WO2002063086A1 - Procédé et dispositif de fabrication de tissu non tissé - Google Patents
Procédé et dispositif de fabrication de tissu non tissé Download PDFInfo
- Publication number
- WO2002063086A1 WO2002063086A1 PCT/JP2002/000691 JP0200691W WO02063086A1 WO 2002063086 A1 WO2002063086 A1 WO 2002063086A1 JP 0200691 W JP0200691 W JP 0200691W WO 02063086 A1 WO02063086 A1 WO 02063086A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- nonwoven fabric
- web
- mesh conveyor
- producing
- heating chamber
- Prior art date
Links
Classifications
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
- D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
- D04H1/54—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by welding together the fibres, e.g. by partially melting or dissolving
Definitions
- the present invention relates to a method and an apparatus for continuously producing a nonwoven fabric of chemical fibers.
- a nonwoven fabric of chemical fibers is sometimes manufactured by heating a mixed aggregate (web) of low-melting fibers and high-melting fibers above the melting point of the low-melting fibers to bond the fibers together.
- a mixed web of low-melting fiber and high-melting fiber use an aggregate of chemical fibers with a core-sheath structure in which a low-melting resin layer is formed on the surface (periphery) of the core material of the high-melting fiber.
- An object of the present invention is to provide a method and an apparatus for continuously producing a nonwoven fabric having a desired density.
- the nonwoven fabric is produced by heating a web containing low-melting-point chemical fibers or a web containing chemical fibers having a low-melting-point surface layer, wherein the gap is conveyed and continuously passed through the heating chamber. Through which the nonwoven fabric is produced continuously.
- the apparatus for manufacturing a nonwoven fabric of the present invention includes a mesh conveyor for transporting a web containing low-melting chemical fibers or a web containing chemical fibers having a low-melting surface layer; a heating chamber provided on the way of transporting the mesh conveyor; Press the web coming out of the heating chamber And a roll for adjusting the thickness to a predetermined thickness.
- a nonwoven fabric is produced continuously without causing wrinkles in the web.
- the web coming out of the heating chamber is sandwiched between rolls and pressed to a predetermined thickness, whereby a nonwoven fabric having a desired density is continuously produced.
- the hot air is evenly applied to the web, thereby shortening the heating time and preventing the nonwoven product from being conveyed.
- FIG. 1 is a schematic cross-sectional view of a nonwoven fabric manufacturing apparatus according to an embodiment. Preferred embodiments of the invention
- FIG. 1 is a schematic longitudinal sectional view showing an example of a method and an apparatus for producing a nonwoven fabric according to an embodiment.
- the web is made of a mixed web of low-melting-point chemical fibers and high-melting-point chemical fibers, or a core-sheath type chemical fiber having a low-melting-point layer in the outer layer.
- the web is conveyed by being sandwiched between the lower first mesh conveyor 1 and the upper second mesh conveyor 2, and passes through the heating chamber 3.
- Reference numeral 4 denotes a height adjusting mechanism such as a screw jack for adjusting the vertical position of the second mesh conveyor 2.
- a hot air supply device (not shown) having an LPG combustor is connected to a lower portion of the heating chamber 3 so as to supply hot air at a predetermined temperature to a lower side of the mesh conveyor 1.
- an induction fan induction fan An
- the nonwoven fabric produced by heating fibers in the heating chamber 3 and bonding the fibers together is pressed from above and below by a press roll 8 when it comes out of the heating chamber 3 to have a predetermined thickness. Thereafter, the nonwoven fabric is sandwiched from above and below by the mesh conveyors 11 and 12 and introduced into the cooling device 10, for example, air at normal temperature is passed through the nonwoven fabric and cooled.
- Reference numeral 13 denotes a screw jack for adjusting the height of the mesh conveyor 12.
- the non-woven fabric is then sent out onto a receiving table 16 and cut into predetermined dimensions by a cutter 15.
- the nonwoven fabric can be continuously manufactured by continuously heating the web.
- the heat history can be made uniform by adjusting the distance between the mesh conveyors 2 and 1 so as to gradually decrease from the inlet side to the outlet side.
- the mesh conveyors 1 and 2 can pass hot air through the pipe significantly more uniformly than the punched iron plate. Also, since the eyes are fine, there is no mark on the non-woven fabric, and the texture on the upper and lower surfaces is good.
- the interval between the mesh conveyors 1 and 2 can be individually and freely adjusted within the range of 20 to 50 Omm on the entrance side and 5 to 10 Omm on the exit side.
- a mechanism shall be provided to move the second mesh conveyor 2 with the distance between the mesh conveyor 1 on the inlet side and the outlet side adjusted in parallel in the vertical direction as a whole (that is, while maintaining the same inclination angle). Is desirable.
- a heater may be used as the heat source, it is preferable to supply the heat source with an LPG parner because the heater may be burned in a low wind speed operation.
- the suction and suction by the exhaust fan 6 stabilize the supply and distribution of hot air.
- This hot air is preferably passed from bottom to top as shown in FIG.
- the thickness of the web is maintained, and the manufactured nonwoven can have a desired density.
- the web becomes thin before heat fusion due to the wind and its own weight, and the web may not be a desired density.
- the press roll 8 may be either a cooling roll or a roll with a heater, but is more preferably a cooling roll. It is preferable to provide an enclosure between the heating chamber 3 and the press roll 8 to prevent heat radiation from the nonwoven fabric. If the temperature of the nonwoven fabric decreases due to heat radiation from the nonwoven fabric, the pressing effect becomes poor, and it becomes difficult to adjust the thickness of the nonwoven fabric.
- the distance between the upper mesh conveyor 12 and the lower mesh conveyor 11 of the cooling device 10 is individually set at the inlet side and the outlet side. It is adjustable.
- the cooling device 10 may have a mechanism for vertically moving the upper mesh conveyor 12 in which the distances from the lower mesh conveyor 11 on the inlet side and the outlet side are adjusted as a whole.
- the cooling device 10 preferably has a mechanism for controlling the temperature of the cooling air.
- the blowing direction of the cooling air may be either from the upper or lower direction. However, when blowing from above, it is preferable to blow from below because there is a possibility that the thickness of the web may be reduced by wind pressure.
- the methods and apparatus of the present invention is suitable for you produce density 0. 01 ⁇ 0. 2 g / c Hi 3 of the nonwoven fabric.
- the velocity of the hot air passing through the web in the heating chamber 3 is preferably from 0.01 to 5 m / sec. Above 5mZs ec, the web may be wrinkled and It is also difficult to control the thickness of the cloth.
- the heating chamber 3 may be a two-chamber system including an upstream preheating chamber and a downstream heat fusion chamber.
- a baffle may be arranged in the heating chamber 3 so that the hot air can be distributed uniformly. Providing baffles enables high wind speed operation. In addition, the heat capacity increases, and the indoor temperature can be maintained at a high temperature.
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Nonwoven Fabrics (AREA)
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002562813A JP4320547B2 (ja) | 2001-02-06 | 2002-01-30 | 不織布の製造方法及び装置 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001-29862 | 2001-02-06 | ||
JP2001029862 | 2001-02-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002063086A1 true WO2002063086A1 (fr) | 2002-08-15 |
Family
ID=18894158
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2002/000691 WO2002063086A1 (fr) | 2001-02-06 | 2002-01-30 | Procédé et dispositif de fabrication de tissu non tissé |
Country Status (2)
Country | Link |
---|---|
JP (1) | JP4320547B2 (ja) |
WO (1) | WO2002063086A1 (ja) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101320797B1 (ko) | 2013-05-14 | 2013-10-23 | 박태근 | 폴리에스테르 고탄성 쿠션재 제조용 드라이 오븐 |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5748289U (ja) * | 1980-08-29 | 1982-03-18 | ||
JPS5795363A (en) * | 1980-12-04 | 1982-06-14 | Sumitomo Durez Co | Production of resin felt |
JPS5818463A (ja) * | 1982-04-12 | 1983-02-03 | 井上金属工業株式会社 | 不織布製造用の加熱成形装置 |
EP0133083A1 (fr) * | 1983-07-07 | 1985-02-13 | Isover Saint-Gobain | Formation de feutres à structure isotrope |
JPS6034660A (ja) * | 1983-07-29 | 1985-02-22 | 池田物産株式会社 | 短繊維フェルトの製造方法 |
JPH0782644A (ja) * | 1993-09-10 | 1995-03-28 | Kiyomine Taniguchi | ポリイミド繊維成形体の製造法 |
JPH09132851A (ja) * | 1995-10-27 | 1997-05-20 | Nippon Filcon Co Ltd | 不織布の形成方法および形成装置 |
JPH11200217A (ja) * | 1998-01-07 | 1999-07-27 | Japan Vilene Co Ltd | 不織布及びその製造方法 |
JP2001355168A (ja) * | 2000-04-13 | 2001-12-26 | Inoac Corp | 繊維集合体の成形方法、該方法によって成形された繊維集合体および前記繊維集合体の成形装置 |
-
2002
- 2002-01-30 WO PCT/JP2002/000691 patent/WO2002063086A1/ja active Application Filing
- 2002-01-30 JP JP2002562813A patent/JP4320547B2/ja not_active Expired - Fee Related
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5748289U (ja) * | 1980-08-29 | 1982-03-18 | ||
JPS5795363A (en) * | 1980-12-04 | 1982-06-14 | Sumitomo Durez Co | Production of resin felt |
JPS5818463A (ja) * | 1982-04-12 | 1983-02-03 | 井上金属工業株式会社 | 不織布製造用の加熱成形装置 |
EP0133083A1 (fr) * | 1983-07-07 | 1985-02-13 | Isover Saint-Gobain | Formation de feutres à structure isotrope |
JPS6034660A (ja) * | 1983-07-29 | 1985-02-22 | 池田物産株式会社 | 短繊維フェルトの製造方法 |
JPH0782644A (ja) * | 1993-09-10 | 1995-03-28 | Kiyomine Taniguchi | ポリイミド繊維成形体の製造法 |
JPH09132851A (ja) * | 1995-10-27 | 1997-05-20 | Nippon Filcon Co Ltd | 不織布の形成方法および形成装置 |
JPH11200217A (ja) * | 1998-01-07 | 1999-07-27 | Japan Vilene Co Ltd | 不織布及びその製造方法 |
JP2001355168A (ja) * | 2000-04-13 | 2001-12-26 | Inoac Corp | 繊維集合体の成形方法、該方法によって成形された繊維集合体および前記繊維集合体の成形装置 |
Also Published As
Publication number | Publication date |
---|---|
JPWO2002063086A1 (ja) | 2004-06-10 |
JP4320547B2 (ja) | 2009-08-26 |
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