Title of Invention

A METHOD OF MANUFACTURING AN ECCENTRIC POLYESTER-POLYETHYLENE-BICOMPONENT FIBRE

Abstract

1. Method for manufacturing an eccentric bicomponent fibre of the core/skin type with a soft fed and having improved latent crimping, wherein an eccentric core/skin fibre, with a skin portion related to the fibre cross-section of 35 to 70%, is manufactured by meft spinning polyester as the com component and polyethylene as the skin component, at a spinning speed of 600 to 2,000 m/min, the fibre thus obtained is drawn at a temperature of 40 to 70°C aid at the ratio W^ + 20%, then stuff-crimped, Wm being understood to refer to the drawing ratio at which the number of arcs per cm reaches a maximum.

Full Text

Eccentric poiyester-poiyethylene-bicomponent fibre Description This invention relates to a bicomponent fibre of the core/skin type with polyester as the core component and polyethylene as the skin component, wherein the core is arranged eccentrically and the fibre is very soft to touch and has an intensive latent crimp. Because of their balanced property profile, polyester fibres are now among the most widely used synthetic fibres. In particular, numerous efforts have been made in recent years to develop polyester fibres with additional specific properties for certain applications. Compared to fibres of polyolefins, such as polyethylene or polypropylene, polyester fibres have a harder feel at the same titre. In some applications, e.g. textile hygiene products, for example nappies and sanitary towels, this harder feel is seen as a disadvantage. This also applies to textile hygiene products such as corresponding non-woven fabrics. There have been many attempts at improving this feel. For example, a polyolefin bicomponent fibre and non-woven fabrics produced from it are described in EP 0 277 707 A2. The fibres described there may, among other things, be a cone/skin fibre with a polyester core and a skin consisting of a mixture erf a linear low density copolymer of ethylene and at least one alpha olefin, with 4 to 8 carbon atoms and 1 to 50% by weight of a crystalline polypropylene. The number of crimping arcs of the core/skin filaments described therein leaves much to be desired, however, with the result that not even the voluminosity of non-woven fabrics which have been manufactured from such fibres meets all the requirements. Not even the method proposed in DE 1 760 755 for improving the crimp, where melt spun filaments emerging from the spinning nozzle are cooled more intensely on one side, so that additional crimping arcs are formed due to the resultant asymmetrical filament structure, produces fibres which exhibit the advantages which are achieved according to this invention. Nor do fibres such as those obtained according to JP 02 139 415 A2 meet aB the requirements imposed on feel and latent crimp. The method described therein consists in spinning to side-by-side filaments a component which consists essentially of polyethylene terephthalate and a second component consisting of a polyester which is manufactured from ethylene glycol, terephthalic acid and isophthalic acid and an aromatic dicarbonic acid with sulphonate groups. Nor does the method for manufacturing bicomponent fibres with latent crimp], described in JP 2 145 811 A, produce fibres which are characterised by a particularly soft feel and improved latent crimp. Finally mention is also made of EP 0 496 734 B1, which describes thermally bonded fibre products which are not produced in wet conditions, including high duty fibres such as polyester, polyamide, silk, etc., which are thermally bonded with dyeable thermoplastic bicomponent fibres. In addition to the side-by-side arrangement of bicomponent fibres, the core/skin arrangement, with an asymmetrical configuration, is also mentioned. Although there is already a whole range of methods for manufacturing fibres, particularly bicomponent fibres with good crimp properties, there is still a demand for improved fibres of the bicomponent type which are characterised by a particularly soft touch and improved latent crimp, which can be produced in particularly in a further development process involving a thermal action and results in an increased number of crimping arcs. A further object of the invention is to provide a simple method in which an extremely high number of crimping arcs is achieved by selecting suitable process parameters, a method in fact which operates simply and at low energy costs. This object is achieved by a method for manufacturing an eccentric bicomponent fibre of the core/skin type, with a soft feel and with improved latent crimp, by producing an eccentric core/skin fibre with a skin portion, related to the cross-section of the fibre, of 35 to 70%, by melt spinning polyester as the core component and polyethylene as the skin component, at a spinning speed of 600 to 2,000, preferably 600 to 1,400 m/min, drawing the fibre thus obtained at a temperature of 40 to 70°C and at a ratio W^ of + 20%, and then stuff- crimped. W^ refers to the drawing ratio at which the number of arcs per cm reaches a maximum and it is determined as indicated below. Drawing is preferably carried out at a temperature of 50 to 60°. It is advantageous for the bicomponent fibre to be manufactured as a core/skin fibre with extreme eccentric&y, where the extreme or maximum eccentricity is reached when the core component reaches the outer edge of the skin components, as shown diagrammatically in Figure 1. Polyethylene terephthalate is ideal as the polyester. Conventional, and in particular commercially available types of polyethylene may be used as polyethylene for the skin component. These include, in particular, fibre-forming linear ethylene polymers such as linear high density polyethylene (HDPE), which has a density in the range of 0.941 to 0.965 g/cm3 and linear low density polyethylene (LLDPE), which typically has a density within the range of low density polyethylene (LOPE), and linear medium density polyethylene (LMDPE), i.e. densities ranging from approx. 0.1 to 0.94 g/cm3. The densities of linear ethylene polymers may be measured according to the standard ASTM D-792; a suitable definition for this can be found in ASTM 0-1248. These polymers may be manufactured using coordination catalysts; they are generally known as linear polymers because essentially they have no branched chains such as those that may be formed when monomers are polymerised to the main polymer chain. LLDPE is a low density linear ethylene polymer in which ethylene has been polymerised with a small quantity of a-p ethylenically unsaturated alkenes which exhibit 3 to 12 carbon atoms per alkene molecule, in particular 4 to 5 carbon atoms. It is advantageous for the fibre to be manufactured with a titre of 2 to 7 dtex, this titre indication relating to the fibre after drawing; the drawing is preferably carried out at a ratio Wmax ranging form 1.4 to 2.4 + 20%. A further object of the invention is the use erf the bicomponent fibres, manufactured according to the method described above for manufacturing hygiene products. The bicomponent fibres are preferred for manufacturing hygienic textile fabrics, and particularly non-woven fabrics. A particularly advantageous application is the manufacture of nappies, towels, liners and the like. The core component may consist of conventional mett-spinnable polyester material. All known types suitable for fibre manufacture may be considered in principle as polyester material. Such polyesters consist essentially of components which derive from aromatic dicarbonic acids and from aliphatic diols. Commonly used aromatic dicarbonic acid components are the bivalent residues of benzol dicarbonic adds, particularly erf terephthafic acid and isophthalic acid; commonly used diols have 2 to 4 C atoms, ethylene glycol being particularly suftable. Of particular advantage is a polyester material at least 85 mol% of which consists of polyethylene terephthalate. The remaining 15 mol% are then composed of dicarbonic acid units and glycol units which act as so-called modifiers and which enable the expert to further influence the physical and chemical properties of the fibres produced in a specific manner. Examples of such dicarbonic acid units are residues of isophthalic acid or of aliphatic dicarbonic acid, e.g. glutaric acid, adipinic acid, sabacic acid; examples of did residues with a modifying action are those of longer chain diols, e.g. of propane diol or butane diol, of di- or triethyiene glycol or, if available in a small quantity, of polygiycol with a molecular weight of 500 to 2000 g/mol. Particularly preferable are polyesters which contain at least 95 mol% of polyethylene terephthalate, particularly those of unmodified polyethylene terephthalate. Such polyesters normally have a molecular weight equivalent to an intrinsic viscosity (IV) of 0.5 to 1.4 (dl/g), measured on solutions in djchtoroacetic acid at 25°C. It is important for the melting point of the polyester component to differ from that of the polyethylene component by at least 30°C because the lower metting component, namely the polyethylene, may or should serve as a bonding material in the manufacture of bonded non- woven fabrics, other textile fabrics and other hygiene products. Devices of prior art, with suitable nozzles, may be used for manufacturing fibres with a core/skin profile where the core occupies an eccentric position. It is essential for the core not to lie centred and symmetrically in the cross-section, but eccentrically. ti is an advantage for the core to be displaced as far as possible from the centre to the periphery, and a particular advantage is the position with extreme eccentricity, i.e. where the core component reaches the edge of the skin component, according to a configuration shown in Fig. 1, i.e. it has at least one point in common tangentialiy of the periphery of the cross-section. The spinning speed in the method according to the invention is between 600 and 2,000, preferably between 600 and 1,400 m/min. The escape speed on the nozzle escape surface is matched to the spinning speed and the drawing ratio so that a fibre is produced with the desired titre, i.e. a titre of approx. 2 to 7 dtex. The spinning speed is understood to be the speed at which the solidified filaments are pulled off. The filaments thus pulled off may either be guided directly to the area of drawing or first wound on and stretched at the ratio Wmax later. The required ratio W^ is determined as follows. Bicomponent filaments of the core/skin type - such as that described above - are spun with an eccentric position of the core, and approximately 10 samples are thai drawn individuaBy at different ratios of between 1.2 and 2.6, the drawing ratios varying by approx. 0.1, i.e. they are 1.2,1.3; 1.4 ...to 2.6. For all the samples the drawing takes place at the same temperature of between 40 and 70°C, preferably at 55°C. The samples are then crimped in a stuffer box. After crimping in the stuffier box the fibres are subjected to heat treatment at 120°C, with a holding time of 3 minutes. The number of arcs per centimetre is then counted for each sample and crimping K1 is determined according to DIN standard 53840. The values obtained are represented graphically as a function of the drawing ratio. Fig. 2 shows a suitable determination of the value W^ for a fibre with a titre of 3.0 dtex and a core/skin ratio of 50:50. The value W^, is 1.7. The Wmax value is read off as the maximum of the number of arcs/an curve (as Y-axis) and drawing ratio (X-axis), and serves as a process parameter for the method according to the invention. This is the optimum value at which eccentric bicomponent fibres having a core/skin ratio of 50:50 aid a titre after drawing of 3 dtex are manufactured according to the invention. Similarly, the ratio Wmax for bicomponent fibres with other trtres, ranging from 2 to 7 dtex, and other core/skin ratios, can be determined by corresponding tests. The maximum crimping K1 may correspond to the maximum for the number of arcs, but need not. Figyre3^soshows^de>«k^»n^ After Wmax is determined the method according to the invention can be carried out on a production scale. The fibres drawn at the ratio Wmax are then stuff-crimped. The stuff-crimped fibres may be cut into staple fibres, then processed into suitable products, in particular textile products, preferably hygiene products, hygiene textile fabrics, hygiene non-woven fabrics, nappies, towels or liners and the lite, but also into cotton wool buds etc. As a result of the method according to the invention the fibres are given an additional latent crimp which, during further processing, can be initiated by heat treatment at temperatures exceeding approx. 100°C. Here the number of arcs already obtained by crimping in the stuffer box is further increased. The fibre therefore not only has a soft feel but also contributes to improving the bulk of the corresponding products. The non-woven fabric can be suitably strengthened by suftable heat treatment at temperatures at which the skin component becomes soft or begins to melt. It was particularly surprising to discover that it is possible, using the method according to the invention with a relatively low drawing ratio, to obtain fibres which, in addition to the arcs due to stuff-crimping, also have an increased number of arcs due to the initiation of the latent crimping capacity. This was particularly surprising as the general view was that an increase in Wensity The invention is explained in greater detail by means of the following example: Example Spun product is produced on a bicomponent spinning installation with an eccentric cross- section from standard polyester in the core, and polyethylene in the skin. The total throughout, at a core/skin ratio of 50/50, was 380 g/min per spinning point with an 827 hole nozzle. The individual spinning titre set here was 4.60 dtex. The drawing off speed was 1,000 m/min. The mass temperature of the polyester was 285°C, that of the polyethylene 265°C. The spun filaments were coded by internal/external blowing over a blowing length erf 500 mm and with a volumetric airflow of 280 m3/h, at an air temperature of 40°C. Before they were piied together the filaments were also prepared with the normal dressing. The spun product was then fed to a conventional fibre belt conveyor said processed further. The drawing in the area indicated, particularly in the specific case for a final titre of 3.0 dtex, took place at a drawing ratio erf 1.7 between rotating rolls. The roll temperature at which the drawing was initiated was 50°C. After subsequent drying of the cable, again on rotating rolls at a temperature of 1G5°C, the fibre cable was mechanically crimped in a stuffer box crimping machine, then dried at 60°C in a flat belt dryer. The fibres were cut with a conventional staple fibre cutting machine. Patent Claims 1. Method for manufacturing an eccentric bicomponent fibre of the core/skin type with a soft fed and having improved latent crimping, wherein an eccentric core/skin fibre, with a skin portion related to the fibre cross-section of 35 to 70%, is manufactured by meft spinning polyester as the com component and polyethylene as the skin component, at a spinning speed of 600 to 2,000 m/min, the fibre thus obtained is drawn at a temperature of 40 to 70°C aid at the ratio W^ + 20%, then stuff-crimped, Wm being understood to refer to the drawing ratio at which the number of arcs per cm reaches a maximum. 2. Method according to daim 1. characterised in that the spinning speed is 600 to 1.400 m/min. 3. Method according to claim 1 or 2, characterised in that drawing is carried out at a temperature of 50 to 60°C. 4. Method according to at least one of claims 1 to 3, characterised in that the bicomponent fibre is manufactured as a core/skin fibre with extreme eccentricity. 5. Method according to at least one of claims 1 to 4, characterised in that polyethylene terephthalate is used as the polyester. 6. Method according to at least one of claims 1 to 5, characterised in that the fibre is manufactured with a tit re, after drawing, of 2 to 7 dtex. 7. Method according to at least one of claims 1 to 6. characterised in that the drawing is carried out at a ratio VV max ranging from 1.4 to 2.4 + 20%. 8. Use erf the bkx>mponent fibres manufac^ least one of claims 1 to 7 for manufacturing hygiene products. 9. Use according to claim 8 for manufacturing hygiene textile fabrics. 10. Use according to claim 9 for manufacturing non-woven fabrics. 11. Use according to claim 9 or 10 for manufacturing nappies. 12. Use according to claim 9 or 10 for manufacturing towels or liners. 13. A method for manufacturing an eccentric bicomponent fibre substantially as herein described with reference to the accompanying drawings.

Documents:

3102-CHENP-2004 AMENDED CLAIMS 17-05-2012.pdf

3102-CHENP-2004 AMENDED PAGES OF SPECIFICATION 17-05-2012.pdf

3102-CHENP-2004 CORRESPONDENCE OTHERS 30-01-2012.pdf

3102-CHENP-2004 CORRESPONDENCE OTHERS 16-03-2012.pdf

3102-CHENP-2004 CORRESPONDENCE OTHERS 18-05-2012.pdf

3102-chenp-2004 drawings.pdf

3102-CHENP-2004 EXAMINATION REPORT REPLY RECEIVED 17-05-2012.pdf

3102-CHENP-2004 FORM-1 17-05-2012.pdf

3102-CHENP-2004 FORM-3 17-05-2012.pdf

3102-CHENP-2004 OTHER PATENT DOCUMENT 17-05-2012.pdf

3102-CHENP-2004 POWER OF ATTORNEY 17-05-2012.pdf

3102-chenp-2004 claims.pdf

3102-chenp-2004 correspondence others.pdf

3102-chenp-2004 correspondence po.pdf

3102-chenp-2004 description (complete).pdf

3102-chenp-2004 form 1.pdf

3102-chenp-2004 form 18.pdf

3102-chenp-2004 form 3.pdf

3102-chenp-2004 form 5.pdf

3102-chenp-2004 pct.pdf