CN102704020A - Method and composite spinning component for preparing ferris wheel sea island composite filaments - Google Patents
Method and composite spinning component for preparing ferris wheel sea island composite filaments Download PDFInfo
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Abstract
The invention relates to a method and a composite spinning component for preparing ferris wheel sea island composite filaments. The method comprises the following steps of: allowing two molten component phases to pass through the composite spinning component and converge at the inlets of spinneret orifices by a double screw composite spinning method, extruding strands together, cooling, oiling, and winding to obtain a semi-finished product, namely undrawn yarns (UDY); and drawing to obtain a finished product, namely draw textured yarns (DTY), or performing drawing deformation to obtain DTY ferris wheel sea island composite filaments, wherein one phase is an unfixed island component blend of polyethylene (PE) and polyamide (PA) in a blending ratio of 50:50-60:40, and the other phase is fixed island component polymer which can be subjected to melt spinning and is resistant to toluene and dimethyl formamide (DMF) solvents. In the used composite spinning component, each needle tube on a needle tube plate is concentric with and in one-to-one correspondence to each spinneret orifice on a spinneret plate, and 2 to 32 inverted U-shaped slits are formed at one end of each needle tube, which is provided with an outlet, and are directly contacted with the surface of the spinneret plate. The cross section of the prepared fibers is like a ferris wheel, a fixed island is arranged on an outer layer, and the rest is unfixed sea island composite filaments.
Description
Technical field
The present invention relates to a kind of manufacturing approach of fabric of island-in-sea type bicomponent filament yarn and the composite spining module of use thereof.
Background technology
Islands-in-sea bicomponent fibre is a kind of polymer with the form of a plurality of superfine fentos (being referred to as the island) among another kind of polymer (being referred to as the sea).
The production of present fabric of island-in-sea type bicomponent filament yarn all is to adopt the island method of deciding, and is promptly passed through the fusion respectively of twin-screw composite spinning machine, is got into the fabric of island-in-sea type filament spinning component by two kinds of polymer, and island phase and marine facies converge ejection through path separately in the porch of spinneret orifice respectively; Form islands-in-sea type fibre; Its island phase and marine facies are continuous, equally distributed at the length direction of fiber, and the island number is fixed, generally more than 37 islands; It normally decides island component with PET or the conduct of PA6 raw material; Water-soluble polyester COPET is as extra large component, and the extra large component of the composite fibre of producing in this way and the ratio of island component are generally 30: 70 or 20: 80, and the content of island component is higher.
In this fabric of island-in-sea type spinnerets, the monofilament on 37 islands is that the high polymer melt thread by the ejection of 37 needle tubing groups is condensed into fibre, and needle tubing and needle plate adopt close-fitting to merge auxilliaryly with the Laser Welding reality needle tubing can not to be come off usually.If spinnerets is 200 holes; Corresponding is 200 needle tubing groups; Every group of 37 needle tubings (amounting to 7400 needle tubings) are corresponding with 200 groups every group 37 pod apertures (amounting to 7400 pod apertures) of deflector; Each needle tubing cooperates concentricity must have high accuracy could satisfy the requirement of spinning islands-in-sea type fibre very much with pod apertures, the island just can be evenly distributed on marine and adhesion, and machining accuracy height, the expense of therefore deciding needle tubing plate, deflector and spinnerets in the assembly of island are big; In the cleaning and assembling process of assembly since the needle tubing plate be prone to bump, yielding, maintenance cost is also high.The island number is many more, and the perforate of spinnerets is few more, and production capacity is low more, invests bigger.
Indefinite island method is produced islands-in-sea bicomponent fibre, and slices of caprone PA6 commonly used and low density polyethylene mix under uniform temperature and condition, through same screw extruder fusion, blend, again through measuring pump, filament spinning component ejection, forms the superfine fibre on indefinite island.Its island of islands-in-sea type fibre that this kind method is produced is mutually discontinuous, fixing, i.e. the length on island and be distributed in and have randomness in the certain limit, so this fiber only is applied in the production of staple fibre at present; The ratio of island phase component is lower in this kind production method; Generally about 50%, if reach 55% when above, the island irregular abnormal shape (king-sized island or island and island adhesion) will occur mutually; But because the production of this fiber employing is conventional filament spinning component; Production cost is low, and output is high, therefore on the microfiber synthetic leather base cloth, still has more widely and uses.
Summary of the invention
The present invention is intended to propose the production method that a kind of cross section is a ferris wheel type island bicomponent filament yarn.
The present invention is intended to propose a kind of employed composite spining module of production ferris wheel type island bicomponent filament yarn that is used for, and the fiber cross section that makes is as ferris wheel, and skin has a delineation island, all the other are the fabric of island-in-sea type bicomponent filament yarn on indefinite island.
The present invention is intended to propose a kind of composite spining module of production ferris wheel type bicomponent filament yarn, and assembly integral body is surrounded by upper and lower casing, and agent structure is followed successively by upper cover plate, distribution plate 1, distribution plate 2, needle tubing plate and spinnerets.Its characteristic one is that each the needle tubing hole on the needle tubing plate is concentric with each spinneret orifice on the spinnerets and corresponding one by one; Outlet one end that its characteristic two is needle tubings is processed to 2～32 " ∩ " shape slits, and directly contacts with spinning plate surface, and the spinnerets inner face is the plane.
In this composite spining module; The blend melt of indefinite island component flows into the needle tubing hole from the upper end of needle tubing plate; And " ∩ " shape slit of the melt of deciding island component between needle tubing plate and the spinnerets through the needle tubing lower end from around flow to and merge in the spinneret orifice porch with indefinite island component melt; Together extrude tow, finally form a delineation island is arranged in the skin, all the other are the ferris wheel type island composite fibre in cross section, indefinite island." ∩ " shape slit number in needle tubing exit is exactly to decide the island number in the ferris wheel fiber type; When selecting different to decide the island when counting, only need select the needle tubing plate of correspondence " ∩ " shape slit number for use.
The manufacturing approach of this ferris wheel type bicomponent filament yarn is following: use twin-screw composite spinning equipment; Adopt twin-screw composite spinning method; The component that makes two kinds of fusions merges in the spinneret orifice porch through above-mentioned composite spining module, together extrudes tow; Through cool off, oil, reeling makes semi-finished product UDY silk, again drawn process finished product DT or again drawn be out of shape and process DTY ferris wheel type bicomponent filament yarn; Wherein indefinite island component is that mixed proportion is PE and the blend of PA between 50: 50 to 60: 40, and deciding island component is a kind of anti-again toluene of melt spinning and high polymer of DMF solvent of carrying out.
Principle of the present invention is: when the melt of deciding island component from around flow to " ∩ " shape slit and indefinite island component converges, when flowing to spinneret orifice simultaneously; Because the melt flow index of indefinite island component is than the height of deciding island component; " low sticking Kelvin effect principle " according to melt in the composite spinning process; In spinneret orifice; The melt of indefinite island component can surround gradually each through " ∩ " shape slit decide the island melt, form finally that a kind of cross section skin has a delineation island (decide the island number and equal " ∩ " shape slit number), all the other are the ferris wheel type island bicomponent filament yarn in cross section, indefinite island.
In the manufacturing approach of this ferris wheel type island bicomponent filament yarn; The fiber number of the finished fiber that makes is 55～330dtex/24～96F; The filament number of finished fiber is 2～10dtex, and behind organic solvent extraction LDPE component, the filament number of deciding after island component separates is 0.02～0.5dtex.Adopt mixed proportion be PE between 50: 50 to 60: 40 with after the blend of PA separates, what stay is that filament number is the indefinite island fiber of 0.001～0.20dtex.
Tricot, loop bonding nonwoven fabric or shoe with this long filament is made into are netted the composite acupuncture nonwoven fabric; After polyurethane coating or dipping technique processing; Dissolve with organic solvent and remove LDPE, what stay fibrous outer decides island and remaining indefinite island fento component, finally can make superfine fibre artificial leather base cloth ventilative, soft approximate dermis; Through napping processing, can make high-grade artificial suede with " writing effect "; As carry out veneer processing, can make high-grade emulational leather etc.
Description of drawings
Fig. 1 is a ferris wheel type island continuous yarn spinning assembly shaping schematic diagram;
Fig. 2 is along the cutaway view of E-E among Fig. 1;
Fig. 3 is the spinning technique flow chart;
Fig. 4 is the drawing process flow chart.
Among Fig. 1, the 1st, needle tubing plate, the 2nd, needle tubing, the 3rd, " ∩ " shape slit of the needle tubing port of export, the 4th, spinnerets; The 5th, decide the inlet of island component, the 6th, the inlet of indefinite island blend;
The specific embodiment
In the manufacturing approach of this ferris wheel type island bicomponent filament yarn; Adopt twin-screw composite spinning method; The component that makes two kinds of fusions merges in the spinneret orifice porch through composite spining module shown in Figure 1, together extrudes tow; Through cool off, oil, reeling makes semi-finished product UDY silk, again drawn process finished product DT or again drawn be out of shape and process DTY ferris wheel type island bicomponent filament yarn; Wherein deciding island phase component is any anti-again toluene of melt spinning and high polymer of DMF solvent of carrying out, and indefinite island is that mixed proportion is PE and the blend of PA between 50: 50 to 60: 40 mutually.
In the manufacturing approach of this ferris wheel type island bicomponent filament yarn, it is the low density polyethylene of 50～70MFI and the blend of the polyamide fibre PA6 that relative viscosity is 2.6～3.2 η that indefinite island component uses melt index.Deciding the island number and can be 2～32 in the composite fibre of this ferris wheel type island, the weight ratio of deciding island and indefinite island two-phase component can be 20/80～40/60, finally can obtain the superfine fibre that line density is 0.001～0.5dtex.
In the manufacturing approach of this ferris wheel type island bicomponent filament yarn, when deciding island component employing PA6, the melt temperature of PA6 component can be controlled in 270～280 ℃, and the melt temperature of indefinite island PA6+PE blend is controlled at 265 ℃～285 ℃.
In the manufacturing approach of this ferris wheel type island bicomponent filament yarn, when deciding island component employing PET, the melt temperature of PET component can be controlled in 280～290 ℃, and the melt temperature of indefinite island PA6+PE blend is controlled at 265 ℃～285 ℃.
In the manufacturing approach of this ferris wheel type island bicomponent filament yarn, when deciding island component employing PTT, the melt temperature of PTT component can be controlled in 255～265 ℃, and the melt temperature of indefinite island PA6+PE blend is controlled at 265 ℃～285 ℃.
In the manufacturing approach of this ferris wheel type island bicomponent filament yarn, when deciding island component employing antibacterial deodourizing PET section, the melt temperature of antibacterial deodourizing PET component can be controlled in 270～285 ℃, and the melt temperature of indefinite island PA6+PE blend is controlled at 265 ℃～285 ℃.
In the manufacturing approach of this ferris wheel type island bicomponent filament yarn, decide island component and adopt high contraction of modified PET to cut into slices, the high melt temperature that shrinks PET of modification can be controlled to be 270～285 ℃, and the melt temperature of indefinite island PA6+PE blend is controlled at 265 ℃～285 ℃.
The concrete technological principle of the manufacturing approach of this ferris wheel type island bicomponent filament yarn and the composite spining module of use thereof and flow process such as Fig. 1, Fig. 2, Fig. 3 and shown in Figure 4.
In the composite spining module that this ferris wheel type island bicomponent filament yarn uses, the needle tubing of importing indefinite island component melt directly contacts with spinning plate surface, and an end of contact can be decided its ∩ shape slit number of island number processing as required.In this programme, select respectively that ∩ shape slit number is 16,12,8 three kind of specification for use, the spinnerets hole count is respectively 48 holes and 84 holes, and the spinnerets micro-pore diameter is 0.30mm.Screw rod and measuring pump are by variable frequency regulating speed control, and each district of screw rod and spin manifold temperature are controlled automatically.
The concrete technological parameter of the manufacturing approach of this ferris wheel type island bicomponent filament yarn and the composite spining module of use thereof is following:
1. chip drying
In the blend: low density polyethylene itself is not moisture, and PA6 directly uses the dry good dried section of manufacturer, does not absorb water feeding intake and measure in the mixed process in order to guarantee two kinds of raw materials, guarantees that spinning is smooth, and drying tower 1 bottom feeds 0.3m
3/ hour dew point for-60 ℃, temperature is 40 ℃ dry N
2Gas is protected, and the dried section of PA6 moisture content is controlled at below the 700ppm during spinning.
PA6 does section: PA6 and uses the dry good dried section of manufacturer, feeds 0.3m during use in drying tower 2 bottoms
3/ hour dew point for-60 ℃, temperature is 60 ℃ dry N
2Gas carries out dry-run protection, and the section moisture content is controlled at below the 500ppm.
PET, antibacterial deodourizing PET, the high contraction section of modified PET, the conventional section of PTT; The preceding process of use Britain Rosion company fluidized bed type section pre-crystallizer and filling drying tower use dew point are that-60 ℃ heating dry air carries out drying, and the moisture content of cutting into slices is controlled at below the 100ppm.
2. spinning technology parameter:
The raw material weight ratio: the weight ratio of deciding island and indefinite island two-phase component can be 20/80～40/60.
Measuring pump specification: decide island component 0.6cc/rev, indefinite island component 1.2cc/rev;
Calculate according to finished product fiber number, proportioning raw materials, PA6 is at 280 ℃ of following fusant density 1.04g/cm
3, PET is at 285 ℃ of following fusant density 1.13g/cm
3, the blend of LDPE+PA6 is at 275 ℃ of following fusant density 0.875g/cm
3
Screw speed: screw speed is pressure controlled by filter outlet, produces the middle filtrator outlet pressure and is controlled to be: PA6, PET, modified PET, PTT 100bar; LDPE+PA6 90bar;
Screw rod is respectively distinguished temperature and is set: 130～285 ℃ of LDPE+PA6,
PA6?220～280℃，
PET?260～290℃，
PTT?200～265℃，
260～285 ℃ of antibacterial deodourizing PET sections;
The high contraction of modified PET cut into slices 260～285 ℃;
Lateral blowing temperature: 16 ℃～22 ℃;
The extractor fan exhausting wind speed of manifold bottom: 1.0m/ second, so that get rid of the monomer that PA6, PE spinning volatilize;
Spinning speed: 300～800m/min.
3. winding process parameter:
Upper oil-pan rotating speed: 15～30rpm/min;
Oil concentration is: the aqueous solution that 6.0% polyamide fibre or terylene are oil solution dedicated;
Draw-off godet speed: 300～800m/min
Winding speed: 300～800m/min;
4. drawing parameter:
Draw speed: 100～200m/min;
Temperature of heat plate: 60 ℃～90 ℃;
Heater temperature: 70 ℃～100 ℃;
Drawing medium: hot-air;
Draw ratio: 3.0～4.0;
5. fibrous finished product performance:
Fiber number: 55～330dtex/24～96F, the filament number of finished fiber is 2～10dtex;
Isolated indefinite island filament number: 0.001～0.20dtex in the blend component;
Decide island component and separate back filament number: 0.02～0.5dtex;
Fracture strength: 2.5～5.0CN/dtex;
Elongation at break: 30～90%.
The manufacturing approach of this ferris wheel type island bicomponent filament yarn and the composite spining module of use thereof have following advantage:
1. the long filament of processing with the composite spining module of the manufacturing approach of this ferris wheel type island bicomponent filament yarn and use thereof: it decides the island number can be 2～32; (deciding island+indefinite island) can be 52/48～70/30 with the weight ratio of marine facies component; Decide island fabric of island-in-sea type bicomponent filament yarn relatively with this manufacturing approach; Its composite spining module simple in structure, therefore processing cost is low, invests relatively low.
2. the long filament of processing with the composite spining module of the manufacturing approach of this ferris wheel type island bicomponent filament yarn and use thereof; After solvent is extracted LDPE out; The filament number of indefinite island fento is 0.001～0.20dtex, and the filament number of deciding the island is 0.02～0.50dtex, has concurrently more less than the ultra-fine indefinite island fiber below the 0.05dtex in this fiber; With the matte series products such as artificial suede that this fiber is processed, the product of comparing 37 islands or 51 islands has better velvet and sense of touch.
3. the long filament of processing with the composite spining module of the manufacturing approach of this ferris wheel type island bicomponent filament yarn and use thereof; Decide island component and select different raw materials for use; The product of being produced just has different styles, for superfine fibre artificial leather base cloth provides more development space.For example, when deciding island component and using the PET composition, because the extension at break of PET superfine fibre is littler than PA6, so this type base cloth is more suitable for being used as high-strength flatness type product, like automobile-used leather.If use the PTT composition, because PTT is a highly elastic fiber, the base cloth good springiness of being produced can be used as the clothing leather lining.If use antibacterial deodourizing PET composition, then base cloth has anti-bacterial anti-foul function.Modified PET is high to shrink section if use, and can or carry out the form of netting the composite acupuncture nonwoven fabric through the loop bonding nonwoven fabric, produces the artificial leather base cloth of thick type, highly dense, feel ultra-soft.
The production technology of embodiment 1:PA6/ (PA6+LDPE) ferris wheel type island bicomponent filament yarn
(a) spinning material:
Decide island component: the PA6 section, trade mark M32600, relative viscosity is 2.6 η; Guangzhou Xin Huimei synthetic fibre reaches limited company and produces.
The blend of LDPE+PA6: melt index is that LDPE and the viscosity of 60MFI is the blend of the PA6 of 2.8 η, wherein: LDPE, trade mark 1I60A, melt index is 60, Yanshan Petrochemical branch company in Beijing produces.
Slices of caprone, trade mark M32800, relative viscosity is 2.8 η;
(b) proportioning raw materials: weight ratio: PA6/ (PA6+LDPE)=30/ (35+35);
(c) spinnerets specification: hole count * ∩ figurate number * aperture is 48 * 16 * 0.30mm;
(d) screw extruder specification: decide island component φ 65, indefinite island component φ 90;
(e) measuring pump specification: decide island component 0.6cc/rev, indefinite island component 1.2cc/rev;
(f) cooling air temperature: 18 ℃, wind speed: 0.6m/s;
(g) upper oil-pan rotating speed: 26rpm/min, oil concentration is: 6.0%;
(h) spinning (coiling) speed: 600m/min;
(i) spinning technique transitivity:
UDY ferris wheel type island, island bicomponent filament yarn spinning technique table is decided in table 1 528dtex/48F * 16
UDY ferris wheel type island, island bicomponent filament yarn physical property measurement data are decided in table 2:528dtex/48F * 16
| Specification | Fracture strength cn/dtex | Elongation at break % | Oil content % |
| The island is decided in 528dtex/48F * 16 | 1.58 | 317.3 | 1.63 |
(j) drawing process transitivity:
Drawing process is set: effectively draw ratio is 3.2, and temperature of heat plate is 75 ℃, and heater temperature is 90 ℃, draw speed 200m/min.
Table 3: superfine fibre number in stretch back DT silk physical property measurement data and the cross section
Tricot that is made into this ferris wheel type island bicomponent filament yarn or the nonwoven fabric of processing, adopt polyurethane impregnated or coating technology to fabric treating after, extract PE out; Process superfine fibre artificial leather base cloth, have the PA6 of 30% ratio to decide the island fiber owing to open in the fiber behind the fibre, because of deciding island fibre fluff length homogeneous, being evenly distributed; Its artificial leather base cloth surface of processing is after napping is handled, and the fine hair on surface is even relatively, and the feel of wool is strong; The filoplume difficult drop-off; Also be difficult for balling-up, the superfine fibre of indefinite island part has then strengthened the sense of touch of product exquisiteness and closely knit elastic sensation, and the high-grade artificial suede of using this fiber to process has well " writes effect ".
The spinning technique of embodiment 2:PET/ (PA6+LDPE) ferris wheel type island bicomponent filament yarn
(a) spinning material:
Decide island component: PET terylene chips, viscosity are 0.64dl/g; Yizheng Fiber Optical plant Co., Ltd produces.
The blend of LDPE+PA6: melt index is that LDPE and the viscosity of 60MFI is the blend of the PA6 of 2.8 η, wherein: LDPE, trade mark 1I60A, melt index is 60, Yanshan Petrochemical branch company in Beijing produces.
Slices of caprone, trade mark M32800, relative viscosity is 2.8 η; Guangzhou Xin Huimei synthetic fibre reaches limited company and produces.
(b) proportioning raw materials: weight ratio: PET/ (PA6+LDPE)=35/ (32+33);
(c) spinnerets specification: hole count * ∩ figurate number * aperture is 36 * 12 * 0.30mm;
(d) screw extruder: decide island component φ 65, indefinite island component φ 90;
(e) measuring pump specification: decide island component 0.6cc/rev, indefinite island component 1.2cc/rev;
(f) cooling air temperature: 19 ℃, wind speed: 0.6m/s;
(g) upper oil-pan rotating speed: 22rpm/min, oil concentration is: 6.0%;
(h) spinning (coiling) speed: 600m/min;
(i) spinning technique transitivity:
UDY ferris wheel type island, island bicomponent filament yarn spinning technique table is decided in table 4 374dtex/36F * 12
UDY ferris wheel type island, island bicomponent filament yarn physical property measurement data are decided in table 5 374dtex/36F * 12
| Specification | Fracture strength cn/dtex | Elongation at break % | Oil content % |
| The island is decided in 374dtex/36F * 12 | 1.27 | 358.9 | 1.45 |
(j) drawing process transitivity:
Drawing process is set: effectively draw ratio is 3.4, and temperature of heat plate is 70 ℃, and heater temperature is 90 ℃, draw speed 200m/min.
Table 6: superfine fibre number in stretch back DT silk physical property measurement data and the cross section
35% PET island ultrafine fiber and 32% the indefinite island of PA6 are arranged in this ferris wheel type island bicomponent filament yarn, and the superfine fibre ratio reaches 67%, tricot or the nonwoven fabric processed with this fabric of island-in-sea type bicomponent filament yarn; Adopt polyurethane impregnated or coating technology to fabric treating; After extracting PE out, because PET fiber good rigidly, extension at break is little; Therefore can make density height, Heat stability is good with this fiber, be difficult for taking place all kinds of artificial leather base cloths of deformation.
Embodiment 3: modified PET is high to shrink the production technology of ferris wheel type island bicomponent filament yarn of section/(PA6+LDPE)
(a) spinning material:
Decide island component: the high contraction of modified PET cut into slices (about dry-hot shrinkage 35%), and viscosity is 0.652dl/g;
The blend of LDPE+PA6: melt index is that LDPE and the viscosity of 60MFI is the blend of the PA6 of 2.8 η, wherein: LDPE, trade mark 1I60A, melt index is 60, Yanshan Petrochemical branch company in Beijing produces.
Slices of caprone, trade mark M32800, relative viscosity is 2.8 η; Guangzhou Xin Huimei synthetic fibre reaches limited company and produces.
(b) proportioning raw materials: weight ratio: high section/(PA6+LDPE)=30/ (35+35) that shrink of modified PET;
(c) spinnerets specification: hole count * ∩ figurate number * aperture is 84 * 8 * 0.30mm;
(d) screw extruder: decide island component φ 65, indefinite island component φ 90;
(e) measuring pump specification: decide island component 0.6cc/rev, indefinite island component 1.2cc/rev;
(f) cooling air temperature: 19 ℃, wind speed: 0.6m/s;
(g) upper oil-pan rotating speed: 30rpm/min, oil concentration is: 6.0%;
(h) spinning (coiling) speed: 600m/min;
(i) spinning technique transitivity:
Island fabric of island-in-sea type bicomponent filament yarn spinning technique table is decided in table 7 652dtex/84F * 8
Island UDY fabric of island-in-sea type bicomponent filament yarn physical property measurement data are decided in table 8 652dtex/84F * 8
| Specification | Fracture strength cn/dtex | Elongation at break % | Oil content % |
| The island is decided in 652dtex/84F * 8 | 1.20 | 341.9 | 1.38 |
(j) drawing process transitivity:
Drawing process is set: effectively draw ratio is 2.9, and temperature of heat plate is 70 ℃, and heater temperature is 80 ℃, draw speed 200m/min.
Table 9: superfine fibre number in stretch back DT silk physical property measurement data and the cross section
Tricot or the nonwoven fabric of using this ferris wheel type island bicomponent filament yarn to process; Adopt polyurethane impregnated or coating technology to fabric treating; After extracting PE out; Process superfine fibre artificial leather base cloth, because the high PET fiber that shrinks in the drying process of base cloth a certain amount of contraction has taken place during high-temperature shaping; Therefore compressed PA6 superfine fibre and PU foaming resin makes base cloth have the elasticity of compression and the feel of enriching preferably, is the excellent material of making high density, feel, the good artificial leather base cloth of sense that hangs down.
Claims (10)
1. manufacturing approach that the cross section is a ferris wheel type island bicomponent filament yarn; Use twin-screw composite spinning equipment, adopt twin-screw composite spinning method, the component that makes two kinds of fusions is through described composite spining module; Merge in the spinneret orifice porch; Together extrude tow, through cool off, oil, reeling makes semi-finished product UDY silk, again drawn process finished product DT or again drawn be out of shape and process the DTY bull wheel type island bicomponent filament yarn that rubs; Wherein one is that mixed proportion is PE and the indefinite island component blend of PA between 50: 50 to 60: 40 mutually, another be mutually a kind of anti-again toluene that carries out melt spinning and DMF solvent decide the island component high polymer; In the made ferris wheel type island composite fibre, a delineation island is arranged in the skin of cross section, all the other are for indefinite island.
2. the manufacturing approach of ferris wheel type as claimed in claim 1 island bicomponent filament yarn; It is characterized in that it is the low density polyethylene of 50～70MFI and the blend of the polyamide fibre PA6 that relative viscosity is 2.6～3.2 η that indefinite island component uses melt index mutually, deciding island component is a kind of anti-again toluene of melt spinning and high polymer of DMF solvent of carrying out mutually; It decides the island number can be 2～32, and the weight ratio of deciding island and indefinite island two-phase component can be 20/80～40/60.
3. the manufacturing approach of ferris wheel type as claimed in claim 2 island bicomponent filament yarn; When it is characterized in that deciding island component employing PA6; The melt temperature of PA6 component can be controlled in 270～280 ℃, and the melt temperature of indefinite island PA6+LDPE blend is controlled at 265 ℃～285 ℃.
4. the manufacturing approach of ferris wheel type as claimed in claim 2 island bicomponent filament yarn; When it is characterized in that deciding island component employing PET; The melt temperature of PET component can be controlled in 280～290 ℃, and the melt temperature of indefinite island PA6+LDPE blend is controlled at 265 ℃～285 ℃.
5. the manufacturing approach of ferris wheel type as claimed in claim 2 island bicomponent filament yarn; When it is characterized in that deciding island component employing PTT; The melt temperature of PTT component can be controlled in 255～265 ℃, and the melt temperature of indefinite island PA6+LDPE blend is controlled at 265 ℃～285 ℃.
6. the manufacturing approach of ferris wheel type as claimed in claim 2 island bicomponent filament yarn; When it is characterized in that deciding island component employing antibacterial deodourizing PET section; The melt temperature of antibacterial deodourizing PET component can be controlled in 270～285 ℃, and the melt temperature of indefinite island PA6+LDPE blend is controlled at 265 ℃～285 ℃.
7. the manufacturing approach of ferris wheel type as claimed in claim 2 island bicomponent filament yarn; It is characterized in that deciding island component adopts high contraction of modified PET to cut into slices; The melt temperature of modified PET can be controlled to be 270～285 ℃, and the melt temperature of indefinite island PA6+LDPE blend is controlled at 265 ℃～285 ℃.
8. the employed composite spining module of the described manufacturing ferris wheel of claim 1 type island bicomponent filament yarn is characterized in that assembly integral body is surrounded by upper and lower casing, and agent structure is followed successively by upper cover plate, distribution plate 1, distribution plate 2, needle tubing plate and spinnerets and constitutes.
9. in the assembly as claimed in claim 8, it is characterized in that each the needle tubing hole on the needle tubing plate is concentric with each spinneret orifice on the spinnerets and corresponding one by one.
10. in the assembly as claimed in claim 8, it is characterized in that outlet one end of needle tubing is processed to 2～32 " ∩ " shape slits, and directly contact that the spinnerets inner face is the plane with spinning plate surface.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011102803788A CN102704020A (en) | 2011-09-20 | 2011-09-20 | Method and composite spinning component for preparing ferris wheel sea island composite filaments |
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| CN2011102803788A CN102704020A (en) | 2011-09-20 | 2011-09-20 | Method and composite spinning component for preparing ferris wheel sea island composite filaments |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103114458A (en) * | 2013-01-24 | 2013-05-22 | 嘉兴学院 | Preparation method of high-density and high-physical-property suede superfine fiber artificial leathers |
| CN103467716A (en) * | 2013-09-09 | 2013-12-25 | 张大省 | Copolyether ester terephthalate capable of being subjected to disperse dye normal-pressure deep dyeing and superfine fiber thereof |
| CN105839209A (en) * | 2016-05-25 | 2016-08-10 | 浙江古纤道股份有限公司 | Process for processing same-spinneret bi-color ultrafine composite polyester fibers |
| CN112575398A (en) * | 2020-12-21 | 2021-03-30 | 江苏华峰超纤材料有限公司 | PP/LDPE sea-island fiber for thermal forming non-woven fabric and preparation method thereof |
| CN116288765A (en) * | 2023-04-13 | 2023-06-23 | 天津市恒宇磁塑制品有限公司 | Preparation process of composite multi-functional fiber |
Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57176210A (en) * | 1981-04-23 | 1982-10-29 | Tanaka Kikinzoku Kogyo Kk | Spinneret for conjugate yarn |
| EP0455927A1 (en) * | 1990-05-11 | 1991-11-13 | Nan Ya Plastics Corporation | Process for preparing partially dissolvable and splittable conjugated microfiber |
| EP0668379A1 (en) * | 1993-09-03 | 1995-08-23 | Polymer Processing Research Institute Limited | Method of manufacturing filament and filament assembly of thermotropic liquid crystal polymer |
| JPH08269811A (en) * | 1995-03-31 | 1996-10-15 | Polymer Processing Res Inst | Production of highly heat-resistant polymer filament |
| JPH10245714A (en) * | 1997-02-27 | 1998-09-14 | Teijin Ltd | Composite spinneret |
| CN1468335A (en) * | 2000-08-03 | 2004-01-14 | BBA�ޱ�֯Ʒ����ɭά����˾ | Process and system for producing multicomponent spunbonded nonwoven fabrics |
| JP2004197284A (en) * | 2002-12-20 | 2004-07-15 | Kasen Nozuru Seisakusho:Kk | Spinneret device for island in sea type conjugate fiber and method for producing island in sea type conjugate fiber by using the same |
| CN1563523A (en) * | 2004-03-23 | 2005-01-12 | 中国石化仪征化纤股份有限公司 | Composite spinning component entities including double constituents |
| CN2823281Y (en) * | 2005-09-15 | 2006-10-04 | 吴江丝绸股份有限公司 | Islands-in-sea type composite ultrathin fiber spinning assembly |
| CN101050554A (en) * | 2007-04-29 | 2007-10-10 | 浙江理工大学 | Imitated natural fabric, fabricating method and equipment |
| CN101333694A (en) * | 2008-08-05 | 2008-12-31 | 无锡双象超纤材料股份有限公司 | Satellite type superfine denier polyamide short fibre and producing method thereof |
| CN101818413A (en) * | 2010-03-18 | 2010-09-01 | 吉安市三江超纤无纺有限公司 | Manufacturing method and device for two-component hollow spun-bonded spunlace non-woven fabrics |
| CN102168321A (en) * | 2011-04-09 | 2011-08-31 | 禾欣可乐丽超纤皮(嘉兴)有限公司 | Sea-island type composite fiber manufacture method |
| CN102168345A (en) * | 2011-04-09 | 2011-08-31 | 浙江禾欣实业集团股份有限公司 | Method for preparing composite superfine fiber artificial leather base fabric |
-
2011
- 2011-09-20 CN CN2011102803788A patent/CN102704020A/en active Pending
Patent Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57176210A (en) * | 1981-04-23 | 1982-10-29 | Tanaka Kikinzoku Kogyo Kk | Spinneret for conjugate yarn |
| EP0455927A1 (en) * | 1990-05-11 | 1991-11-13 | Nan Ya Plastics Corporation | Process for preparing partially dissolvable and splittable conjugated microfiber |
| EP0668379A1 (en) * | 1993-09-03 | 1995-08-23 | Polymer Processing Research Institute Limited | Method of manufacturing filament and filament assembly of thermotropic liquid crystal polymer |
| JPH08269811A (en) * | 1995-03-31 | 1996-10-15 | Polymer Processing Res Inst | Production of highly heat-resistant polymer filament |
| JPH10245714A (en) * | 1997-02-27 | 1998-09-14 | Teijin Ltd | Composite spinneret |
| CN1468335A (en) * | 2000-08-03 | 2004-01-14 | BBA�ޱ�֯Ʒ����ɭά����˾ | Process and system for producing multicomponent spunbonded nonwoven fabrics |
| JP2004197284A (en) * | 2002-12-20 | 2004-07-15 | Kasen Nozuru Seisakusho:Kk | Spinneret device for island in sea type conjugate fiber and method for producing island in sea type conjugate fiber by using the same |
| CN1563523A (en) * | 2004-03-23 | 2005-01-12 | 中国石化仪征化纤股份有限公司 | Composite spinning component entities including double constituents |
| CN2823281Y (en) * | 2005-09-15 | 2006-10-04 | 吴江丝绸股份有限公司 | Islands-in-sea type composite ultrathin fiber spinning assembly |
| CN101050554A (en) * | 2007-04-29 | 2007-10-10 | 浙江理工大学 | Imitated natural fabric, fabricating method and equipment |
| CN101333694A (en) * | 2008-08-05 | 2008-12-31 | 无锡双象超纤材料股份有限公司 | Satellite type superfine denier polyamide short fibre and producing method thereof |
| CN101818413A (en) * | 2010-03-18 | 2010-09-01 | 吉安市三江超纤无纺有限公司 | Manufacturing method and device for two-component hollow spun-bonded spunlace non-woven fabrics |
| CN102168321A (en) * | 2011-04-09 | 2011-08-31 | 禾欣可乐丽超纤皮(嘉兴)有限公司 | Sea-island type composite fiber manufacture method |
| CN102168345A (en) * | 2011-04-09 | 2011-08-31 | 浙江禾欣实业集团股份有限公司 | Method for preparing composite superfine fiber artificial leather base fabric |
Non-Patent Citations (1)
| Title |
|---|
| 宋心远等: "《新型纤维及织物染整》", 31 January 2006, 中国纺织出版社 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103114458A (en) * | 2013-01-24 | 2013-05-22 | 嘉兴学院 | Preparation method of high-density and high-physical-property suede superfine fiber artificial leathers |
| CN103467716A (en) * | 2013-09-09 | 2013-12-25 | 张大省 | Copolyether ester terephthalate capable of being subjected to disperse dye normal-pressure deep dyeing and superfine fiber thereof |
| CN105839209A (en) * | 2016-05-25 | 2016-08-10 | 浙江古纤道股份有限公司 | Process for processing same-spinneret bi-color ultrafine composite polyester fibers |
| CN112575398A (en) * | 2020-12-21 | 2021-03-30 | 江苏华峰超纤材料有限公司 | PP/LDPE sea-island fiber for thermal forming non-woven fabric and preparation method thereof |
| CN116288765A (en) * | 2023-04-13 | 2023-06-23 | 天津市恒宇磁塑制品有限公司 | Preparation process of composite multi-functional fiber |
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