosity by 45.1%. PRI me R 3. Polyethylene terephthalate with
    0 - relative viscosity 20.4 was molded from the melt at a block temperature of 275 ° C using a spinneret having 900 round holes arranged with eight concentric circles, with the diameter
    5 outer circle was about 4.5 inches. The extruded filaments were cooled in air in a radial cooling unit and then coiled at a speed of 1624 rds per minute to obtain the equilibrium
    0 where the threads had a weight number of 3.6.
    The control yarn was obtained by the same procedure using a typical radial cooling unit, where the size of all holes in the inner radial
    5, wall 23 (FIG. 1) is the same. Test yarns were obtained using a radial cooling unit, similar to the unit used to obtain sample A2 from example 1, i.e. in the inner wall 23
    There were larger openings around the cooling block near the spinneret. The total air flow was the same for both types of yarn.
    Samples test and control
    Five yarns were cut across, mounted in a microscope, and the image in the microscope was designed on a large screen. For each sample, the diameter of each of the 360 threads designed
    0 images, the result was recorded and the mean and standard deviation were calculated. It turned out that the control sample had an average filament diameter of 19.5 μm with a standard deviation of 1.852, whereas the test sample had an average filament diameter of 19.5 μm and a standard deviation of 1.037 A comparison of standard deviations indicates an improvement in the diameter uniformity of more than 40% for test yarn.
    权利要求:
    Claims (1)
    [1]
    The invention of the device for forming from a polymer melt, containing a die plate, cooling chamber having a hollow cylindrical perforated element placed directly under the die plate, and a chamber with inlet ventilation, having a gas supply nozzle, characterized in that properties by improving the gas distribution conditions, the hole in the perforated IMRUT element
    gv / s
    diameter decreasing in direction from die to exit from cooling chamber
    gz
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    同族专利:
    公开号 | 公开日
    YU224687A|1989-02-28|
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    US4712988A|1987-12-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2252684A|1938-08-09|1941-08-19|Du Pont|Apparatus for the production of artificial structures|
    US3070839A|1958-12-24|1963-01-01|Du Pont|Controlled quenching apparatus|
    US3067458A|1959-04-07|1962-12-11|Du Pont|Melt spinning apparatus and process|
    US3061874A|1960-11-23|1962-11-06|Du Pont|Melt spinning apparatus|
    US3274644A|1964-04-27|1966-09-27|Du Pont|Adjustable profile chimney|
    US3299469A|1964-11-18|1967-01-24|Du Pont|Melt-spinning apparatus|
    GB1150590A|1966-10-28|1969-04-30|Vnii Mash Dlya Proizv Sint Vol|Apparatus for Filament Cooling|
    US3745061A|1969-02-26|1973-07-10|Du Pont|Synthetic filaments having at least three continuous nonround voids|
    US3632719A|1969-03-08|1972-01-04|Teijin Ltd|Process and apparatus for melt-spinning of polyamide|
    US3834847A|1970-01-16|1974-09-10|Du Pont|Open cell foam device for gas distribution in filament quenching chimneys|
    JPS5317717B2|1975-07-21|1978-06-10|
    US3999910A|1975-10-08|1976-12-28|Allied Chemical Corporation|Filament quenching apparatus|
    US4444710A|1982-02-19|1984-04-24|E. I. Du Pont De Nemours And Company|Process for increasing void volume of hollow filaments|
    US4492557A|1983-07-19|1985-01-08|Allied Corporation|Filament quenching apparatus|
    US4631018A|1984-11-01|1986-12-23|E. I. Du Pont De Nemours And Company|Plate, foam and screen filament quenching apparatus|
    JPH0753924B2|1985-01-22|1995-06-07|旭化成工業株式会社|Cooling tube for melt spinning of synthetic fibers|DE4038447A1|1990-12-03|1992-06-11|Air Prod Gmbh|Contactless cooling of extruded plastic section - uses very low temp. gas with liq. nitrogen@ injection to maintain temp. independently of throughput|
    US5178814A|1991-08-09|1993-01-12|The Bouligny Company|Quenching method and apparatus|
    AT131224T|1991-09-06|1995-12-15|Akzo Nobel Nv|DEVICE FOR THE QUICK SPINNING OF MULTIFILE THREADS AND THE USE THEREOF.|
    BR9400682A|1993-03-05|1994-10-18|Akzo Nv|Apparatus for the fusing spinning of multifilament yarns and their application|
    US5219582A|1991-12-06|1993-06-15|E. I. Du Pont De Nemours And Company|Apparatus for quenching melt spun filaments|
    US5219506A|1991-12-06|1993-06-15|E. I. Du Pont De Nemours And Company|Preparing fine denier staple fibers|
    ATA53792A|1992-03-17|1995-02-15|Chemiefaser Lenzing Ag|METHOD FOR PRODUCING CELLULOSIC MOLDED BODIES, DEVICE FOR IMPLEMENTING THE METHOD AND USE OF A SPINNING DEVICE|
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    JP2002309431A|2000-06-21|2002-10-23|Toray Eng Co Ltd|Spinning apparatus|
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    US20050184429A1|2002-11-09|2005-08-25|Saurer Gmbh & Co. Kg|Method and apparatus for melt spinning and cooling a plurality of synthetic filaments|
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    US7037097B2|2003-05-20|2006-05-02|Hills, Inc.|Methods and apparatus for controlling airflow in a fiber extrusion system|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US07/020,019|US4712988A|1987-02-27|1987-02-27|Apparatus for quenching melt sprun filaments|
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