CN1324172C - Spinneret, oiling device, production device and production method for synthetic fibers - Google Patents
Spinneret, oiling device, production device and production method for synthetic fibers Download PDFInfo
- Publication number
- CN1324172C CN1324172C CNB028260287A CN02826028A CN1324172C CN 1324172 C CN1324172 C CN 1324172C CN B028260287 A CNB028260287 A CN B028260287A CN 02826028 A CN02826028 A CN 02826028A CN 1324172 C CN1324172 C CN 1324172C
- Authority
- CN
- China
- Prior art keywords
- spinneret
- induction element
- filament
- spinneret orifice
- elastic filament
- Prior art date
- 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.)
- Expired - Fee Related
Links
- 238000004519 manufacturing process Methods 0.000 title abstract description 16
- 229920002994 synthetic fiber Polymers 0.000 title abstract description 7
- 239000012209 synthetic fiber Substances 0.000 title abstract description 7
- 238000009987 spinning Methods 0.000 claims abstract description 41
- 238000000034 method Methods 0.000 claims abstract description 26
- 230000006698 induction Effects 0.000 claims description 65
- 229920001971 elastomer Polymers 0.000 claims description 47
- 239000000806 elastomer Substances 0.000 claims description 47
- 238000002074 melt spinning Methods 0.000 claims description 29
- 238000007599 discharging Methods 0.000 claims description 6
- 229920000642 polymer Polymers 0.000 abstract description 34
- 239000000463 material Substances 0.000 abstract description 13
- 230000002950 deficient Effects 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 32
- 230000000052 comparative effect Effects 0.000 description 23
- 238000001816 cooling Methods 0.000 description 22
- 239000004433 Thermoplastic polyurethane Substances 0.000 description 18
- 239000004744 fabric Substances 0.000 description 18
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 18
- 239000000835 fiber Substances 0.000 description 17
- 229920002635 polyurethane Polymers 0.000 description 14
- 239000004814 polyurethane Substances 0.000 description 14
- 238000011156 evaluation Methods 0.000 description 13
- 230000004927 fusion Effects 0.000 description 13
- 230000000694 effects Effects 0.000 description 11
- 229920002334 Spandex Polymers 0.000 description 10
- 239000004759 spandex Substances 0.000 description 10
- 230000000704 physical effect Effects 0.000 description 9
- 230000008859 change Effects 0.000 description 7
- 229920000728 polyester Polymers 0.000 description 7
- 230000014509 gene expression Effects 0.000 description 6
- 238000005259 measurement Methods 0.000 description 6
- 238000009434 installation Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 230000003746 surface roughness Effects 0.000 description 5
- 239000004952 Polyamide Substances 0.000 description 4
- 229920002647 polyamide Polymers 0.000 description 4
- 239000002243 precursor Substances 0.000 description 4
- 235000013351 cheese Nutrition 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 230000000994 depressogenic effect Effects 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000002828 fuel tank Substances 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 238000009940 knitting Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 238000004804 winding Methods 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 229920006306 polyurethane fiber Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 240000002129 Malva sylvestris Species 0.000 description 1
- 235000006770 Malva sylvestris Nutrition 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- NIHJEJFQQFQLTK-UHFFFAOYSA-N butanedioic acid;hexanedioic acid Chemical compound OC(=O)CCC(O)=O.OC(=O)CCCCC(O)=O NIHJEJFQQFQLTK-UHFFFAOYSA-N 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000000578 dry spinning Methods 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000013101 initial test Methods 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
- D01F6/70—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyurethanes
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D4/00—Spinnerette packs; Cleaning thereof
- D01D4/02—Spinnerettes
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
- D01D5/096—Humidity control, or oiling, of filaments, threads or the like, leaving the spinnerettes
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Abstract
A spinneret, an oiling device, a spinning device and a spinning method that are used for the production of synthetic fibers. The spinneret (1) has a single row of nozzle holes (2). Yarns spat out from the nozzle holes (2) of the spinneret (1) are taken up by a take-up roll (12) via an oiling device (8) and godet rollers (9, 10) without being twisted. A spinneret (20) is formed with grooves (24) radially extending from a nozzle hole (23). Molten polymer filtered by a filtering material (22) is allowed to enter the nozzle hole (23) via the grooves (24). An oiling device (31) may be provided with an oiling member (8) and a guide member (9) to eliminate defective oiling by the collaboration between them.
Description
Technical field
The present invention relates to be used for spinneret/spinning head, oiling device, manufacturing installation and the manufacture method of synthetic fiber.To describe the present invention in detail below.
At first, the present invention relates to a kind of be used to spin plurality of threads/filament and then when cutting apart, solidifying this long filament to its spinneret of reeling, and relate to a kind of manufacture method of using the synthetic fiber of this spinneret.More specifically, the present invention relates to a kind of spinneret that reduces the physical property difference between plurality of threads.
Secondly, the present invention relates to a kind of spinneret that is suitable for making polyurethane fiber, polyester fiber, polyamide fiber, polyamide fiber etc., and more specifically, relate to a kind of spinneret that can prolong the service life of filter medium and stably discharge polymer.
The 3rd, the present invention relates to a kind of device that comprises elastomer such as polyurethane that is used on clothes and the other products that is used to make, a kind of method that is used to make this elastomer and a kind of oiling device of refueling to by continuous spun elastic filament of being used for.
Background technology
The device for spinning that is used for synthetic fiber has a spinneret that is used for polymer is carried out spinning usually, and one is used for the oiling device and that refuels from the spun long filament of the spinneret orifice of this spinneret be used for reeling after the oiling roller that batches of this long filament.
Up to now, device for spinning various improvement have been made so that can stably produce high-quality long filament.Yet, as described below, what time need in addition to improve at building block and aspect being provided with.
Spinneret
Therein polymer from a spinneret, discharge and the manufacturing of the synthetic fiber of when solidifying, being reeled in, use a kind of following method usually.That is,, discharge polymer and winding several threads then from a plurality of spinnerets of every spinning machine from the viewpoint of productivity ratio.
Traditionally, in order to simplify its operation, maintenance etc., the spinneret that is used for this device for spinning have be arranged to arrange for example circumference, rhombus layout, grid layout, interlaced arrangement etc. more spinneret orifice to be mainly used in the effective use that realizes this spinneret area.
Yet in this employed up to now spinneret, variations in temperature is very big between the position of spinneret orifice.In addition, because polymer is to discharge from many rows, so blow to the cooling conditions of air difference on the long filament of being discharged.These factors have increased the differences of physical properties between long filament, and this is a problem.
Especially, during melt spinning, spin a kind of fusion elastomer with extremely low spinning tension.Therefore, for example can not cause that at common melt spinning the variation of state that is used to cool off a long filament of discharging of any problem can influence the fusion elastomer significantly in the polyester spinning etc., and cause it inhomogeneous, thereby make its deterioration.
In addition, in this spinneret, usually by before molten polymer is discharged from spinneret orifice, this molten polymer being filtered by a kind of filter medium with foreign matter/contaminant removal.In a kind of like this melt spinning is handled,, be known that by using a kind of being provided with as letter in Figure 13 shown in to filter from aspects such as processing ease, simplified equipment.Promptly, placing tight the place ahead of an assembly 102 spinnerets 101 to make a filter medium 100 has a space so that this polymer passes through the whole surface of this filter medium equably between this filter medium 100 and spinneret 101, thus the whole surface that can use filter medium 100 effectively.
Yet in melt spinning, it is usually higher and pollutant will be deposited on the filter medium 100 during operation gradually to be applied to pressure on the filter medium 100.As a result, the pressure that is applied on the filter medium 100 raises, and as shown in figure 14, the distortion of the whole or part building block of filter medium 100.This can cause irregular flow in the intake section of the spinneret orifice 103 of spinneret 101, and, in some cases, spinneret orifice 103 half obstruction that can become.A kind of like this state can cause the rapid rising of filter pressure, the decline and irregular the flowing of filter efficiency, and this can cause negative effect to the long filament of discharging from spinneret orifice, causes incomplete discharge etc.Therefore, when the some parts of filter medium was out of shape, even this filter medium itself still can filter, this whole filter medium should be changed immediately, thereby caused productivity ratio to reduce.Especially, compare with filter medium when having less discharge area when spinneret, for example be used for the spinneret of monofilament, this problem is very obvious.
Oiling device
Be used for the device for spinning of synthetic fiber, a kind of oiling device refuels to prevent because the wearing and tearing grade causes the damage of this long filament to long filament, and increases its smoothness and make processing ease.
A kind of such oiling device is a roller formula oiling device, wherein, one roller under being immersed in state in one oil groove/fuel tank, is rotated its some parts, on the surface of this roller, applying a uniform oil reservoir, and make long filament with this roller surperficial attached in advance and apply to carry out oil.
Also have a kind of guiding oiling device, wherein oil is supplied in the groove that is formed in the guiding piece, and a long filament is introduced this groove and it is advanced, thereby on this long filament, refuel.
In these oiling devices, before this long filament is wound on the roller, this long filament that is discharged from when oil is applied on this long filament or this not long ago contacted with the surface of described guiding piece.
The long filament that is discharged from refuel and contact surface on part because it solidifies etc. fully instability extremely.Therefore, any fluctuation of frictional resistance can be strengthened the labile state of this long filament, and this can to the character of the long filament of reeling particularly its homogeney have a negative impact.
In order to address the above problem, the inventor proposes a kind of oiling device that comprises at least one induction element, this induction element is used for by making a long filament will be applied to this long filament by an oil that is formed on the fuel feeding opening supply of this groove by a groove, wherein, this groove has: a summit, this summit have a tangent line on (this long filament) vertical curve/vertical line; All from this summit with respect to sweptback upper inclined surface of (this long filament) vertical line and inclined-plane, a bottom, simultaneously, this groove has the narrowest part with summit position adjacent place.This fuel feeding opening is arranged in above the summit 3mm or higher and be formed at this from (this long filament) vertical curve 2mm or farther position rooved face is arranged one, and has a bigger diameter (the open No.1993-23076 of Japanese unexamined patent publication No.) of width than the narrowest part of this groove.
Disclosed oiling device is an outstanding invention in the open No.1993-230706 of this Japanese unexamined patent publication No., wherein, is carrying out fuel feeding by when making that contact area between this long filament and guiding piece is as far as possible little and reduce to rub.
In recent years, to the increase in demand of elastomer, but because they can realize surcharge by increasing elasticity, improvement adaptability (fitting ability) etc.Elastomer for example as a kind of polyurethane elastomeric fiber of exemplary, shows the high extensibility of 50-300% in the actual scope of application.The long filament of one elastomer spins from a spinneret orifice and by air drying, spinning oil is applied thereto to reduce the friction between this long filament and guiding piece etc. then.Consider its high extensibility, compare, apply about 10 times oil mass with general fibre.
Yet, in the open No.1993-230706 of above-mentioned Japanese unexamined patent publication No. in the disclosed oiling device, even it is described a large amount of when oily when planning on an elastic filament, to apply, if this elastic filament does not contact consistently with this oiling device, promptly, if it, also will occur the part of fully not refueled because spinning swing, vibration or other factors and from oiling device or even temporarily break away from this elastic filament, thereby reduce the performance of this elastomer significantly.
The layout of device for spinning
As mentioned above, in recent years, polyurethane elastomeric fiber is owing to its excellent elasticity causes a large amount of attentions.Polyurethane fiber can be used for various purposes, but thereby because it can increase elasticity, improvement adaptability, stable shaped etc. make the dress material increment by the less amount of only mixing in dress material.
As the manufacture method of polyurethane elastomeric fiber, known have dried spin processes, wet spin processes and a melt spinning method.Wherein, the polyurethane elastomeric fiber that obtains by melt spinning method has good thermosetting, erosion resistant degree and transparency and low production cost.Therefore, in recent years, the use amount of polyurethane elastomeric fiber increases.In melt spinning method, as mentioned above, molten polymer is discharged from a spinneret, and the long filament of this discharge solidifies by cooling air (cold wind), and is refueled, and is wound on then on the roller.
The coiling of elastic filament normally carries out in the mode identical with the polyester filament with low elasticity, Tynex etc.Especially, molten polymer is expressed in the spinneret from an extruder (not shown), and from each spinneret orifice the long filament of elastomer is discharged along substantially straight down a direction.Each long filament of elastomer blows and solidifies on it by will cool off air with a hair-dryer, and refuels by an oiling device, and platoon leader's silk turns to by an induction element.After this, regulate the tension force of this elastomer of arranging again, and this long filament is fed to a work beam and is wound into the silk volume by two godet rollers.
In above-mentioned manufacturing installation, reeled in distortion with the state of 90 ℃ of its orientation rotations from the spun elastic filament of spinneret.Therefore, the length in this long filament road and dissimilate in this elastic filament from the frictional force that guiding piece is subjected to.Therefore an impossible problem when reel above-mentioned polyester, nylon etc. has appearred.That is, because polyurethane elastomeric fiber becomes than easier strains such as polyester, when this polyurethane elastomeric fiber was reeled with different long filament road length and frictional force, the performance of this elastomer in each volume dissimilated, and causes product performance to alter a great deal.For example, be arranged in the silk volume of work beam central authorities, almost do not having to twist and reel from the spun elastomer of spinneret.On the other hand, being arranged in the silk volume of work beam one end, reel with the bigger twist angle of variation that causes by guiding piece from the spun elastomer of spinneret.Therefore, owing to the frictional resistance that contacts this long filament that produces of long filament and guiding piece becomes bigger, and between a plurality of volumes, produce the tension difference of this elastic filament.Especially, in the silk volume of end, because the length in elastic filament road is longer, this elastic filament stands bigger air drag.This has further increased the tension difference between end silk volume and the central authorities' elastic filament of rolling up.
The difference of the frictional force that each elastic filament is subjected to causes the shape of thickness, elasticity, intensity and the undrawn yarn volume of long filament to produce difference.If by making fabric in conjunction with the silk volume that is wound with long filament of different nature on it, then the value of this product will be owing to as reducing by the bad outward appearance as shown in the striped etc.
Summary of the invention
The invention provides following invention to solve the problems referred to above of prior art.
Spinneret
First purpose of the present invention is to provide a kind of can be controlled at the spinneret of the physical property difference between long filament from their temperature differences when they are cooled spinneret orifice by what minimize the plurality of threads of discharging from spinning machine as far as possible.
First purpose of the present invention can be by a spinneret realization that is used to make plurality of threads, and this spinneret comprises a plurality of spinneret orifices that are formed in the single spinning plate, and wherein, described spinneret orifice is set to become substantially delegation.
A plurality of spinneret orifices of formation and spinneret orifice are set to become substantially delegation can reduce the spinneret surface temperature change in a single spinning plate of spinneret.Simultaneously, in cooling during from long filament that spinneret orifice is discharged, be set to become substantially delegation by spinneret orifice, can avoid fully, and the cold wind that blows on the long filament that moves ahead does not influence the long filament of going in the back owing to the temperature of cooling off the cold wind that causes at the spun long filament that moves ahead raises.When satisfying these conditions, can make uniform long filament and do not have the variation of the state of cooling.
Preferably, in spinneret of the present invention, be formed with 8 or more a plurality of spinneret orifice.This is because in the field of a large amount of spinneret orifice of needs, that is, in the large-duty field of needs, effect of the present invention can easily show by having 8 or more a plurality of spinneret orifice.
In addition, preferably, cold wind blows from a direction that is basically perpendicular to the polymer of discharging from above-mentioned spinneret with spinneret orifice of being arranged to delegation.This is because by blowing cold wind in such a way, the temperature of the cold wind of being accepted by each long filament becomes evenly, and the temperature of spinneret becomes even in above-mentioned direction.This has reduced the temperature difference between spinneret orifice.
The present invention preferably is applied to make the fusion elastomer, and this is because its effect is remarkable especially.Compare with multiduty fibers such as polyester fiber, polyamide fibers, elastomer has extremely low spinning tension usually.The temperature and being used to that its physical property is subjected to spinneret is cooled off the very big influence of temperature of the air of the long filament of discharging from spinneret orifice.Therefore, in elastomer, not only between long filament, show tangible differences of physical properties, and the swing of the long filament in cooling segment is also different because of long filament, and causes the inhomogeneous of long filament and fracture.
It is an essential characteristic of the present invention that spinneret orifice is set to become substantially delegation.In this was provided with, it was at interval necessary to consider that being used between spinneret orifice is easy to the long filament separate operation, and preferably the long filament number is 1 to 3.
Second purpose of the present invention is to provide a kind of spinneret, thereby this spinneret can the filter capacity that be arranged on the filter medium in this spinneret prevents from not exclusively to discharge and the replacement cycle of prolongation filter medium boosts productivity by making full use of.
Consider that filter efficiency can descend when contact when filter medium distortion and with spinneret, the inventor has carried out a large amount of research solving prior art problems, and so and finishes the present invention.
In order to realize above-mentioned second purpose, the invention provides a kind of spinneret, wherein, be provided with one on the top of this spinneret and be used for removing the filter medium of foreign matter, and be formed with and be used to guide through the molten polymer of filter medium guiding groove to spinneret orifice from molten polymer.
By being provided for guiding the guiding groove of the molten polymer of process filter medium to spinneret, even filter medium is out of shape and contacts with spinneret, also can be so that polymer passes through the surface of the filter medium directly over this groove reliably at least.This is arranged so that and can effectively utilizes filter area, and with replacement cycle of filter medium extend to one very long during and can not cause incomplete discharge.
Preferably, of the present invention be used to guide through molten polymer to the groove of spinneret orifice of filter medium arrange radially and be its center with spinneret orifice.This is because a kind of like this polymer that can guide the process filter medium reposefully that is arranged so that is to spinneret orifice.
In addition, when spinneret has a spinneret orifice corresponding to a filter medium, can realize effect of the present invention significantly.In other words, for example be used for the spinneret of monofilament, the area of the inlet in the top of spinneret orifice with respect to the area of filtration members hour, effect of the present invention can display significantly.
Consider the design difference of the size of spinneret, the intensity of filter medium etc., the shape of above-mentioned groove, the degree of depth etc. are unrestricted.Yet polymer should be directed in the spinneret orifice.Having above-mentioned other setting in addition causes polymer can not pass through filter medium.Preferably, the groove of spinneret is arranged on the whole surface of filter medium, and the distance between groove is less, and the number of groove is more.This is because if the distance between groove is excessive, this groove can be owing to the distortion of filter medium is stopped up.In addition, if groove forms inhomogeneously or the number of groove seldom, then can not utilize the filter capacity of filter medium fully or can not discharge stably.
Can be owing to the protuberance that groove forms is set with an acute angle towards filter medium.This makes and can reduce area that groove contacts with filter medium and the intensity that keeps protuberance, feasiblely can use filter medium effectively.
By being set in spinneret, protuberance that groove forms can begin to contact when filter medium is set with this filter medium.Even under this state, also can realize the effect of spinneret of the present invention.
Preferably, spinneret of the present invention can be used to spin for example elastic filament of typical polyurethane filament.With multiduty long filament for example polyester, polyamide etc. compare, elastic filament often is subjected to the uneven influence of long filament that causes because of disturbance, and therefore effect of the present invention becomes remarkable.
Oiling device
The 3rd purpose of the present invention is to provide a kind of oiling device, it can be by making elastic filament and refuel guiding piece and contact the quality of the elastic filament that keeps having good lubrication reliably, and prevent owing to becoming excessive with frictional force that contacting of oiling device produces.
The 3rd purpose of the present invention can realize by a kind of oiling device that is used for elastomer, this oiling device comprises that oil element and one that are used for oil is applied on the elastic filament are used to guide the induction element of elastic filament to the element that oils, and is characterized in that: the described element that oils comprises that a slot part that is used to guide elastic filament and one are used for oil is applied to through the oil supplying hole on the elastic filament of this slot part; This slot part comprises that one has the apex portion of tangent line and all from upper inclined surface and the lower bevel of this apex portion with respect to the vertical curve hypsokinesis on vertical curve; The elastic filament of being arranged to be positioned at the position lower than apex portion with induction element has one with respect to the elastic filament that is positioned at the position higher than apex portion and is not more than 3 ° back rake angle greater than 0 °.
Preferably, the width at the narrowest part place adjacent with apex portion of described slot part is 1.5mm or littler.
Preferably, oil around the apex portion of element and the surface roughness of induction element is 2S to 10S.
Preferably, the long filament of elastomer is 2 or still less, and total fineness is 88dtex or littler.In addition, preferably, described elastomer is a kind of elastomer that obtains by the melt spinning elastomer.
Device for spinning
The 4th purpose of the present invention can realize by a kind of device that is used to make elastomer, this device comprises a plurality of spinneret orifices and a work beam that is used to reel from the spun elastic filament of this spinneret orifice, wherein, described a plurality of spinneret orifice is arranged to the axially substantially parallel of its alignment direction and work beam as the crow flies.
This manufacturing installation also comprises and is arranged between spinneret orifice and the work beam, is used for guiding to the induction element of work beam from the spun elastic filament of spinneret orifice along direction substantially straight down, wherein, this induction element is arranged in therebetween interval width greater than the interval width between spinneret orifice, and to be arranged to elastic filament be 1.5 ° or littler with respect to the maximum and the difference between the minimum of a value at the inclination angle of vertical curve, and this inclination angle is created between spinneret orifice and the induction element and is owing to the interval difference between the spinneret orifice and between the induction element produces.
This manufacturing installation also comprises and being arranged between spinneret orifice and the induction element so that continue to use so that the oiling device that the direction of exerting pressure of the induction element that elastic filament tilts refuels to elastic filament.At this, the part from spinneret orifice to induction element comprises this induction element, and therefore oiling device can be arranged in this induction element.
The present invention also provides a kind of method that is used to make elastomer, and this method comprises that one is used for and will be wound to a step that has on the work beam of rotation of the alignment direction that is basically parallel to spinneret orifice from a plurality of spun elastic filaments of spinneret orifice of being arranged to a line.
Above-mentioned manufacture method can for: be arranged on induction element between spinneret orifice and the work beam and make interval width between guiding piece greater than the interval width between spinneret orifice, wherein, induction element guides to work beam with elastic filament with substantially straight down direction, wherein, elastic filament is 1.5 ° or littler with respect to the maximum and the difference between the minimum of a value at the inclination angle of vertical curve, and this inclination angle is created between spinneret orifice and the induction element and be owing to the interval difference between the spinneret orifice and between the induction element produces.
Above-mentioned manufacture method can for: continue to use so that the direction of exerting pressure of the induction element that elastic filament tilts refuels to elastic filament.At this, the part from spinneret orifice to induction element comprises induction element, and therefore can carry out refueling operation in induction element.
Description of drawings
Fig. 1 is the perspective view that illustrates according to the spinneret of one embodiment of the invention;
Fig. 2 one schematically illustrated one comprises the perspective view of the melt spinning device of spinneret shown in Figure 1;
Fig. 3 one illustrates the perspective view of the spinneret of prior art;
Fig. 4 illustrates spinneret according to another embodiment of the present invention, wherein, Fig. 4 (a) is a vertical view, and Fig. 4 (b) is a longitudinal sectional view, and Fig. 4 (c) is the viewgraph of cross-section that a nozzle block is shown, and this assembly remains on this spinneret and a filter medium wherein together;
Fig. 5 schematically illustrates a front view that comprises according to the melt spinning device of the oiling device of one embodiment of the invention;
Fig. 6 is the side view that the melt spinning device shown in the Fig. 5 with other annex schematically is shown;
Fig. 7 is the longitudinal sectional view that the amplification of the oiling device among Fig. 5 is shown;
Fig. 8 is the front view of the oiling device shown in Fig. 7;
Fig. 9 is the perspective view of an embodiment that the guiding piece of one of building block as oiling device of the present invention is shown;
Figure 10 is the partial front elevation view of Fig. 2;
Figure 11 illustrates a kind of perspective view that is used for the melt spinning device of melt spinning device shown in Figure 10 contrast;
Figure 12 illustrates the spinneret of Figure 11 and the vertical view of the relation of the position between the guiding piece;
Figure 13 is the longitudinal sectional view that the spinneret of a prior art is shown;
Figure 14 be Figure 13 is shown spinneret in time and the longitudinal sectional view of the variation that produces.
The specific embodiment
One embodiment of spinneret of the present invention is described below with reference to Fig. 1 and Fig. 2.
As shown in Figure 1, in a spinneret 1, be formed with a plurality of spinneret orifices 2, and this spinneret orifice 2 is to arrange substantially in single file.This spinneret 1 has 8 spinneret orifices 2.Preferably the number of this spinneret orifice 2 is more than 8 or 8.
To the material that is used in the single spinning plate in this spinneret 1 and size without limits, as long as it is being suitable for indeformable and warpage under the condition of employed polymer.
To the shape of cross section by using the fiber that this spinneret 1 obtains without limits, it can be the combination of circle, triangle, hollow type, cross or different shape.To the degree of its shape difference or hollow rate (hollowness ratio) also without limits.
In the melt spinning device shown in Fig. 24, be provided with a nozzle block 3 that in its housing, accommodates this spinneret 1.
This melt spinning device 4 is provided with an extruder 5, gear pump 6, nozzle block 3, hair-dryer 7, oiling device 8, godet roller 9,10, friction roller 11 and work beam 12.
The assessment test that spinneret to spinneret 1 of the present invention and prior art compares will be described below.In the spinneret of the prior art, as shown in Figure 3, in a single spinning plate 10, form two row spinneret orifices 11.These spinnerets are arranged in the device for spinning shown in Figure 2, and these two kinds of spinnerets are estimated.
Evaluation to the swing of the long filament in cooling segment
The long filament of observation position of 2cm begun to cool off the place by hair-dryer below is swung, and estimates according to following standard.
A: the swing of one filament is less than 2mm, and this swings aperiodicity;
B: the swing of one filament equals 2mm or greater than 2mm and less than 4mm, this swings aperiodicity;
C: the swing of one filament is equal to or greater than 4mm, and this swings aperiodicity.
The long filament uniformity is estimated
The Keisokki Evenness Tester that use is made by Keisokki Kogyo Co.Ltd. (Keisokki Kogyo Co., Ltd.), (give speed: 7.85m/min) giving precursor and making its elongation is 200% to measure the long filament uniformity to Model KET-80C by actively separating easypro (positivereeling).Measuring condition is as follows.Measurement pattern: the inertia pattern, sample velocities: 8m/min, measurement electrode length: 18mm, electrode width: 0.13mm, sample in measurement time: 5min is used for the speed of the twisting apparatus of plurality of threads/multifilament: 1000rpm.
The sample number is set to n=24, obtains U% (I) mean value of this 24 threads and estimates based on following standard.
A:U% (I) is less than 2%;
B:U% (I) equals 2% or greater than 2% and less than 3%;
C:U% (I) is equal to or greater than 3%.
Long filament property ranges (R) is estimated:
The REM-250 Tensilon that uses Toyo Baldwin Co.Ltd. to make measures.The initial testing power of using every filament fineness (dtex) 1/1110g is measured tensile strength and general extension degree as 50mm and draw speed under as the condition of 500mm/min in this filament length.Each sample is repeated 5 times to be measured.Calculate the mean value of this tensile strength and general extension degree then.Use the standard of n=24, obtain the R (scope between maximum and the minimum of a value) of the tensile strength of sample and general extension degree and estimate based on following standard.
A: tensile strength R is less than 0.07cN/dtex, and general extension degree R is less than 20%;
B: tensile strength R equals 0.07 or greater than 0.07 and less than 0.14cN/dtex, and general extension degree R equals 20% or greater than 20% and less than 30%;
C: tensile strength R is greater than 0.14cN/dtex, and general extension degree R is equal to or greater than 40%.
Knitted fabric is estimated: preparation does not have the knitted fabric of coating classification standard sample.Then, circular knitting machine MODEL TN-1 (the syringe diameter: 3.5 inches that use is made by KoikeSeisakusho with a thread-carrier, the knitting needle number: 350), precursor (is given speed: when 84m/min) being fed to by with knitting two minutes of the syringe of 168rpm work easypro by actively separating.Formed nothing is coated fabric tube to be placed on the standard blackboard to estimate this knitted fabric and it is stretched to a precalculated position.Coat knitted fabric classification standard sample by this formed knitted fabric sample of visual contrast and previously prepared nothing, to the nothing of this formed knitted fabric coat the knitted fabric grade estimate (one-level: good, secondary: good, three grades: common, level Four: relatively poor, Pyatyi: get dirty).
Use the standard of n=24, the grade that coats knitted fabric grade and each long filament based on average nothing is estimated sample according to following standard.
A: average do not have the knitted fabric of coating grade less than 2.5, level Four and Pyatyi do not occur;
B: average do not have the knitted fabric of coating grade and equal 2.5 or greater than 2.5 and less than 3.5, Pyatyi do not occur;
C: average nothing coats the knitted fabric grade and is equal to or greater than 3.5, Pyatyi do not occur.
(example 1)
TPU(Thermoplastic polyurethanes) is carried out melt spinning under 220 ℃ of melt temperatures, having 24 from one is formed on base material (spinneret in the hole (aperture φ 1.0) that being in line SUS630:W360 * T80 * H20mm) is arranged to delegation spins, and by being that the unidirectional cooling air through rectification of 0.3m/min cools off from the speed that blows perpendicular to this line direction.Then, by the roller oiling this long filament is refueled, and formed fusion Spandex (spandex) long filament (22dtex, 1 threads) is reeled.To the unevenness of the character of the swing of the long filament in the cooled region when reeling, the long filament that obtained, long filament and do not have the grade that coats knitted fabric and estimate.
(example 2)
TPU(Thermoplastic polyurethanes) is carried out melt spinning under 220 ℃ of melt temperatures, having 24 from one is formed on base material (spinneret in the hole (aperture φ 1.0) that being in line SUS630:W360 * T80 * H20mm) is arranged to delegation spins, and by being that the unidirectional cooling air through rectification of 0.3m/min cools off from the speed that blows perpendicular to this line direction.Then, by the roller oiling this long filament is refueled, and formed fusion Spandex long filament (44dtex, 2 threads) is reeled.Be similar to the evaluation of example 1.
(example 3)
TPU(Thermoplastic polyurethanes) is carried out melt spinning under 220 ℃ of melt temperatures, having 24 from one is formed on base material (spinneret in the hole (aperture φ 1.0) that being in line SUS630:W360 * T80 * H20mm) is arranged to delegation spins, and by being that the unidirectional cooling air through rectification of 0.3m/min cools off from the speed that blows perpendicular to this line direction.Then, by the roller oiling this long filament is refueled, and formed fusion Spandex long filament (66dtex, 3 threads) is reeled.Be similar to the evaluation of example 1.
(comparative examples 1)
TPU(Thermoplastic polyurethanes) is carried out melt spinning under 220 ℃ of melt temperatures, have 24 from one and be formed on base material (SUS630:W360 * T80 * H20mm) and be in line that to be arranged to wherein first row and second row be that the spinneret in holes (aperture φ 1.0) of two row of 4mm spins perpendicular to a cooling air outlet slit surface and line space, and by being that the unidirectional cooling air through rectification of 0.3m/min cools off from the speed that blows perpendicular to this line direction.Then, by the roller oiling this long filament is refueled, and formed fusion Spandex long filament (22dtex, 1 threads) is reeled.Be similar to the evaluation of example 1.
(comparative examples 2)
TPU(Thermoplastic polyurethanes) is carried out melt spinning under 220 ℃ of melt temperatures, have 24 from one and be formed on base material (SUS630:W360 * T80 * H20mm) and be in line that to be arranged to wherein first row and second row be that the spinneret in holes (aperture φ 1.0) of two row of 10mm spins perpendicular to a cooling air outlet slit surface and line space, and by being that the unidirectional cooling air through rectification of 0.3m/min cools off from the speed that blows perpendicular to this line direction.Then, by the roller oiling this long filament is refueled, and formed fusion Spandex long filament (22dtex, 1 threads) is reeled.Be similar to the evaluation of example 1.
(comparative examples 3)
TPU(Thermoplastic polyurethanes) is carried out melt spinning under 220 ℃ of melt temperatures, from one have 24 be formed on base material (SUS630:W360 * T80 * H20mm) and the spinneret in the holes (aperture φ 1.0) of the be in line angle that is arranged to wherein to have between first row and second row one 15 ° and line space two row that are 10mm spin, by being that the unidirectional cooling air through rectification of 0.3m/min cools off from the speed that blows perpendicular to this line direction.Then, by the roller oiling this long filament is refueled, and formed fusion Spandex long filament (22dtex, 1 threads) is reeled.Be similar to the evaluation of example 1.
(comparative examples 4)
TPU(Thermoplastic polyurethanes) is carried out melt spinning under 220 ℃ of melt temperatures, from one have 24 be formed on base material (SUS630:W360 * T80 * H20mm) and the spinneret in the holes (aperture φ 1.0) of the be in line angle that is arranged to wherein to have between first row and second row one 30 ° and line space two row that are 10mm spin, by being that the unidirectional cooling air through rectification of 0.3m/min cools off from the speed that blows perpendicular to this line direction.Then, by the roller oiling this long filament is refueled, and formed fusion Spandex long filament (22dtex, 1 threads) is reeled.Be similar to the evaluation of example 1.
The evaluation result of example 1 to 3 and comparative examples 1 to 4 is shown in Table 1.
Table 1
| Example 1 | Example 2 | Example 3 | Comparative examples 1 | Comparative examples 2 | Comparative examples 3 | Comparative examples 4 | |
| The long filament swing | A | A | A | C | C | B | B |
| The long filament unevenness | A | A | A | C | C | B | B |
| Property ranges | A | A | A | A | C | C | C |
| Knitted fabric is estimated | A | A | A | C | C | B | B |
| Overall assessment | A | A | A | C | C | B | B |
(comparative examples 5)
TPU(Thermoplastic polyurethanes) is carried out melt spinning under 220 ℃ of melt temperatures, from one have 24 be formed on base material (SUS630:W360 * T80 * H20mm) and the spinneret in the holes (aperture φ 1.0) of the be in line angle that is arranged to wherein to have between first row and second row one 60 ° and line space two row that are 10mm spin, by being that the unidirectional cooling air through rectification of 0.3m/min cools off from the speed that blows perpendicular to this line direction.Then, by the roller oiling this long filament is refueled, and formed fusion Spandex long filament (22dtex, 1 threads) is reeled.Be similar to the evaluation of example 1.
(comparative examples 6)
TPU(Thermoplastic polyurethanes) is carried out melt spinning under 220 ℃ of melt temperatures, have 24 from one and be formed on base material (SUS630:W360 * T80 * H20mm) and be in line that to be arranged to wherein first row and second row be that the spinneret in holes (aperture φ 1.0) of two row of 10mm spins perpendicular to cooling air outlet slit surface and line space, by being that the unidirectional cooling air through rectification of 0.3m/min cools off from the speed that blows perpendicular to this line direction.Then, by the roller oiling this long filament is refueled, and formed fusion Spandex long filament (44dtex, 2 threads) is reeled.Be similar to the evaluation of example 1.
The evaluation result of comparative examples 5 and 6 has been shown in the table 2.
Table 2
| Comparative examples 5 | Comparative examples 6 | |
| The long filament swing | C | C |
| The long filament unevenness | C | C |
| Property ranges | C | C |
| Knitted fabric is estimated | C | C |
| Overall assessment | C | C |
As above know in the table 1 and 2 and to illustrate, when the polymer of will discharge is spun into fiber, the spinneret of above-mentioned first embodiment can make spinneret temperature unanimity, and can prevent to be vulnerable at long filament the variation of the cooling condition between long filament in the cooling step of influence of disturbance.This makes can stably supply the precursor with less unevenness, the loss in intermediate process steps, raising end product quality and the increase output that the uneven long filament of minimizing causes.
Another embodiment of spinneret of the present invention is described below with reference to Fig. 4.
As shown in Figure 4, spinneret 20 is contained in the housing 21.On this spinneret 20, be provided with a filter medium 22.This spinneret 20 has a single spinneret orifice 23 in the central.This spinneret 20 comprises a plurality of guiding grooves 24 of the molten polymer of process filter medium 22 to spinneret orifice 23 that are used to guide.These a plurality of guiding grooves 24 are arranged radially and it is centered close to spinneret orifice 23 places.At the entrance side of this spinneret orifice 23, be formed with a tapered hole part 25.
Carry out one be used to estimate spinneret 20 performance measurement and below measurement result is described.
(example 4)
One have place in the device for spinning of a single shaft extruder one have Xiao A hardness be 90 by polyalcohol/methyl diphenylene diisocyanate/1 based on the poly adipate succinic acid ester base, the polyether polyols with reduced unsaturation that the 4-butanediol constitutes.Then, this polymer is extruded from the spinneret with following structure by a filter medium under 220 ℃ spinning temperature.In order to obtain 20 DENIER (denier) monofilament, carry out continued operation with the winding speed of 500m/min.
Spinneret structure: as shown in Figure 4.
Spinneret orifice number: 1
The angle of taper on spinneret orifice top: 30 °
Spinneret orifice inlet diameter: φ 2.0mm
Spinneret orifice diameter: φ 0.28mm
Spinneret orifice length: 0.56mm
The layout of the groove of spinneret: radial (angle between groove: 18 °)
The number of groove: 20
Well width: 0.5mm
Groove depth: 0.5mm
Distance between filter medium and the spinneret: 0.5mm
Carry out spinning under these conditions.The initial back pressure of filter medium is 4Mpa when spinning begins, and only is increased to 4.7Mpa after 7 days.Not exclusively discharge and stable operation take place have been carried out 30 days.In having used a filter medium of 30 days, find no the depressed part in bellmouth 25.
(comparative examples 7)
Use to remove and to be not used in guiding and to pass through the groove that the polymer of filter medium enters spinneret orifice and identical spinneret shown in the example 4, with example 4 in carry out a spinning operation under the identical condition.
Carry out spinning under these conditions.When the beginning spinning, the initial back pressure of filter medium is 6Mpa, and is increased to 10Mpa after 7 days.The back pressure of filter medium became 15Mpa after 12 days, and began to occur incomplete discharge.Therefore, must change filter medium.In having used 12 days filter medium, find to have the depressed part in bellmouth 25.
(comparative examples 8)
Use except that be not used in guiding through the polymer of filter medium enter the groove of spinneret orifice and filter medium with spinneret between distance as 0mm with spinneret contacts with identical spinneret shown in the example 4, with example 4 in carry out a spinning operation under the identical condition.
Carry out spinning under these conditions.When the beginning spinning, the initial back pressure of filter medium is 8Mpa.This back pressure rose to 15Mpa after 7 days, and must change filter medium because begin to occur not exclusively to discharge.In having used 7 days filter medium, find to have the depressed part in bellmouth.
Illustrate according to an embodiment who is used for the oiling device of elastomer of the present invention below with reference to Fig. 5 to 9.
In Fig. 5 and 6, with reference to label 31 expressions one oiling device, with reference to label 32 expressions one nozzle block, with reference to label 33 and 33 ' expression godet roller, reference marks F represents friction roller, and reference marks P represents paper tube.In Fig. 6, with reference to label 34 expression gear pumps, with reference to label 35 expression extruders, with reference to label 36 expression hair-dryers.The elastic filament W that discharges from nozzle block 32 through oiling device 31, godet roller 33,33 ' and friction roller F be wound on the paper tube P.
Oiling device 31 comprises that one is used for oil is added to the guiding piece 39 that the element 38 and that oils on the elastic filament W is used for elastic filament W is guided to the element 38 that oils.This elastic filament W one guiding device is made of oil element 38 and guiding piece 39.
Shown in Fig. 7 and 8, the element 38 that oils comprises that a slot part 40 that is used for guiding elastic filament W and one are towards the opening 41 that is formed at this slot part 40 oil supplying hole 42 of opening to be used for refueling to the elastic filament W that advances at slot part 40 communicatively.This slot part 40 comprise one with Fig. 7 in vertically the apex portion that contact of dotted line H 43, one with respect to the vertical curve H from these apex portion 43 extensions have the upper inclined surface 44 of back rake angle and lower bevel 43 and with the narrowest part 46 of these apex portion 43 adjacent position.
Preferably, this apex portion 43 be circle and have a little radius (for example, 0.1 to 20mm); But, to the not restriction of its shape.Importantly elastic filament W only contacts with slot part in this apex portion 43.Therefore, to upper inclined surface 44 and lower bevel 43 without limits with respect to the back rake angle α of the vertical curve H that extends from this apex portion 43 and β, but preferably this angle in 15 ° to 70 ° scopes.
As shown in Figure 7, preferably, the opening 41 in this slot part 40 is provided with in such a way, promptly, 41 beeline dH is 3mm or bigger from apex portion 43 to opening, is positioned at the direct of travel top of elastomer, and is 2mm or bigger from the beeline L of vertical dotted line H.Notice that above-mentioned " vertical curve " is the term that is used to limit oiling device of the present invention, and in the spinning of reality, this elastic filament can enter from (between α and β) between upper inclined surface 44 (lower bevel 45) and this vertical curve.
In addition, preferably, the maximum gauge of opening 41 is greater than the narrowest width (N among Fig. 8) of slot part 40.It is one trapezoidal that this slot part 40 can form its side-looking section, as shown in Figure 7, and as shown in Figure 8, when when the front is seen, this have slot part form can one from upward to narrowing down to the angled V-arrangement of the narrowest part adjacent with apex portion 43, and broaden with an inverted V-shaped angled towards the below.The sidewall of this slot part 40 forms a groove toward each other and with upper inclined surface and lower bevel; Yet this slot part 40 can have a flexure plane shape that does not have tangible sidewall.
Preferably, the width N of the narrowest part 46 of this slot part 40 is 0.1 to 1.5mm.This is because if the width N of the narrowest part 46 of this slot part 40 greater than 1.5mm, will be difficult to prevent the swing of the long filament in this slot part 40, and oiling tends to become inhomogeneous.In addition, preferably, this slot part 40 to the depth D of apex portion 43 is 3 to 10mm.Note, preferably, the maximum gauge of opening 41 than the minimum widith N big 0.2 of the narrowest part 46 of slot part 40 to 0.4mm.
The element 38 that oils with said structure remains on spun elastic filament and prevents in the groove that change in location from being reeled until them, and has reduced significantly owing to following the labile state that the into friction variation in holding point of direction (along the vertical curve direction of this elastomer) causes.
Guiding piece 39 can constitute: for example, as shown in Figure 9, along a direction that is parallel to elastic filament two pectinate plates 39 ', 39 ' are being set, and this elastic filament is by the gap between this broach.
Guiding piece 39 must be arranged to: the part of this elastic filament below the apex portion 43 of element 38 that oils has one greater than 0 ° and be not more than 3 ° back rake angle ε (see figure 7) with respect to the vertical dotted line H that draws from apex portion 43, and more preferably is a back rake angle ε who is not more than 2 °.As long as satisfy this requirement, without limits to shape of guiding piece 39 etc.
Preferably, owing to following reason, around the apex portion of the element 38 that oils and the surface roughness of guiding piece 39 be 2 to 10S.If this surface roughness is less than 2S, it is big that real contact area becomes, and friction becomes big.On the other hand, excessive if surface roughness becomes, it is big that capillary variation becomes, and keep the ability of oil to change easily.If surface roughness surpasses 10S, what tend to refuel is inhomogeneous.
In addition, this oiling device of the present invention is preferably used for elastomer, and wherein the long filament number is 2 or still less, and its overall fineness is 88dtex or littler.This be because if the long filament number greater than 2, the boundling state between long filament can change, and almost can not obtain effect of the present invention.When total fineness surpassed 88dtex, the part of not refueling appearred in a circumferential direction easily.When such part contacted with induction element, this long filament partly was subjected to excessive frictional resistance.
Table 3 and 4 shows the evaluation result of the melt spinning device with above-mentioned oiling device.
Table 3 shows the measurement result with the tension force of advancing of the long filament of 200% elongation of reeling when changing back rake angle ε.Table 4 shows the defective incidence of measuring in rolled long filament (cheese), promptly so-called step incidence (step-occurrence rate) when changing back rake angle ε.Be used for measuring the test of tension force of advancing, the feed speed of elastomer is set at 15.7 meters/minute, and Measuring Time is set at 1 minute, and the time set that is used to import data is 0.2 second/time.In table 3 and 4, A to L is corresponding to 12 cheeses (be cheese-form and be wound on elastic filament on the work beam).
Table 3
The advance mean value (g) of tension force 200
| A | B | C | D | E | F | G | H | I | J | K | L | AVE | MAX | MIN | R | | |
| 1 | 4.08 | 4.31 | 4.47 | 4.44 | 4.43 | 4.69 | 4.58 | 4.72 | 4.37 | 4.28 | 4.33 | 4.44 | 4.47 | 4.72 | 4.08 | 0.64 | 0.21 |
| 1.5 | 4.14 | 4.23 | 4.29 | 4.66 | 4.49 | 4.59 | 4.59 | 4.72 | 4.34 | 4.4 | 4.26 | 4.46 | 4.46 | 4.72 | 4.14 | 0.58 | 0.22 |
| 2 | 3.91 | 4.15 | 4.06 | 4.4 | 4.25 | 4.51 | 4.49 | 4.34 | 4.32 | 4.32 | 4.29 | 4.25 | 4.51 | 3.91 | 0.6 | 0.23 | |
| 2.5 | 4.15 | 4.4 | 4.46 | 4.62 | 4.52 | 4.64 | 4.8 | 4.85 | 4.7 | 4.61 | 4.51 | 4.57 | 4.56 | 4.85 | 4.15 | 0.7 | 0.23 |
| 3 | 4.22 | 4.48 | 4.57 | 4.81 | 4.61 | 4.66 | 4.84 | 4.79 | 4.77 | 4.71 | 4.53 | 4.83 | 4.62 | 4.84 | 4.22 | 0.62 | 0.21 |
| 4 | 4.22 | 4.51 | 4.6 | 4.97 | 4.68 | 4.64 | 4.95 | 5.07 | 4.87 | 4.6 | 4.68 | 4.85 | 4.71 | 5.07 | 4.22 | 0.85 | 0.28 |
| 5 | 4.18 | 4.59 | 4.65 | 4.97 | 4.66 | 4.82 | 4.97 | 5.33 | 4.96 | 4.67 | 4.67 | 4.95 | 4.77 | 5.33 | 4.18 | 1.15 | 0.34 |
| BL-A VE | 4.17 | 4.57 | 4.96 | 4.84 | 5.07 | 4.87 | 4.8 | 4.91 | 5.05 | 4.75 | 4.68 | 5.1 | 4.77 | 5.07 | 4.17 | 0.9 | 0.28 |
| BL | 4.28 | 4.62 | 5.08 | 4.91 | 5.1 | 4.96 | 4.97 | 5 | 4.96 | 4.71 | 4.65 | 4.92 | 4.87 | 5.1 | 4.28 | 0.82 | 0.28 |
Annotate:
AVE represents mean value;
MAX represents maximum;
MIN represents minimum of a value;
R is illustrated in the difference between maximum and the minimum of a value;
STDEV represents standard deviation.
Table 4
Step incidence (%)
| Angle/batch | A | B | C | D | E | F | G | H | I | | K | L | 12 batches | n | ||
| 1 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0.0 | 24 | ||
| 1.5 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0.0 | 203 | ||
| 2 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0.0 | 60 | ||
| 2.5 | 0 | 0 | 0 | 2.7 | 0 | 0.8 | 0 | 0 | 0 | 0 | 1.5 | 0 | 5.0 | 264 | ||
| 3 | 0 | 0 | 0 | 3.3 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 3.3 | 60 | ||
| 4 | 0 | 0 | 0 | 0 | 0 | 6.3 | 0 | 8.3 | 0 | 0 | 0 | 0 | 14.6 | 48 | ||
| 5 | 0 | 0 | 0 | 4.2 | 0 | 4.2 | 0 | 0 | 0 | 0 | 0 | 0 | 8.4 | 24 |
As clearly shown in Figure 3, reach 3 ° up to back rake angle ε, the tension force of advancing does not all almost change; Yet, when back rake angle ε becomes 4 ° or when bigger, it changes and becomes greatly.
Equally as clearly shown in Figure 4, when back rake angle ε surpasses 2 °, step (a kind of defective of the cheese of coiling) appears, and along with this stage incidence of increase of this back rake angle ε becomes big.According to table 4, back rake angle ε preferably is not more than 2 °; Yet what need only this back rake angle ε is not more than 3 °, just falls within the allowed band of practical operation.
Shown in clear in Fig. 3 and 4, according to above-mentioned evaluation test, oiling device of the present invention can be by using induction element to set for back rake angle ε greater than 0 ° and being not more than 3 ° of maximum and the difference between the minimum of a value and stage defectives that reduce the tension force of advancing.As a result, oiling device of the present invention can keep the elastic filament quality by spun elastic filament is contacted with guiding device so that oil is applied on the long filament, and prevents simultaneously because the frictional force that contact produces becomes excessive.
Then, a kind of below with reference to Fig. 2 and 10 explanations according to the device that is used to make elastomer of the present invention.
In the present embodiment, with a kind of melt spinning device that is used to make polyurethane elastomeric fiber of explanation.
Importantly, as shown in Figure 2, in this melt spinning device 4, a kind of spinneret 3 that is used to spin elastic filament W is arranged to extend along the direction of the axial direction that is basically parallel to a work beam 12, and the spinneret orifice 2 that is used to discharge elastic filament W is at regular intervals along the setting that vertically is in line of spinneret 3.
One is used for molten polymer and its extruder 5 that is extruded into spinneret 3 is passed through gear pump 6 being connected with spinneret 3.Almost under spinneret 3, be provided with a plurality of being used for elastic filament W is arranged to the induction element that waves 59 that is parallel to the alignment direction of spinneret orifice 2 and controls this long filament.As shown in Figure 10, the direction of the parallel longitudinal of induction element 59 edges and spinneret 3 is arranged on and makes on the supporting member 51 that the interval between the induction element 59 is bigger than the interval between the spinneret orifice 2.Thereby each elastic filament W is being reeled in the longitudinal extension of spinneret 3.Notice that it is 1.5 ° or littler with respect to maximum and the difference between the minimum of a value of the inclination angle λ of vertical curve that the distance between each induction element 59 is arranged to each elastic filament W.
In each induction element 59, be formed with the slot part 53 that an elastic filament W engages therein, and, in slot part 53 with the contacted part of elastic filament W in be formed with a jet pipe 55 that is used to discharge oil.In each jet pipe 55, as shown in Figure 2, oil is supplied with through a gear pump 57 from a fuel tank 59.In addition, the direction of exerting pressure that each jet pipe 55 is configured to continue to use in the induction element 59 that elastomer is tilted refuels to elastic filament W, and reason is as described below.Because each elastic filament W has a down dip and expansion downwards in the effect of induction element 59, be applied to that thread-tension on this long filament works so that this long filament returns towards the central authorities of supporting member 51, and this has increased the friction between induction element 59 and elastic filament in the direction.As mentioned above, discharge oil towards elastic filament W, can increase the effect of the friction of reduction and induction element 59 by direction of exerting pressure along induction element 59.Notice that in the present embodiment, oiling device of the present invention is made of a jet pipe 55, gear pump 57 and fuel tank 59.
As shown in Figure 2, be provided with a hair-dryer 7 between spinneret 3 and induction element 59, this hair-dryer blows cold wind along the direction vertical with the alignment direction of elastic filament W on elastic filament W.Below this induction element 59, be provided with 9,10 and work beams 12 of two godet rollers.They are arranged to the edge and extend with the direction of the parallel longitudinal of spinneret 3.With on winding filament to the silk volume 60 be by one in this long filament of guiding the lateral guides (not shown) along the axially reciprocating of this volume 60 carry out.
Below, a kind of use of explanation is had the elastic filament manufacture method of the device for spinning of above-mentioned setting.Polymer by an extruder 5 fusions is extruded to spinneret 3 by a gear pump 6 when its quantity delivered is conditioned, and spins elastic filament W downwards by spinneret orifice 2.This elastic filament W extends the distance of also expanding a little simultaneously therebetween along downward direction.After being refueled by an induction element 59, this elastic filament is being wound onto on two godet rollers 9,10 when the direction identical with the alignment direction of spinneret orifice 2 alignd.Then, after regulating its tension force by this godet roller 9,10, this elastic filament W delivers to a work beam 12, and is wound on the silk volume 60.
As mentioned above, according to present embodiment, because the alignment direction of the spinneret orifice 2 of spinneret 3 is arranged to be basically parallel to the axial of godet roller 9,10 and work beam 12, elastic filament W is wound onto on the work beam 12 with the alignment direction identical with the alignment direction of spinneret orifice 2, and can not make this row elastic filament produce deflection largely.Therefore, thus can reduce owing to the difference that acts on friction on the elastic filament and the tension force between elastic filament that the difference of each long filament road length causes after making this row elastic filament deflection and reduce therebetween differences of physical properties.Therefore, even when the silk volume that uses at the diverse location place of same device, also can prevent from striped etc. on cloth, to occur, thereby high-quality product is provided.
In addition, as shown in Figure 10, each elastic filament W is 1.5 ° or littler with respect to maximum and the difference between the minimum of a value of the inclination angle λ of induction element 59.This makes and can further reduce the difference of the frictional force that produces between elastic filament and make the physical property homogenising of respectively rolling up long filament between elastic filament W and induction element 59.
In the above-described embodiments, in induction element 59, refuel; Yet this oiling device can be arranged with this induction element in 59 minutes.As an oiling device, for example, can use a kind of wherein elastic filament be configured to its surface on be applied with the type that contacts of roller of oil.Yet, importantly this long filament with refuel before induction element 59 contacts, that is, refuel in the somewhere between spinneret orifice 2 and induction element 5.Thereby, can prevent from that elastic filament from not refueled and having under the state of a bigger coefficient of friction at it to contact with induction element 59.This has prevented that elastic filament is directed element and tangles and be damaged.
To the structure of this induction element without limits, as long as it can control waving of long filament, and therefore, except an induction element is provided for an elastic filament, can also be arranged to: for example, a plurality of grooves of formation and each groove guide an elastic filament in supporting member, or the like.
In the above-described embodiments, device for spinning of the present invention is used for making a kind of elastic polyurethane long filament by melt spinning; Yet this device can be used for other method, for example dry spinning and wet type spinning.
Can also use this device to make above-mentioned elastic polyurethane long filament elastic filament in addition.
The following describes example of the present invention and comparative examples about above-mentioned elastomer manufacturing installation.In example 5, use shown in Fig. 2 and 10 device and in comparative examples 9, use the device shown in Figure 11 and 12.
Device for spinning 81 shown in Figure 11 and 12 comprises that one has that a plurality of vertically the spinneret 3, one of the spinneret orifice 2 of alignment are used for being arranged on hair-dryer 7, the godet roller 9,10 between spinneret 3 and the oiling device 8 and being used for elastic filament W is wound to a work beam 69 on the volume 67 the oiling device that refuels 8, one along it in the downward direction guiding elastic filament W of spinneret 3.Aspect this, this device for spinning 81 has the identical structure of device as shown in Figure 2.Yet, the difference of its structure and device shown in Figure 2 be a guided rings 82, godet roller 9,10 and work beam 12 be configured to below the oiling device 8 its axially with spinneret 3 vertical between angle be 90 ° to utilize the space fully.
In device for spinning 81, make the elastic polyurethane long filament in the following manner with said structure.Molten polymer is extruded into spinneret 3 from an extruder (not shown), and elastic filament W discharges along direction substantially straight down from spinneret orifice 2.Each elastic filament W is by being blown cold wind cooling on it to be cured by hair-dryer 7, oil is applied on each elastic filament by oiling device 8, and this row elastic filament W turns to by guided rings 82.Its alignment direction therefore and the tension force of the elastic filament W of distortion is regulated by two godet rollers 9,10, this long filament is sent on the work beam 12 and is wound on the silk volume 60 then.
In above-mentioned example 5 and comparative examples 9, the diameter of spinneret orifice is set at 0.28mm, and spinning speed is set at 550m/min, and the resin melt temperature is set at 200 ℃, and this long filament is wound on 12 silk volumes.
Table 5 is illustrated in the stress ST value of the elastic polyurethane long filament in example 5 and the comparative examples 9.This stress ST value is the tension force of advancing of the elastic filament of the elongation 200% of reeling in the above described manner when with the supply of the speed of 15.7m/min.
Table 5
| The mean value (g) of the stress ST value of all volumes | At the maximum of stress ST value and poor (g) between the minimum of a value | |
| Example 5 | 4.4 | 0.7 |
| Comparative examples 9 | 4.8 | 1.6 |
Shown in above-mentioned table 5, the stress ST value that the higher average value of comparative examples 9 illustrates this elastic filament is bigger on the whole, and the maximum of stress ST value and the differential between the minimum of a value go out widely different between the elastic filament.On the other hand, in example 5, elastic filament extends largely, and therefore stress ST value is less on the whole, compares with comparative examples 9, and the difference of stress ST value is very little.As mentioned above, the device that is used to make elastic filament obviously according to the present invention compared with prior art can provide more uniform elastic filament.
As mentioned above, according to the device that is used to make elastic filament of the present invention, because elastic filament from the alignment direction of the spinneret orifice of its discharge be basically parallel to work beam axially, can not make this row's elastic filament produce deflection largely so elastic filament can the alignment direction identical with spinneret orifice be wound on the work beam.Therefore, can reduce the tension difference between elastic filament, and this difference is in the prior art owing to act on frictional force difference on the elastic filament and the problem that difference caused of long filament road length.Thereby can reduce differences of physical properties between elastic filament.Therefore,, also can prevent on cloth, to have a striated pattern etc., have high-quality product thereby provide even use the different silks in same device to roll up.
Make that by induction element elastic filament W is 1.5 ° or littler with respect to the maximum and the difference between the minimum of a value at the inclination angle of vertical curve.This feasible physical property homogenising that can be reduced in the difference of the frictional force in the elastic filament further and make the long filament in each volume.
In addition, continue to use, can obtain following effect thus so that the direction of exerting pressure of the induction element that elastomer tilts is applied to oil on the elastic filament.Each elastic filament W is by this induction element and in its long filament road medium dip, and therefore is subjected to along the tension force that is back to the direction in this precursor road, and this make in the direction and induction element 59 between frictional force become big.As mentioned above, this can by along induction element with respect to the direction of exerting pressure of elastic filament W refuel reduce and induction element between frictional force.
Claims (9)
1. device that is used to make elastomer, it comprises:
One has the spinneret of a plurality of spinneret orifices; With
A work beam that is used to reel from the spun elastic filament of this spinneret orifice; Wherein,
Described a plurality of spinneret orifice is in line and is arranged to the axially substantially parallel of its alignment direction and this work beam; With
This device that is used to make elastomer also comprises:
Being arranged on being used between spinneret orifice and the work beam will guide to the induction element of work beam from the spun elastic filament of spinneret orifice along substantially straight down direction, wherein,
This induction element is arranged in therebetween interval width greater than the interval width between spinneret orifice, and to be arranged to make the maximum and the difference between the minimum of a value with respect to the inclination angle of vertical curve of elastic filament be 1.5 ° or littler, this inclination angle is created between spinneret orifice and the induction element, and described difference is owing to the interval difference between the spinneret orifice and between the induction element produces.
2. the device that is used to make elastomer according to claim 1, it is characterized in that it comprises that also one is arranged between spinneret orifice and the induction element to continue to use so that the oiling device that the direction of exerting pressure of the induction element that elastic filament tilts refuels to this elastic filament.
3. the device that is used to make elastomer according to claim 1 is characterized in that, described spinneret comprises a plurality of spinneret orifices that are formed in the single spinning plate, and described spinneret orifice is set to become substantially delegation.
4. the device that is used to make elastomer according to claim 3 is characterized in that, described spinneret has 8 or more a plurality of spinneret orifice.
5. the device that is used to make elastomer according to claim 3 is characterized in that, it comprises that one is used for cold wind is applied to fan on the described long filament along the direction that is basically perpendicular to the surface that comprises the long filament of discharging from a spinneret.
6. a method that is used to make elastomer is characterized in that,
Be wound onto a work beam with rotation of the alignment direction that is basically parallel to spinneret orifice from the spun elastic filament of spinneret with a plurality of spinneret orifices of arranging of being in line;
Induction element is arranged between spinneret and the work beam, and the interval width between the induction element is greater than the interval width between the spinneret orifice simultaneously;
Induction element guides to work beam along direction substantially straight down with elastic filament; With
The maximum and the difference between the minimum of a value with respect to the inclination angle of vertical curve of elastic filament are 1.5 ° or littler, and this inclination angle is created between spinneret orifice and the induction element, and described difference is owing to the interval difference between the spinneret orifice and between the induction element produces.
7. the method that is used to make elastomer according to claim 6 is characterized in that, continues to use so that the direction of exerting pressure of the induction element that elastic filament tilts refuels to this elastic filament.
8. the method that is used to make elastomer according to claim 6 is characterized in that, described elastomer has 2 or long filament still less, and total fineness is 88dtex or littler.
9. the method that is used to make elastomer according to claim 6 is characterized in that, described elastomer is the melt spinning elastomer.
Applications Claiming Priority (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP397133/2001 | 2001-12-27 | ||
| JP2001397133A JP3888436B2 (en) | 2001-12-27 | 2001-12-27 | Elastic fiber manufacturing apparatus and manufacturing method |
| JP2001399245A JP2003201619A (en) | 2001-12-28 | 2001-12-28 | Apparatus for applying finishing agent for elastic fiber |
| JP399245/2001 | 2001-12-28 | ||
| JP57712/2002 | 2002-03-04 | ||
| JP57713/2002 | 2002-03-04 | ||
| JP2002057713A JP2003253521A (en) | 2002-03-04 | 2002-03-04 | Spinneret and method for producing synthetic fiber using the same |
| JP2002057712A JP2003253520A (en) | 2002-03-04 | 2002-03-04 | Spinneret |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1608149A CN1608149A (en) | 2005-04-20 |
| CN1324172C true CN1324172C (en) | 2007-07-04 |
Family
ID=27482752
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB028260287A Expired - Fee Related CN1324172C (en) | 2001-12-27 | 2002-11-29 | Spinneret, oiling device, production device and production method for synthetic fibers |
Country Status (5)
| Country | Link |
|---|---|
| CN (1) | CN1324172C (en) |
| AU (1) | AU2002349612A1 (en) |
| ES (1) | ES2267369B2 (en) |
| TW (1) | TW200301324A (en) |
| WO (1) | WO2003060204A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104313815A (en) * | 2014-11-07 | 2015-01-28 | 浙江尤夫高新纤维股份有限公司 | Polyester industrial yarn functional assistant multi-channel oil nozzle oiling device |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5448901B2 (en) * | 2010-02-15 | 2014-03-19 | Ｔｍｔマシナリー株式会社 | Oil diffusion device and spinning winder |
| CN102926002A (en) * | 2011-08-11 | 2013-02-13 | 苏州一丞咨询服务有限公司 | Oiling device for fine-denier spinning |
| JP5855283B2 (en) * | 2012-01-24 | 2016-02-09 | エーリコン テクスティル ゲゼルシャフト ミット ベシュレンクテル ハフツング ウント コンパニー コマンディートゲゼルシャフトＯｅｒｌｉｋｏｎ Ｔｅｘｔｉｌｅ ＧｍｂＨ ＆ Ｃｏ． ＫＧ | Device for wetting multiple yarns |
| CN103305938A (en) * | 2013-06-25 | 2013-09-18 | 苏州锦凯纺织有限公司 | Novel oiling equipment for pre-oriented yarn |
| CN104976877B (en) * | 2015-07-10 | 2017-03-08 | 广东溢达纺织有限公司 | Contaminate drying frame |
| JP7186006B2 (en) * | 2018-02-05 | 2022-12-08 | Ｔｍｔマシナリー株式会社 | Lubrication guide and spinning take-up device |
| CN108265340A (en) * | 2018-03-06 | 2018-07-10 | 杨晓波 | Nano-fiber manufacturing apparatus |
| CN108823664A (en) * | 2018-09-29 | 2018-11-16 | 安徽和邦纺织科技有限公司 | A kind of use for laboratory spinning equipment |
| CN109097845A (en) * | 2018-11-12 | 2018-12-28 | 长兴盛纺织有限公司 | A kind of transmission traction device of chemical fiber wire |
| DE102019001484A1 (en) * | 2019-03-02 | 2020-09-03 | Oerlikon Textile Gmbh & Co. Kg | Preparation thread guide |
| JP7475004B2 (en) * | 2020-02-12 | 2024-04-26 | Ｔｍｔマシナリー株式会社 | Oil application guide and spinning take-off machine |
| CN113252225A (en) * | 2021-04-13 | 2021-08-13 | 武汉纺织大学 | Bundling tension detection system |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3001230A (en) * | 1959-01-29 | 1961-09-26 | Eltherma A G | Spinnerette nozzles |
| US3059991A (en) * | 1959-03-20 | 1962-10-23 | E B & A C Whiting Company | Method of making oriented filamentary article of isotactic polypropylene |
| JPS61245307A (en) * | 1985-04-23 | 1986-10-31 | Toray Ind Inc | Production of specific filament of polyester |
| JPH05230706A (en) * | 1992-02-17 | 1993-09-07 | Toyobo Co Ltd | Finish applicator |
| US5330338A (en) * | 1992-02-17 | 1994-07-19 | Toyo Boseki Kabushiki Kaisha | Apparatus for spinning of polyurethane elastic filaments |
| US5362433A (en) * | 1986-12-17 | 1994-11-08 | Viscosuisse S.A. | Process of making polyurethane elastomer thread |
| US5387387A (en) * | 1993-09-30 | 1995-02-07 | Alex James & Associates, Inc. | Method and apparatus for dry spinning spandex |
| JPH10280224A (en) * | 1997-04-10 | 1998-10-20 | Teijin Ltd | Nozzle for impacting finishing agent |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS3610507B1 (en) * | 1959-04-03 | 1961-07-14 | ||
| JPS4416325Y1 (en) * | 1966-09-28 | 1969-07-15 | ||
| GB1415947A (en) * | 1972-09-11 | 1975-12-03 | Autlmatik Apparate Maschinenba | Spinning machines for producing and reeling synthetic fibres |
| DE4336097A1 (en) * | 1993-10-22 | 1995-04-27 | Bayer Ag | Continuous process for melt spinning monofilament threads |
| DE10046220A1 (en) * | 1999-11-18 | 2001-05-23 | Barmag Barmer Maschf | Melt spinning of filaments from spinning packs arranged in a circle includes guiding of yarns into a linear arrangement before further treatment |
-
2002
- 2002-11-29 WO PCT/JP2002/012475 patent/WO2003060204A1/en active IP Right Grant
- 2002-11-29 CN CNB028260287A patent/CN1324172C/en not_active Expired - Fee Related
- 2002-11-29 TW TW091134868A patent/TW200301324A/en unknown
- 2002-11-29 ES ES200450038A patent/ES2267369B2/en not_active Expired - Fee Related
- 2002-11-29 AU AU2002349612A patent/AU2002349612A1/en not_active Abandoned
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3001230A (en) * | 1959-01-29 | 1961-09-26 | Eltherma A G | Spinnerette nozzles |
| US3059991A (en) * | 1959-03-20 | 1962-10-23 | E B & A C Whiting Company | Method of making oriented filamentary article of isotactic polypropylene |
| JPS61245307A (en) * | 1985-04-23 | 1986-10-31 | Toray Ind Inc | Production of specific filament of polyester |
| US5362433A (en) * | 1986-12-17 | 1994-11-08 | Viscosuisse S.A. | Process of making polyurethane elastomer thread |
| JPH05230706A (en) * | 1992-02-17 | 1993-09-07 | Toyobo Co Ltd | Finish applicator |
| US5330338A (en) * | 1992-02-17 | 1994-07-19 | Toyo Boseki Kabushiki Kaisha | Apparatus for spinning of polyurethane elastic filaments |
| US5387387A (en) * | 1993-09-30 | 1995-02-07 | Alex James & Associates, Inc. | Method and apparatus for dry spinning spandex |
| JPH10280224A (en) * | 1997-04-10 | 1998-10-20 | Teijin Ltd | Nozzle for impacting finishing agent |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104313815A (en) * | 2014-11-07 | 2015-01-28 | 浙江尤夫高新纤维股份有限公司 | Polyester industrial yarn functional assistant multi-channel oil nozzle oiling device |
Also Published As
| Publication number | Publication date |
|---|---|
| TW200301324A (en) | 2003-07-01 |
| ES2267369B2 (en) | 2007-11-16 |
| ES2267369A1 (en) | 2007-03-01 |
| CN1608149A (en) | 2005-04-20 |
| WO2003060204A1 (en) | 2003-07-24 |
| AU2002349612A1 (en) | 2003-07-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1324172C (en) | Spinneret, oiling device, production device and production method for synthetic fibers | |
| CN1272490C (en) | Apparatus for high speed beaming of elastomeric yarns | |
| CN1934303A (en) | Spun isotropic pitch-based carbon fiber yarn, composite yarn and woven fabric made by using the same, and processes for the production of them | |
| CN1279229C (en) | Method for producing polyester filament yarn | |
| WO2006001324A1 (en) | Spinning pack for dry-wet spinning, diverting guide for fiber bundle, and apparatus and method for producing fiber bundle | |
| CN1225573C (en) | Apparatus and method for spinning polymeric filaments | |
| CN1195910C (en) | Poly (trimethylene terephthalate) modified cross-section yarn | |
| CN110117827B (en) | Oil supply guide and spinning draft device | |
| CN1950552A (en) | Spinning poly(trimethylene terephthalate) yarns | |
| CN1771357A (en) | Spin annealed poly (trimethylene terephthalate) yarn | |
| CN1192961C (en) | Stretched yarn pirn | |
| JP5262834B2 (en) | Method and apparatus for producing ultrafine synthetic fiber comprising multi-threads | |
| CN1462323A (en) | Production method of synthetic fiber and yarn traverse device | |
| EP2072647B1 (en) | Draft roller | |
| CN1214137C (en) | Poly(trimethylene terephthalate) multifilament yarn | |
| JP2010070887A (en) | Cooling device for spinning and melt-spinning method | |
| CN1210449C (en) | Method for spinning and winding of polyester filaments using spinning additives, polyester filaments obtained by spinning method, draw texturing of polyester filaments and bulked polyester filaments | |
| JP2008057085A (en) | Method and apparatus for producing polyamide monofilament | |
| US7076840B2 (en) | Draft device | |
| JP3774810B2 (en) | Manufacturing method of spinneret pack | |
| JP6701822B2 (en) | Melt spinning pack | |
| CN101525773B (en) | Pre-network device for polyamide composite filaments | |
| JP2007009342A (en) | Method for producing synthetic multifilament yarn | |
| CN1584136A (en) | Production of thin fibers | |
| KR20110065743A (en) | Producing process of a monofilament using a seperating guide |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070704 Termination date: 20101129 |