EP2185757B1 - Method for producing a textile fabric consisting of at least partially split yarns, fibers or filaments - Google Patents
Method for producing a textile fabric consisting of at least partially split yarns, fibers or filaments Download PDFInfo
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- EP2185757B1 EP2185757B1 EP08785156A EP08785156A EP2185757B1 EP 2185757 B1 EP2185757 B1 EP 2185757B1 EP 08785156 A EP08785156 A EP 08785156A EP 08785156 A EP08785156 A EP 08785156A EP 2185757 B1 EP2185757 B1 EP 2185757B1
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- EP
- European Patent Office
- Prior art keywords
- filaments
- dry ice
- fibers
- fabric
- splittable
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06C—FINISHING, DRESSING, TENTERING OR STRETCHING TEXTILE FABRICS
- D06C29/00—Finishing or dressing, of textile fabrics, not provided for in the preceding groups
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- 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
- D04H1/42—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 characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
- D04H1/4382—Stretched reticular film fibres; Composite fibres; Mixed fibres; Ultrafine fibres; Fibres for artificial leather
- D04H1/43825—Composite fibres
- D04H1/43828—Composite fibres sheath-core
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- 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
- D04H1/44—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 the fleeces or layers being consolidated by mechanical means, e.g. by rolling
- D04H1/46—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 the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres
- D04H1/492—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 the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres by fluid jet
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- 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
- D04H1/542—Adhesive fibres
- D04H1/549—Polyamides
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- 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
- D04H1/542—Adhesive fibres
- D04H1/55—Polyesters
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- 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
- D04H18/00—Needling machines
- D04H18/04—Needling machines with water jets
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- 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
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/005—Synthetic yarns or filaments
- D04H3/007—Addition polymers
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- 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
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/005—Synthetic yarns or filaments
- D04H3/009—Condensation or reaction polymers
- D04H3/011—Polyesters
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- 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
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/08—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
- D04H3/14—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between thermoplastic yarns or filaments produced by welding
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- 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
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/08—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
- D04H3/14—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between thermoplastic yarns or filaments produced by welding
- D04H3/147—Composite yarns or filaments
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- 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
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/08—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
- D04H3/16—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between thermoplastic filaments produced in association with filament formation, e.g. immediately following extrusion
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06C—FINISHING, DRESSING, TENTERING OR STRETCHING TEXTILE FABRICS
- D06C11/00—Teasing, napping or otherwise roughening or raising pile of textile fabrics
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- 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
- D04H1/541—Composite fibres, e.g. sheath-core, sea-island or side-by-side; Mixed fibres
- D04H1/5412—Composite fibres, e.g. sheath-core, sea-island or side-by-side; Mixed fibres sheath-core
Definitions
- the present invention relates to a process for producing a sheet from at least partially split yarns, fibers or filaments and to an apparatus for producing the same.
- a method for treating the surface of textiles by subjecting to drying ice is out WO 01/36733 known.
- a process for producing a sheet of at least partially split yarns, fibers or filaments is made EP 1428919 known.
- the object of the present invention has been made to provide a method which simplifies the production process of fabrics of splittable yarns, fibers or filaments and is economically particularly favorable.
- fibers or filaments only one, for example, compared to a high pressure water jet treatment, especially in Pressing about 120 to 500 bar, particularly low energy or low mechanical force are needed.
- the method is intended to enable at least partial splitting of both compatible polymers and conjugated yarns, fibers or filaments consisting of mutually incompatible polymers.
- a splittable starting sheet is formed by treatment, in particular by bombardment, with dry ice, with frozen water or with an air-particle mixture at a temperature of at least 20 ° C. to 30 ° C. below the glass transition temperature (Tg).
- Tg glass transition temperature
- the glass transition temperature (Tg) or softening temperature of an amorphous polymer used is the temperature at which the polymer exhibits the greatest change in deformability.
- the so-called Glass transition separates the below-lying brittle energy-elastic area (glass area) from the soft entropy-elastic area (rubber-elastic area) above.
- the transition to the flow region of the amorphous polymer is fluid.
- Semicrystalline polymers have both a glass transition temperature, below which the amorphous phase "freezes" (accompanied by embrittlement), as well as a melting temperature at which the crystalline phase dissolves. The melting temperature clearly separates the entropy-elastic range from the flow range.
- Particularly suitable solid particles of the air-particle mixture are inorganic particles, such as sand (for example quartz sand), or polymeric granules.
- the dry ice, the frozen water or the air-particle mixture is used in the form of pellets.
- dry ice or frozen water use as snow is also possible.
- dry ice pellets preferably cylindrical particles with a diameter of about 3 mm and a length between 5 and 30 mm are used here.
- dry-ice snow is understood to mean finer-grained and therefore less hard particles which, for example, have a diameter of approximately 0.1 mm and a length of equal to or less than 1 mm.
- the dry ice is frozen carbon dioxide with a temperature of about -78.5 ° C, which passes without residue into the gaseous state on impact with the splittable starting fabric (sublimation).
- the frozen water or the air-particle mixture no liquid, in particular no liquid water, is used for the splitting, an otherwise, for example in the case of a water jet treatment, required especially time, energy is eliminated -, and / or costly drying process of the fabric of at least partially split yarns, fibers or filaments.
- the temperature of the treated surface drops below the selected process parameters by about 60 ° C.
- the treatment temperature is chosen such that the temperature of the treated surface is at least 20 to 30 ° C below the glass transition temperature (Tg) of the polymers used as game, fibers or filaments.
- the treatment temperature is at least 20 to 30 ° C below the glass transition temperature (Tg) of polymers used as game, fibers or filaments, a certain embrittlement of the polymers is achieved, whereby the splitting of the fabric into elementary filaments is at least supported or promoted, without damage the elementary filaments.
- Tg glass transition temperature
- Damage to the elementary filaments is also avoided by the comparatively low hardness of the dry ice, the air-sand mixture or the frozen water.
- the volume of carbon dioxide from the solid to the gaseous state of aggregation expands abruptly by about 600 to 800 times its original volume.
- the dry ice settles between the elementary filaments, whereby the splitting of the fabric into elementary filaments is also at least supported or promoted.
- core-sheat structure core-sheat structure
- orange-slit or cake-piece structure pie-structure
- splittable starting sheet one in which the elementary filaments are present in a pie structure, preferably having 2 to 64 segments, in particular for influencing the diameter of the filaments.
- a nonwoven fabric is used as the splittable starting sheet.
- the nonwoven fabric staple fiber nonwoven fabrics or spunbonded nonwoven fabrics having continuous fibers or composite fibers which are obtained by either a melt spinning or a solvent spinning process are preferably used.
- melt-spun nonwovens which have the advantage over solvent-spun nonwovens that no solvent has to be removed and that their use is less expensive.
- splittable starting sheet is preferably a pre-bonded nonwoven fabric used, which is thermally, mechanically and / or chemically preconsolidated, particularly preferably thermally preconsolidated.
- the yarns, fibers or filaments of the fabric preferably have at least two elementary filaments which are selected from polymer pairs or blends of polyolefins, polyesters, polyamides and / or polyurethanes in any desired combination with one another.
- polyethylene or polypropylene are used, as preferred polyesters, for example, polyethylene terephthalate, polybutylene terephthalate, polytrimethylene terephthalate, recycled polyester, polylactate or copolyester, as preferred polyamides, for example polyamide 6, polyamide 12, polyamide 66 or copolyamides.
- the treatment in particular the bombardment, takes place on the surface of the splittable starting sheet with the dry ice, the frozen water or the air-particle mixture preferably at an angle of incidence of 0.1 ° to 180 °, more preferably of 45 ° to 135 ° and most preferably of 90 °.
- the kinetic energy of the particles of the dry ice, the frozen water or the air-particle mixture is advantageously equal to or more than 0.4 Joule.
- the mass and the speed of the particles are chosen so that there is no optical damage to the fabric or formation of a hole in the fabric.
- the flow rate on the dry ice, on the frozen water or on the air-particle mixture is advantageously 30 kg / h to 70 kg / h, preferably 30 kg / h to 50 kg / h.
- the particles of the dry ice, of the frozen water or of the air-particle mixture preferably impinge on the surface of the splittable starting fabric with an average size of 10 ⁇ m to 30 mm, particularly preferably of 0.1 mm to 10 mm.
- the bombardment of the surface of the splittable starting fabric with the dry ice, frozen water or the air-particle mixture is preferably carried out at a speed of 100 m / s to 500 m / s at a feed rate of the outlet nozzle from 2.5 m / min 12, 5 m / min, more preferably from 2.5 m / min to 5 m / min.
- the splitting into the elementary filaments is advantageously carried out at pressures of from 0.5 bar to 16 bar, preferably from 0.5 bar to 6 bar, particularly preferably from 0.5 to 2 bar.
- the device for splitting a fabric from at least partially split yarns, fibers or filaments of at least two elementary filaments in particular according to a method of claims 1 to 7, at least one can be directed against the splittable starting fabric outlet nozzle for firing the at least one splittable surface of the cleavable starting fabric with dry ice, with frozen water or with an air-particle mixture.
- internals for comminuting the dry ice, the frozen water or the air-particle mixture are arranged in at least one outlet nozzle.
- Scanning electron micrographs were taken using a JEOL JSM-6480LV low-pressure scanning electron microscope under an acceleration voltage of 20 kV.
- Example 1 a spunbonded nonwoven fabric, in particular a spunbonded nonwoven fabric, from bicomponent endless filaments with a piezoelectric structure with 16 segments consisting of alternating polyethylene terephthalate / polyamide 6 (PET / PA6) in a weight ratio of 70: 30, bombarded with dry ice pellets.
- PET / PA6 polyethylene terephthalate / polyamide 6
- the spunbonded fabric is minimally needled and thus minimally mechanically solidified, so that the spunbonded fabric can be transported.
- the spunbonded fabric is thermally preconsolidated, wherein the thermal preconsolidation takes place on a heatable platen press in a period of 30 seconds at a temperature of 150 ° C and a pressure of 300 bar.
- the spunbonded fabric is placed at an angle of 90 ° below the outlet nozzle of the dry ice pellets.
- the shape of the nozzle is a wide-spout nozzle with a rectangular exit area of 50 mm x 4 mm. This nozzle is used to distribute the energy over as large an area as possible, with the use of, for example, a round nozzle being suitable in principle. Subsequently, the spunbond fabric is bombarded vertically with the dry ice pellets.
- Polyethylene terephthalate (crystalline) has a glass transition temperature (Tg) of about 80 ° C and a melting temperature of about 255 ° C according to ISO 11359 according to ISO 75 HDT / A (1.8 MPa) and polyamide 6 has according to ISO 75 HDT / A (1.8 MPa) has a glass transition temperature (Tg) of about 65 ° C and a melting temperature of about 220 ° C according to ISO 11359).
- the dry ice pellets have a diameter of about 3 mm and a length of 1 cm. At a density of dry ice of 1.56 g / cm 3 , a pellet weighs about 0.11 g (mass m).
- the bombardment with dry ice pellets takes place with a flow rate of 50 kg / h at a speed (v) of the dry ice pellets of 300 m / s.
- the distance between the exit nozzle and the surface of the splittable starting sheet is between 10 mm and 100 mm, preferably between 25 mm and 75 mm.
- the pressure of the dry ice pellets in the bombardment of the spunbonded fabric is 2 bar.
- the feed speed of the outlet nozzle is 5 m / min.
- FIG. 1 shows a scanning electron micrograph of the spunbonded fabric of Example 1.
- dry ice snow with a particle size of about 0.1 mm ⁇ 0.5 mm is used instead of the dry ice pellets.
- the dry ice snow weighs 0.0105 g (mass m).
- the bombardment with dry ice snow takes place at a speed (v) of 300 m / s.
- the spunbonded nonwoven fabric used is made of bicomponent filaments having a pie structure with 16 segments, consisting of polyethylene terephthalate / polyamide 6 in a weight ratio of 70: 30.
- the nonwoven fabric is not thermally preconsolidated. Otherwise, the process is carried out analogously to the conditions of Example 1, wherein only dry ice snow is used instead of the dry ice pellets.
- FIG. 2 shows a scanning electron micrograph of the spunbonded fabric of Example 2.
- the filaments are more mobile than those according to Example 1.
- Example 3 a spunbonded nonwoven fabric of bicomponent filaments having a pie structure with 16 segments, consisting of polyethylene terephthalate / polyamide 6 in a weight ratio of 70: 30 used.
- the procedure is analogous to Example 2 with dry ice snow instead of dry ice pellets.
- the pressure of the dry ice snow in Example 3 in the bombardment of the spunbonded fabric only 1 bar instead of 2 bar.
- FIG. 3 shows a scanning electron micrograph of the spunbonded fabric of Example 3.
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- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Nonwoven Fabrics (AREA)
- Artificial Filaments (AREA)
- Treatment Of Fiber Materials (AREA)
- Chemical Or Physical Treatment Of Fibers (AREA)
- Woven Fabrics (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
Abstract
Description
Die vorliegende Erfindung betrifft ein Verfahren zur Herstellung eines Flächengebildes aus zumindest teilweise gesplitteten Garnen, Fasern oder Filamenten und eine Vorrichtung zu dessen Herstellung.The present invention relates to a process for producing a sheet from at least partially split yarns, fibers or filaments and to an apparatus for producing the same.
Aus dem Dokument
Ein Verfahren zur Herstellung polymerer Erzeugnisse, die mit feinen Partikeln beaufschlagt werden, ist aus
Ein Verfahren zur Behandlung der Oberfläche von Textilien durch eine Beaufschlagung von Trockneneis ist aus
Ein Verfahren zur Herstellung eines Flächengebildes aus zumindest teilweise gesplitteten Garnen, Fasern oder Filamenten ist aus
Die vorliegende Erfindung hat sich die Aufgabe gestellt, ein Verfahren anzugeben, welches den Herstellungsprozess von Flächengebilden aus splittbaren Garnen, Fasern oder Filamenten vereinfacht und wirtschaftlich besonders günstig ist.The object of the present invention has been made to provide a method which simplifies the production process of fabrics of splittable yarns, fibers or filaments and is economically particularly favorable.
Für den Herstellungsprozess von Flächengebilden aus zumindest teilweise splittbaren Garnen, Fasern oder Filamenten soll nur eine beispielsweise gegenüber einer Hochdruck-Wasserstrahlbehandlung, insbesondere bei Drücken von etwa 120 bis 500 bar, besonders geringe Energie bzw. geringe mechanische Kraft benötigt werden.For the production process of fabrics of at least partially splittable yarns, fibers or filaments only one, for example, compared to a high pressure water jet treatment, especially in Pressing about 120 to 500 bar, particularly low energy or low mechanical force are needed.
Ferner sollen bei dem Verfahren zusätzliche besonders zeit-, energie-, und/oder kostenintensive Prozessschritte, wie zum Beispiel die bei einer Wasserstrahlbehandlung erforderliche Trocknung des Flächengebildes, nicht erforderlich sein.Furthermore, in the method additional particularly time, energy, and / or cost-intensive process steps, such as the drying of the fabric required in a water jet treatment, should not be required.
Des Weiteren soll das Verfahren die zumindest teilweise Splittung sowohl von aus miteinander verträglichen Polymeren als auch von aus miteinander unverträglichen Polymeren bestehenden konjugierten Garnen, Fasern oder Filamenten ermöglichen.Furthermore, the method is intended to enable at least partial splitting of both compatible polymers and conjugated yarns, fibers or filaments consisting of mutually incompatible polymers.
Die Lösung der gestellten Aufgaben wird mit den Merkmalen der Ansprüche 1 bis 7 erreicht.The solution of the objects is achieved with the features of claims 1 to 7.
Bezüglich des erfindungsgemäßen Verfahrens wird dabei ein aufspaltbares Ausgangs-Flächengebilde durch Behandlung, insbesondere durch Beschuss, mit Trockeneis, mit gefrorenem Wasser oder mit einem Luft-Partikel-Gemisch bei einer Temperatur von mindestens 20 °C bis 30 °C unterhalb der Glasübergangstemperatur (Tg) der als Game, Fasern oder Filamente eingesetzten Polymere zumindest teilweise in die Elementarfilamente aufgespalten bzw. aufgesplittet.With regard to the method according to the invention, a splittable starting sheet is formed by treatment, in particular by bombardment, with dry ice, with frozen water or with an air-particle mixture at a temperature of at least 20 ° C. to 30 ° C. below the glass transition temperature (Tg). the polymers used as game, fibers or filaments at least partially split or split into the elementary filaments.
Die Glasübergangstemperatur (Tg) oder Erweichungstemperatur eines eingesetzten amorphen Polymers ist die Temperatur, bei der das Polymer die größte Änderung der Verformungsfähigkeit aufweist. Der sogenannte Glasübergang trennt den unterhalb liegenden spröden energieelastischen Bereich (Glasbereich) vom oberhalb liegenden weichen entropieelastischen Bereich (gummielastischen Bereich). Der Übergang in den Fließbereich des amorphen Polymers ist fließend. Teilkristalline Polymere besitzen sowohl eine Glasübergangstemperatur, unterhalb derer die amorphe Phase "einfriert" (einhergehend mit Versprödung), als auch eine Schmelztemperatur, bei der sich die kristalline Phase auflöst. Die Schmelztemperatur trennt den entropieelastischen Bereich deutlich vom Fließbereich ab.The glass transition temperature (Tg) or softening temperature of an amorphous polymer used is the temperature at which the polymer exhibits the greatest change in deformability. The so-called Glass transition separates the below-lying brittle energy-elastic area (glass area) from the soft entropy-elastic area (rubber-elastic area) above. The transition to the flow region of the amorphous polymer is fluid. Semicrystalline polymers have both a glass transition temperature, below which the amorphous phase "freezes" (accompanied by embrittlement), as well as a melting temperature at which the crystalline phase dissolves. The melting temperature clearly separates the entropy-elastic range from the flow range.
Als feste Partikel des Luft-Partikel-Gemischs kommen insbesondere anorganische Partikel, wie Sand (z.B. Quarzsand), oder polymere Granulate in Betracht.Particularly suitable solid particles of the air-particle mixture are inorganic particles, such as sand (for example quartz sand), or polymeric granules.
Bevorzugt wird das Trockeneis, das gefrorene Wasser oder das Luft-Partikel-Gemisch in Form von Pellets eingesetzt. Bezüglich des Trockeneises oder des gefrorenen Wassers kommt auch ein Einsatz als Schnee in Betracht.Preferably, the dry ice, the frozen water or the air-particle mixture is used in the form of pellets. With respect to dry ice or frozen water, use as snow is also possible.
Als Trockeneis-Pellets werden hier bevorzugt zylindrische Partikel mit einem Durchmesser von ca. 3 mm und einer Länge zwischen 5 und 30 mm eingesetzt. Unter Trockeneis-Schnee werden demgegenüber feinkörnigere und damit weniger harte Partikel verstanden, die beispielsweise einen Durchmesser von ca. 0,1 mm und eine Länge von gleich oder kleiner 1 mm aufweisen.As dry ice pellets preferably cylindrical particles with a diameter of about 3 mm and a length between 5 and 30 mm are used here. In contrast, dry-ice snow is understood to mean finer-grained and therefore less hard particles which, for example, have a diameter of approximately 0.1 mm and a length of equal to or less than 1 mm.
Beim Trockeneis handelt es sich um gefrorenes Kohlendioxid mit einer Temperatur von etwa -78,5 °C, das beim Aufprall auf das aufspaltbare Ausgangs-Flächengebilde rückstandslos in den gasförmigen Zustand übergeht (Sublimation).The dry ice is frozen carbon dioxide with a temperature of about -78.5 ° C, which passes without residue into the gaseous state on impact with the splittable starting fabric (sublimation).
Die Verwendung von Trockeneis hat daher den Vorteil, dass keine anschließende Abtrennung oder Filtration, wie beispielsweise bei Verwendung eines Luft-Sand-Gemischs, von den aufgespaltenen Elementarfilamente erfolgen muss.The use of dry ice therefore has the advantage that no subsequent separation or filtration, as for example when using an air-sand mixture, must be made of the split elementary filaments.
Ferner bildet sich bei der Verwendung von Trockeneis unter Normaldruck keine Flüssigkeit, wie zum Beispiel bei Wassereis, wodurch auch die Bezeichnung Trockeneis entstanden ist.Furthermore, when using dry ice under normal pressure no liquid is formed, as for example in the case of water ice, whereby the term dry ice has also arisen.
Dadurch, dass bei dem erfindungsgemäßen Verfahren mit dem Trockeneis, dem gefrorenen Wasser oder dem Luft-Partikel-Gemisch keine Flüssigkeit, insbesondere kein flüssiges Wasser, für die Aufspaltung verwendet wird, entfällt ein ansonsten, beispielsweise bei einer Wasserstrahlbehandlung, erforderlicher besonders zeit-, energie-, und/oder kostenintensiver Trocknungsprozess des Flächengebildes aus zumindest teilweise gesplitteten Garnen, Fasern oder Filamenten.Due to the fact that in the process according to the invention with the dry ice, the frozen water or the air-particle mixture no liquid, in particular no liquid water, is used for the splitting, an otherwise, for example in the case of a water jet treatment, required especially time, energy is eliminated -, and / or costly drying process of the fabric of at least partially split yarns, fibers or filaments.
Durch das Beschießen mit Trockeneis fällt die Temperatur der behandelten Oberfläche unter den ausgewählten Prozessparametem um ca. 60 °C herab.By bombarding with dry ice, the temperature of the treated surface drops below the selected process parameters by about 60 ° C.
Bei der Verwendung eines Luft-Partikel-Gemischs oder von gefrorenem Wasser wird die Behandlungstemperatur derart gewählt, dass die Temperatur der behandelten Oberfläche um mindestens 20 bis 30 °C unterhalb der Glasübergangstemperatur (Tg) der als Game, Fasern oder Filamente eingesetzten Polymere liegt.When using an air-particle mixture or frozen water, the treatment temperature is chosen such that the temperature of the treated surface is at least 20 to 30 ° C below the glass transition temperature (Tg) of the polymers used as game, fibers or filaments.
Dadurch, dass die Behandlungstemperatur mindestens 20 bis 30 °C unterhalb der Glasübergangstemperatur (Tg) der als Game, Fasern oder Filamente eingesetzten Polymere liegt, wird eine gewisse Versprödung der Polymere erreicht, wodurch die Aufspaltung des Flächengebildes in Elementarfilamente zumindest unterstützt oder gefördert wird, ohne die Elementarfilamente zu schädigen.The fact that the treatment temperature is at least 20 to 30 ° C below the glass transition temperature (Tg) of polymers used as game, fibers or filaments, a certain embrittlement of the polymers is achieved, whereby the splitting of the fabric into elementary filaments is at least supported or promoted, without damage the elementary filaments.
Eine Schädigung der Elementarfilamente wird auch durch die vergleichsweise geringe Härte des Trockeneises, des Luft-Sand-Gemischs bzw. des gefrorenen Wassers vermieden.Damage to the elementary filaments is also avoided by the comparatively low hardness of the dry ice, the air-sand mixture or the frozen water.
Der Einsatz in Form von Schnee anstelle von Pellets ist wegen dessen kleinerer Partikelgröße bzw. dessen geringer Härte (größerer "Weichheit") besonders bevorzugt im Hinblick auf eine die Elementarfilamente nicht schädigende, besonders schonende Aufspaltung bzw. Splittung.The use in the form of snow instead of pellets is particularly preferred in view of its smaller particle size or its low hardness (greater "softness") with regard to a filaments not particularly damaging, particularly gentle splitting or splitting.
Durch den Sublimationseffekt des Trockeneises bei der Behandlung des aufspaltbaren Ausgangs-Flächengebildes dehnt sich das Volumen des Kohlendioxids vom festen in den gasförmigen Aggregatzustand schlagartig um etwa das 600 bis 800-Fache seines ursprünglichen Volumens aus. Das Trockeneis legt sich dabei zwischen die Elementarfilamente, wodurch die Aufspaltung des Flächengebildes in Elementarfilamente ebenfalls zumindest unterstützt oder gefördert wird.Due to the sublimation effect of the dry ice in the treatment of the splittable starting fabric, the volume of carbon dioxide from the solid to the gaseous state of aggregation expands abruptly by about 600 to 800 times its original volume. The dry ice settles between the elementary filaments, whereby the splitting of the fabric into elementary filaments is also at least supported or promoted.
Als Anordnung der Elementarfilamente kommt über den Querschnitt der Game, Fasern oder Filamente betrachtet beispielsweise eine Kem-Mantel-Struktur (core-sheat-Struktur) oder eine Orangenspalten- bzw. Kuchenstück-Struktur (Pie-Struktur) in Betracht. Besonders bevorzugt wird als aufspaltbares Ausgangs-Flächengebilde eines eingesetzt, bei dem die Elementarfilamente in Pie-Struktur vorliegen, bevorzugt mit 2 bis 64 Segmenten, insbesondere zur Beeinflussung des Durchmessers der Filamente.As an arrangement of the elementary filaments considered over the cross section of the game, fibers or filaments considered, for example, a core-shell structure (core-sheat structure) or an orange-slit or cake-piece structure (pie-structure) into consideration. It is particularly preferred to use as the splittable starting sheet one in which the elementary filaments are present in a pie structure, preferably having 2 to 64 segments, in particular for influencing the diameter of the filaments.
Bevorzugte Ausgestaltungen der Erfindung sind Gegenstand der Unteransprüche.Preferred embodiments of the invention are the subject of the dependent claims.
Vorteilhafterweise wird als aufspaltbares Ausgangs-Flächengebilde ein Vliesstoff verwendet. Als Vliesstoff werden bevorzugt Stapelfaservliesstoffe oder Spinnvliesstoffe mit Endlosfasern oder mit zusammengesetzten Fasern eingesetzt, die entweder über einen Schmelzspinn- oder einen Lösungsmittelspinnprozess gewonnen werden.Advantageously, a nonwoven fabric is used as the splittable starting sheet. As the nonwoven fabric, staple fiber nonwoven fabrics or spunbonded nonwoven fabrics having continuous fibers or composite fibers which are obtained by either a melt spinning or a solvent spinning process are preferably used.
Bevorzugt werden Schmelzspinnvliesstoffe eingesetzt, die gegenüber Lösungsmittelspinnvliesstoffen den Vorteil haben, dass kein Lösungsmittel entfernt werden muss und dass deren Verwendung kostengünstiger ist.Preference is given to using melt-spun nonwovens which have the advantage over solvent-spun nonwovens that no solvent has to be removed and that their use is less expensive.
Als aufspaltbares Ausgangs-Flächengebilde wird vorzugsweise ein vorverfestigter Vliesstoff eingesetzt, der thermisch, mechanisch und/oder chemisch vorverfestigt wird, besonders bevorzugt thermisch vorverfestigt wird.As a splittable starting sheet is preferably a pre-bonded nonwoven fabric used, which is thermally, mechanically and / or chemically preconsolidated, particularly preferably thermally preconsolidated.
Die Garne, Fasern oder Filamente des Flächengebildes weisen vorzugsweise mindestens zwei Elementarfilamente auf, die ausgewählt sind aus Polymerpaaren oder -blends aus Polyolefinen, Polyestern, Polyamiden und/oder Polyurethanen in beliebiger Kombination untereinander.The yarns, fibers or filaments of the fabric preferably have at least two elementary filaments which are selected from polymer pairs or blends of polyolefins, polyesters, polyamides and / or polyurethanes in any desired combination with one another.
Als bevorzugte Polyolefine werden beispielsweise Polyethylen oder Polypropylen eingesetzt, als bevorzugte Polyester zum Beispiel Polyethylenterephthalat, Polybutylenterephthalat, Polytrimethylenterephthalat, recyclierte Polyester, Polylactat oder Copolyester, als bevorzugte Polyamide beispielsweise Polyamid 6, Polyamid 12, Polyamid 66 oder Copolyamide.As preferred polyolefins, for example, polyethylene or polypropylene are used, as preferred polyesters, for example, polyethylene terephthalate, polybutylene terephthalate, polytrimethylene terephthalate, recycled polyester, polylactate or copolyester, as preferred polyamides, for example polyamide 6, polyamide 12, polyamide 66 or copolyamides.
Für einen guten Wirkungsgrad erfolgt die Behandlung, insbesondere der Beschuss, auf die Oberfläche des aufspaltbaren Ausgangs-Flächengebildes mit dem Trockeneis, dem gefrorenen Wasser oder dem Luft-Partikel-Gemisch bevorzugt unter einem Auftreffwinkel von 0,1° bis 180°, besonders bevorzugt von 45° bis 135° und ganz besonders bevorzugt von 90°.For a good efficiency, the treatment, in particular the bombardment, takes place on the surface of the splittable starting sheet with the dry ice, the frozen water or the air-particle mixture preferably at an angle of incidence of 0.1 ° to 180 °, more preferably of 45 ° to 135 ° and most preferably of 90 °.
Die kinetische Energie der Partikel des Trockeneises, des gefrorenen Wassers oder des Luft-Partikel-Gemischs beträgt dabei vorteilhafterweise gleich oder mehr als 0,4 Joule. Dabei werden die Masse und die Geschwindigkeit der Partikel so gewählt, dass es nicht zu einer optischen Beschädigung des Flächengebildes bzw. einer Lochbildung im Flächengebilde kommt.The kinetic energy of the particles of the dry ice, the frozen water or the air-particle mixture is advantageously equal to or more than 0.4 Joule. The mass and the speed of the particles are chosen so that there is no optical damage to the fabric or formation of a hole in the fabric.
Die Durchflussmenge an dem Trockeneis, an dem gefrorenen Wasser oder an dem Luft-Partikel-Gemisch beträgt vorteilhafterweise 30 kg/ h bis 70 kg/ h, bevorzugt 30 kg/ h bis 50 kg/ h.The flow rate on the dry ice, on the frozen water or on the air-particle mixture is advantageously 30 kg / h to 70 kg / h, preferably 30 kg / h to 50 kg / h.
Die Partikel des Trockeneises, des gefrorenen Wassers oder des Luft-Partikel-Gemischs treffen bevorzugt mit einer mittleren Größe von 10 µm bis 30 mm, besonders bevorzugt von 0,1 mm bis 10 mm, auf die Oberfläche des aufspaltbaren Ausgangs-Flächengebildes auf.The particles of the dry ice, of the frozen water or of the air-particle mixture preferably impinge on the surface of the splittable starting fabric with an average size of 10 μm to 30 mm, particularly preferably of 0.1 mm to 10 mm.
Der Beschuss der Oberfläche des aufspaltbaren Ausgangs-Flächengebildes mit dem Trockeneis, gefrorenen Wasser oder dem Luft-Partikel-Gemisch erfolgt vorzugsweise mit einer Geschwindigkeit von 100 m/s bis 500 m/s bei einer Vorschubgeschwindigkeit der Austrittsdüse von 2,5 m/min bis 12, 5 m/min, besonders bevorzugt von 2,5 m/min bis 5 m/min.The bombardment of the surface of the splittable starting fabric with the dry ice, frozen water or the air-particle mixture is preferably carried out at a speed of 100 m / s to 500 m / s at a feed rate of the outlet nozzle from 2.5 m / min 12, 5 m / min, more preferably from 2.5 m / min to 5 m / min.
Die Aufspaltung in die Elementarfilamente erfolgt vorteilhafterweise bei Drücken von 0,5 bar bis 16 bar, bevorzugt von 0,5 bar bis 6 bar, besonders bevorzugt von 0,5 bis 2 bar.The splitting into the elementary filaments is advantageously carried out at pressures of from 0.5 bar to 16 bar, preferably from 0.5 bar to 6 bar, particularly preferably from 0.5 to 2 bar.
Ferner soll eine für das vorgenannte erfindungsgemäße Verfahren besonders geeignete Vorrichtung bereitgestellt werden, die dieses Verfahren auf einfache Weise ermöglicht.Furthermore, a particularly suitable for the aforementioned method according to the invention device is to be provided which allows this method in a simple manner.
Dazu weist die Vorrichtung zum Aufspalten eines Flächengebildes aus zumindest teilweise gesplitteten Garnen, Fasern oder Filamenten aus mindestens zwei Elementarfilamente, insbesondere nach einem Verfahren der Ansprüche 1 bis 7, mindestens eine gegen das aufspaltbare Ausgangs-Flächengebilde richtbare Austrittsdüse zum Beschuss der mindestens einen aufspaltbaren Oberfläche des aufspaltbaren Ausgangs-Flächengebildes mit Trockeneis, mit gefrorenem Wasser oder mit einem Luft-Partikel-Gemisch auf.For this purpose, the device for splitting a fabric from at least partially split yarns, fibers or filaments of at least two elementary filaments, in particular according to a method of claims 1 to 7, at least one can be directed against the splittable starting fabric outlet nozzle for firing the at least one splittable surface of the cleavable starting fabric with dry ice, with frozen water or with an air-particle mixture.
Vorteilhafterweise sind in zumindest einer Austrittsdüse Einbauten zur Zerkleinerung des Trockeneises, des gefrorenen Wassers oder des Luft-Partikel-Gemischs angeordnet.Advantageously, internals for comminuting the dry ice, the frozen water or the air-particle mixture are arranged in at least one outlet nozzle.
Der Gegenstand der Erfindung wird nachfolgend anhand von Beispielen und Figuren näher erläutern.
- In Fig. 1
- ist eine REM-Aufnahme eines 100-fach vergrößerten Ausschnitts der Oberfläche eines erfindungsgemäß mit Trockeneis-Pellets bei 2 bar gesplitteten und zuvor thermisch vorverfestigten Spinnvliesstoffs aus segmentierten PET/PA6-Piefasern mit einem Gewichtsverhältnis von 70 : 30 gezeigt,
- in Fig. 2
- ist eine REM-Aufnahme eines 100-fach vergrößerten Ausschnitts der Oberfläche eines erfindungsgemäß mit Trockeneis-Schnee bei 2 bar gesplitteten (nicht-thermisch-vorverfestigten) Spinnvliesstoffs aus segmentierten PET/PA6-Piefasem mit einem Gewichtsverhältnis von 70: 30 gezeigt und
- in Fig. 3
- ist eine REM-Aufnahme eines 100-fach vergrößerten Ausschnitts der Oberfläche eines erfindungsgemäß mit Trockeneis-Schnee bei 1 bar gesplitteten (nicht-thermisch-vorverfestigten) Spinnvliesstoffs aus segmentierten PET/PA6-Piefasem mit einem Gewichtsverhältnis von 70 : 30 gezeigt.
- In Fig. 1
- is a SEM image of a 100-fold enlarged section of the surface according to the invention with dry ice pellets split at 2 bar and previously thermally pre-bonded spunbonded nonwoven fabric from segmented PET / PA6 pief fibers with a weight ratio of 70: 30 shown
- in Fig. 2
- is a SEM micrograph of a 100-fold enlarged section of the surface of an inventive dry ice snow at 2 bar split (non-thermally pre-bonded) spunbonded fabric of segmented PET / PA6 Piefasem shown with a weight ratio of 70: 30 and
- in Fig. 3
- is an SEM image of a 100-fold enlarged section of the surface of an inventive dry ice snow at 1 bar split (non-thermally preconsolidated) spunbonded nonwoven fabric from segmented PET / PA6 piefasem having a weight ratio of 70:30.
Die Rasterelektronenmikroskop-Aufnahmen (REM-Aufnahmen) wurden mit einem Niederdruck-Rasterelektronenmikroskop JEOL JSM-6480LV unter einer Beschleunigungsspannung von 20 kV erstellt.Scanning electron micrographs (SEM images) were taken using a JEOL JSM-6480LV low-pressure scanning electron microscope under an acceleration voltage of 20 kV.
Gemäß Beispiel 1 wird ein Spinnvliesstoff, insbesondere ein Schmelzspinnvliesstoff, aus Bikomponenten-Endlosfilamenten mit einer Pie-Struktur mit 16 Segmenten, bestehend abwechselnd aus Polyethylenterephthalat/ Polyamid 6 (PET/ PA6) im Gewichtsverhältnis 70 : 30, mit Trockeneis-Pellets beschossen.According to Example 1, a spunbonded nonwoven fabric, in particular a spunbonded nonwoven fabric, from bicomponent endless filaments with a piezoelectric structure with 16 segments consisting of alternating polyethylene terephthalate / polyamide 6 (PET / PA6) in a weight ratio of 70: 30, bombarded with dry ice pellets.
Dazu liegt der Spinnvliesstoff minimal vernadelt und damit minimal mechanisch verfestigt vor, so dass der Spinnvliesstoff transportiert werden kann. Außerdem liegt der Spinnvliesstoff thermisch vorverfestigt vor, wobei die thermische Vorverfestigung an einer beheizbaren Plattenpresse in einem Zeitraum von 30 Sekunden bei einer Temperatur von 150°C und einem Druck von 300 bar erfolgt.For this purpose, the spunbonded fabric is minimally needled and thus minimally mechanically solidified, so that the spunbonded fabric can be transported. In addition, the spunbonded fabric is thermally preconsolidated, wherein the thermal preconsolidation takes place on a heatable platen press in a period of 30 seconds at a temperature of 150 ° C and a pressure of 300 bar.
Für die Splittung der Filamente im Spinnvliesstoff wird der Spinnvliesstoff in einem Winkel von 90° unterhalb der Austrittsdüse der Trockeneis-Pellets platziert. Bei der Form der Düse handelt es sich um eine Breitspitzdüse mit rechteckiger Austrittsfläche mit einer Größe von 50 mm x 4 mm. Diese Düse wird eingesetzt, um die Energie auf eine möglichst große Fläche zu verteilen, wobei prinzipiell auch der Einsatz beispielsweise einer Runddüse geeignet ist. Anschließend wird der Spinnvliesstoff senkrecht mit den Trockeneis-Pellets beschossen.For the splitting of the filaments in the spunbonded fabric, the spunbonded fabric is placed at an angle of 90 ° below the outlet nozzle of the dry ice pellets. The shape of the nozzle is a wide-spout nozzle with a rectangular exit area of 50 mm x 4 mm. This nozzle is used to distribute the energy over as large an area as possible, with the use of, for example, a round nozzle being suitable in principle. Subsequently, the spunbond fabric is bombarded vertically with the dry ice pellets.
Polyethylenterepthalat (kristallin) hat gemäß ISO 75 HDT/A (1,8 MPa) eine Glasübergangstemperatur (Tg) von ca. 80°C und eine Schmelztemperatur von ca. 255°C gemäß ISO 11359) und Polyamid 6 hat gemäß ISO 75 HDT/A (1,8 MPa) eine Glasübergangstemperatur (Tg) von ca. 65°C und eine Schmelztemperatur von ca. 220°C gemäß ISO 11359).Polyethylene terephthalate (crystalline) has a glass transition temperature (Tg) of about 80 ° C and a melting temperature of about 255 ° C according to ISO 11359 according to ISO 75 HDT / A (1.8 MPa) and polyamide 6 has according to ISO 75 HDT / A (1.8 MPa) has a glass transition temperature (Tg) of about 65 ° C and a melting temperature of about 220 ° C according to ISO 11359).
Die Trockeneis-Pellets haben ungefähr einen Durchmesser von 3 mm und eine Länge von 1 cm. Bei einer Dichte von Trockeneis von 1,56 g/cm3 wiegt ein Pellet ca. 0,11 g (Masse m).The dry ice pellets have a diameter of about 3 mm and a length of 1 cm. At a density of dry ice of 1.56 g / cm 3 , a pellet weighs about 0.11 g (mass m).
Der Beschuss mit Trockeneis-Pellets erfolgt mit einer Durchflussmenge von 50 kg/h bei einer Geschwindigkeit (v) der Trockeneis-Pellets von 300 m/s.The bombardment with dry ice pellets takes place with a flow rate of 50 kg / h at a speed (v) of the dry ice pellets of 300 m / s.
Damit beträgt die kinetische Energie (Ekin = 0,5 m v2 = 0,5 x 0,11 x 10-3 kg x (300 m/s)2 = 4,95 kg m2/s2) der Trockeneis-Pellets 4,95 Joule.Thus, the kinetic energy (E kin = 0.5 mv 2 = 0.5 x 0.11 x 10-3 kg x (300 m / s) 2 = 4.95 kg m 2 / s 2 ) of the dry ice pellets 4.95 joules.
Der Abstand zwischen der Austrittsdüse und der Oberfläche des aufspaltbaren Ausgangs-Flächengebildes beträgt zwischen 10 mm und 100 mm, bevorzugt zwischen 25 mm und 75 mm.The distance between the exit nozzle and the surface of the splittable starting sheet is between 10 mm and 100 mm, preferably between 25 mm and 75 mm.
Der Druck der Trockeneis-Pellets bei dem Beschuss des Spinnvliesstoffs beträgt 2 bar. Die Vorschubgeschwindigkeit der Austrittsdüse beträgt 5 m/min.The pressure of the dry ice pellets in the bombardment of the spunbonded fabric is 2 bar. The feed speed of the outlet nozzle is 5 m / min.
Die
Im Beispiel 2 wird im Unterschied zum Beispiel 1 statt der Trockeneis-Pellets Trockeneis-Schnee mit einer Partikelgröße von ca. 0,1 mm x 0,5 mm eingesetzt. Der Trockeneis-Schnee wiegt 0,0105 g (Masse m).In example 2, in contrast to example 1, dry ice snow with a particle size of about 0.1 mm × 0.5 mm is used instead of the dry ice pellets. The dry ice snow weighs 0.0105 g (mass m).
Der Beschuss mit Trockeneis-Schnee erfolgt mit einer Geschwindigkeit (v) von 300 m/s.The bombardment with dry ice snow takes place at a speed (v) of 300 m / s.
Damit beträgt die kinetische Energie (Ekin = 0,5 m v2 = 0,5 x 0,0105 x 10-3 kg x (300 m/s)2 = 0,4725 kg m2/s2) des Trockeneis-Schnees 0,4725 Joule.Thus, the kinetic energy (E kin = 0.5 mv 2 = 0.5 x 0.0105 x 10-3 kg x (300 m / s) 2 = 0.4725 kg m 2 / s 2 ) of the dry ice snow 0.4725 joules.
Zudem wird der eingesetzte Spinnvliesstoff aus Bikomponenten-Filamenten mit einer Pie-Struktur mit 16 Segmenten, bestehend aus Polyethylenterephthalat/ Polyamid 6 im Gewichtsverhältnis 70 : 30. Im Unterschied zu der Verfahrensweise in Beispiel 1 wird der Vliesstoff nicht thermisch vorverfestigt. Ansonsten erfolgt das Verfahren analog zu den Bedingungen aus Beispiel 1, wobei lediglich anstelle der Trockeneis-Pellets Trockeneis-Schnee eingesetzt wird.In addition, the spunbonded nonwoven fabric used is made of bicomponent filaments having a pie structure with 16 segments, consisting of polyethylene terephthalate / polyamide 6 in a weight ratio of 70: 30. In contrast to the procedure in Example 1, the nonwoven fabric is not thermally preconsolidated. Otherwise, the process is carried out analogously to the conditions of Example 1, wherein only dry ice snow is used instead of the dry ice pellets.
Die
Durch die fehlende thermische Vorverfestigung sind die Filamente beweglicher als die gemäß Beispiel 1.Due to the lack of thermal preconsolidation, the filaments are more mobile than those according to Example 1.
Bei dem Verfahren gemäß Beispiel 3 wird ebenfalls ein Spinnvliesstoff aus Bikomponenten-Filamenten mit einer Pie-Struktur mit 16 Segmenten, bestehend aus Polyethylenterephthalat/ Polyamid 6 im Gewichtsverhältnis 70 : 30 eingesetzt. Das Verfahren erfolgt analog zu Beispiel 2 mit Trockeneis-Schnee anstelle von Trockeneis-Pellets. Im Unterschied zu Beispiel 2 beträgt der Druck des Trockeneis-Schnees im Beispiel 3 bei dem Beschuss des Spinnvliesstoffs lediglich 1 bar statt 2 bar.In the method according to Example 3, a spunbonded nonwoven fabric of bicomponent filaments having a pie structure with 16 segments, consisting of polyethylene terephthalate / polyamide 6 in a weight ratio of 70: 30 used. The procedure is analogous to Example 2 with dry ice snow instead of dry ice pellets. In contrast to Example 2, the pressure of the dry ice snow in Example 3 in the bombardment of the spunbonded fabric only 1 bar instead of 2 bar.
Die
Dieses Verfahren gemäß Beispiel 3 zeigt, dass die Aufspaltung in die Elemantarfilamente selbst bei einem Druck von 1 bar noch gut möglich ist.This procedure according to Example 3 shows that the splitting into the elementary filaments is still well possible even at a pressure of 1 bar.
Claims (7)
- Method of forming a fabric comprising at least partially split yarns, fibers or filaments that are formed of at least two elementary filaments, characterized in that a splittable starting fabric is split by treatment, more particularly bombardment, with dry ice, with frozen water or with an air-particle mixture at a temperature of at least 20°C to 30°C below the glass transition temperature (Tg) of the polymers used as yarns, fibers or filaments at least partially into the elementary filaments.
- Method according to Claim 1 wherein a fibrous nonwoven web, more particularly a spunbonded fibrous nonwoven web, is used as splittable starting fabric.
- Method according to Claim 1 or 2 wherein a preconsolidated fibrous nonwoven web is used as splittable starting fabric.
- Method according to any one of the preceding claims wherein the yarns, fibers or filaments have at least two elementary filaments selected from polymer pairs or blends from polyolefins, polyesters, polyamides and/or polyurethanes in any desired combination.
- Method according to any one of the preceding claims wherein the treatment, more particularly the bombardment, onto the surface of the splittable starting fabric with said dry ice, said frozen water or said air-particle mixture is effected under an angle of incidence (α) of 0.1° to 180°, preferably 45° to 135° and more preferably 90°.
- Method according to any one of the preceding claims wherein the kinetic energy of the particles of said dry ice, of said frozen water or of said air-particle mixture is not less than 0.4 joule.
- Method according to any one of the preceding claims wherein the splitting into the elementary filaments is effected at pressures of 0.5 bar to 16 bar, preferably 0.5 to 6 bar and more preferably 0.5 to 2 bar.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL08785156T PL2185757T3 (en) | 2007-09-03 | 2008-07-28 | Method for producing a textile fabric consisting of at least partially split yarns, fibers or filaments |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102007041630A DE102007041630B4 (en) | 2007-09-03 | 2007-09-03 | Process for producing a fabric from at least partially split yarns, fibers or filaments and apparatus for its production |
PCT/EP2008/006206 WO2009030317A1 (en) | 2007-09-03 | 2008-07-28 | Method for producing a textile fabric consisting of at least partially split yarns, fibers or filaments and device for the production thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2185757A1 EP2185757A1 (en) | 2010-05-19 |
EP2185757B1 true EP2185757B1 (en) | 2012-04-25 |
Family
ID=40100190
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08785156A Not-in-force EP2185757B1 (en) | 2007-09-03 | 2008-07-28 | Method for producing a textile fabric consisting of at least partially split yarns, fibers or filaments |
Country Status (10)
Country | Link |
---|---|
EP (1) | EP2185757B1 (en) |
JP (1) | JP2010538170A (en) |
CN (1) | CN101778972A (en) |
AT (1) | ATE555242T1 (en) |
DE (1) | DE102007041630B4 (en) |
ES (1) | ES2383472T3 (en) |
PL (1) | PL2185757T3 (en) |
PT (1) | PT2185757E (en) |
TW (1) | TWI364467B (en) |
WO (1) | WO2009030317A1 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ITPR20110061A1 (en) * | 2011-07-06 | 2013-01-07 | A & G Chemical Production S R L | METHOD AND USE OF DRY ICE TO MAKE AND MODIFY AT LEAST PARTIALLY A FABRIC OR A CLOTHING GARMENT, FABRIC AND CLOTHING HEAD FROM THIS METHOD |
ITBO20120396A1 (en) * | 2012-07-20 | 2014-01-21 | Mactec S R L | METHOD TO TREAT AND / OR TO CLEAN FABRICS AND DEVICE TO REALIZE THIS METHOD |
EP2777662B1 (en) | 2013-03-11 | 2015-07-08 | Carl Freudenberg KG | Use of a velvet fibrebonded fabric substance |
KR20170113435A (en) * | 2016-04-01 | 2017-10-12 | 코오롱인더스트리 주식회사 | The Non-woven fabric Sheet For Mask Pack |
JP6855903B2 (en) * | 2017-04-24 | 2021-04-07 | セイコーエプソン株式会社 | Processing equipment and sheet manufacturing equipment |
JP6855904B2 (en) * | 2017-04-24 | 2021-04-07 | セイコーエプソン株式会社 | Processing equipment and sheet manufacturing equipment |
EP3539517B1 (en) * | 2018-03-13 | 2021-03-10 | BSN medical GmbH | Mechanical wound cleansing device |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4960430A (en) * | 1987-05-13 | 1990-10-02 | Veb Greika Greiz Weberei Und Veredlung | Method for manufacturing of mat and rough, laminar, ribbon-shaped or fibrous polymeric products with a stream of particles |
FR2749860B1 (en) * | 1996-06-17 | 1998-08-28 | Freudenberg Spunweb Sa | NON WOVEN TABLECLOTH FORMED OF VERY THIN CONTINUOUS FILAMENTS |
JPH10168740A (en) * | 1996-11-28 | 1998-06-23 | Toray Ind Inc | Flocked product and its production |
JP2000054255A (en) * | 1998-08-07 | 2000-02-22 | Daito Kosan:Kk | Fiber-processing machine |
DE19955660C1 (en) * | 1999-11-19 | 2001-03-22 | Messer Griesheim Gmbh | Particle jet treatment for texturing of cloth surfaces, employs particles made from cold, solidified fluid |
DE10115185A1 (en) * | 2001-03-27 | 2002-10-24 | Freudenberg Carl Kg | Splittable yarns, fibers or filaments and process for their production and device |
DE10258112B4 (en) * | 2002-12-11 | 2007-03-22 | Carl Freudenberg Kg | Process for producing a sheet from at least partially split yarns, fibers or filaments |
JP4064290B2 (en) * | 2003-04-25 | 2008-03-19 | 株式会社グリンテック山陽 | Coloring method for jeans products |
DE10347639A1 (en) * | 2003-10-09 | 2005-05-04 | Karl-Josef Brockmanns | Method for pneumatic and wet processing of textile products involves blowing of liquid and/or powderized dry carbon dioxide ice in a pressurized jet onto a textile product |
DE102005012895A1 (en) * | 2005-03-21 | 2006-09-28 | Eduard Küsters Maschinenfabrik GmbH & Co. KG | Method and device for the treatment of fibrous or filamentous materials |
DE102005014317A1 (en) * | 2005-03-30 | 2006-10-05 | Carl Freudenberg Kg | Synthetic leather, process for its preparation and its use |
-
2007
- 2007-09-03 DE DE102007041630A patent/DE102007041630B4/en not_active Expired - Fee Related
-
2008
- 2008-07-28 WO PCT/EP2008/006206 patent/WO2009030317A1/en active Application Filing
- 2008-07-28 AT AT08785156T patent/ATE555242T1/en active
- 2008-07-28 PT PT08785156T patent/PT2185757E/en unknown
- 2008-07-28 PL PL08785156T patent/PL2185757T3/en unknown
- 2008-07-28 ES ES08785156T patent/ES2383472T3/en active Active
- 2008-07-28 JP JP2010522202A patent/JP2010538170A/en active Pending
- 2008-07-28 CN CN200880103286A patent/CN101778972A/en active Pending
- 2008-07-28 EP EP08785156A patent/EP2185757B1/en not_active Not-in-force
- 2008-07-31 TW TW097128919A patent/TWI364467B/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
TWI364467B (en) | 2012-05-21 |
TW200934903A (en) | 2009-08-16 |
WO2009030317A1 (en) | 2009-03-12 |
JP2010538170A (en) | 2010-12-09 |
PT2185757E (en) | 2012-05-29 |
DE102007041630A1 (en) | 2009-03-05 |
EP2185757A1 (en) | 2010-05-19 |
CN101778972A (en) | 2010-07-14 |
ES2383472T3 (en) | 2012-06-21 |
ATE555242T1 (en) | 2012-05-15 |
PL2185757T3 (en) | 2012-09-28 |
DE102007041630B4 (en) | 2010-09-30 |
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