CN109943909A - A kind of PE/PET figured islands-in-sea fiber and preparation method thereof - Google Patents

A kind of PE/PET figured islands-in-sea fiber and preparation method thereof Download PDF

Info

Publication number
CN109943909A
CN109943909A CN201910145654.6A CN201910145654A CN109943909A CN 109943909 A CN109943909 A CN 109943909A CN 201910145654 A CN201910145654 A CN 201910145654A CN 109943909 A CN109943909 A CN 109943909A
Authority
CN
China
Prior art keywords
island
sea
pet
melt
spinning
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.)
Pending
Application number
CN201910145654.6A
Other languages
Chinese (zh)
Inventor
陈亚精
林海
黄洁希
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangdong Chemical Fiber Research Institute
Original Assignee
Guangdong Chemical Fiber Research Institute
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangdong Chemical Fiber Research Institute filed Critical Guangdong Chemical Fiber Research Institute
Priority to CN201910145654.6A priority Critical patent/CN109943909A/en
Publication of CN109943909A publication Critical patent/CN109943909A/en
Pending legal-status Critical Current

Links

Landscapes

  • Multicomponent Fibers (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)

Abstract

The invention discloses a kind of PE/PET figured islands-in-sea fiber, sea-island fibre is formed by the island Hai He, and the ingredient in the sea is PE component, and the ingredient on the island is PET component.The invention also discloses the preparation methods of above-mentioned sea-island fibre.Sea-island fibre of the invention is using PET ingredient as island, due to the resistance to most of organic solvents of PET ingredient, when the sea component of sea-island fibre is extracted by organic solvent, the ingredient on island is unaffected, also, the ingredient in sea is extracted by organic solvent, regeneration PE component can be recycled after extraction, can be recycled.With PE slice and PET slice through imitated POY long filament, POY long filament bobbin boundling contain bucket, after spin and process three-steps process route, the island figured islands-in-sea POY long filament Bu Nian can be produced using the compound spinning production line of POY of excess capacity, through boundling, post-processing at figured type staple fiber.Also, the case where two-step process route in compared with the existing technology, island sticks together, is few.

Description

A kind of PE/PET figured islands-in-sea fiber and preparation method thereof
Technical field
The present invention relates to fibre technology fields more particularly to a kind of PE/PET figured islands-in-sea fiber and preparation method thereof.
Background technique
Under the weight that environmental protection policy is administered in blowdown, environmental protection corium not up to standard, synthetic leather enterprise will gradually be shut down.Woven fabric The all very close corium of its internal structure, appearance tactile impression is removed from office, price only has the 1/4-1/5 of corium, and super fiber leather can solve in corium The problem of common penetrating odor, formaldehyde, heavy metals exceeding standard, thus quickly grow.It is domestic to use import sea-island fibre in recent years Downstream product of exploitation such as imitation buckskin, leather base fabric, cleaning cloth for glasses etc. has developed in advance, therefore sea-island fibre has formed exploitation heat Point.
For determining the relatively indefinite island woven fabric of island woven fabric, more stable performance is had, and color fastness can be many by force.Determine island The synthetic leather product of superfine fibre production has bigger in various aspects such as feel, artificial leather style, mechanical performance and dyeabilities Improvement, there is comparable attraction to high-end synthetic leather product is developed, be particluarly suitable for garment industry and developed.Exploitation PE/PET figured islands-in-sea fiber applications are in the field high to quality requirements
Existing sea-island fibre is usually PE/PA, copet/PA or copet/PET figured sea-island staple fibre, copet It is alkali soluble polyester, the sea as sea-island fibre is more easily separated.But the more difficult recycling of copet after separation.It is existing Sea-island fibre usually dyed in a manner of water dye, coloring spinning sea will affect the color grade on island when separating, product color fastness is poor.
The production technology of existing sea-island fibre is the preceding two-step process road for spinning production fabric of island-in-sea type wound packages silk and rear spinning processing Line, since the spinning hole number of the sea-island fibre is more, there are about the islands of 3-5% to stick together, and influences the quality of product, influences fabric Feel, mechanical performance and artificial leather degree.
Summary of the invention
It is an object of the invention to propose a kind of PE/PET figured islands-in-sea fiber, have the characteristics that color fastness is high;
Another object of the present invention is to propose a kind of preparation method of PE/PET figured islands-in-sea fiber, there is island not glue Even the characteristics of.
To achieve this purpose, the present invention adopts the following technical scheme:
A kind of PE/PET figured islands-in-sea fiber, sea-island fibre are formed by the island Hai He, extra large ingredient be PE component, island at It is divided into PET component.
PET material in wider temperature range have excellent physical mechanical property, creep resistance, fatigue durability, Rub resistance, dimensional stability are all fine.PET has ester bond, resistance to most of organic solvents, good weatherability.PET can be at 55-60 DEG C It is used for a long time in temperature range, short-period used is resistant to 65 DEG C of high temperature, is resistant to -70 DEG C of low temperature, and to its mechanical performance when high and low temperature Influence very little.
Due to the resistance to most of organic solvents of PET ingredient, when the sea component of sea-island fibre is extracted by organic solvent, island at It is point unaffected, also, the ingredient in sea is extracted by organic solvent, be can be recycled after extraction and is regenerated PE component.
It further, include coloring components in PET component.The present invention replaces the prior art in the form of PET original liquid coloring Sea-island fibre water after super fiber leather product be made dye, sea-island fibre of the invention dyes after super fiber leather product is made without water, It is environmentally protective.
Further, the filament number of sea-island fibre is 0.04-0.06detx, belongs to superfine fibre, has excellent properties, Manufactured fabrics feel soft, smooth, drapability is good, plentiful, bulk, good permeability, villus are uniformly and with writing effect.
Further, there is the island 30-40 on the cross section of sea-island fibre.By limiting the quantity on the island of sea-island fibre, so that Sea-island fibre prevents the adhesion on island during the spinning process.
Further, in sea-island fibre, the weight ratio on the island Hai Yu is 3:7-5:5.By limiting the weight ratio on the island Hai Yu, In the case that the dosage in guarantee sea is relatively small and guarantee that there is enough anti-sticking distances between each island, if the distance between each island mistake Greatly, then consumption of organic solvent when extracting sea is excessive, not only causes the waste of organic solvent, also reduces the yield of finished silk;If The distance between each island is too small, then one sticks together during the spinning process, influences the performance of sea-island fibre.
The preparation method of above-mentioned PE/PET figured islands-in-sea fiber, comprising the following steps:
(1), by PET slice melt extruded become can spinning PET melt, which is transported to manifold and uniform Distribution is island phase to island composite component spinneret orifice;
(2), by PE slice melt extruded become can spinning PE melt, which to manifold and is evenly distributed It is marine facies to island composite component spinneret orifice;
(3), PET melt and PE melt are uniformly extruded as spun filament from island composite component spinneret orifice simultaneously;
(4), POY tow is made in spun filament, and POY tow enters fiber barrel by creel and feeding machine, will contain silk later Tow in bucket successively passes through boundling, oils, heats, drawing-off, curling, sizing, obtains PE/PET figured islands-in-sea fibrous finished product.
In preparation method of the invention, contained with PE slice and PET slice through imitated POY long filament, POY long filament bobbin boundling Bucket, rear spin process three-steps process route, can produce figured islands-in-sea POY long using the compound spinning production line of POY of excess capacity The island Si Bunian, through boundling, post-processing at figured type staple fiber.Also, the two-step process route in compared with the existing technology, island The case where sticking together is few.
Further, in step (4), the drawing temperature of drafting step is 60-85 DEG C, drafting multiple 1.3-1.75, Draft speed 150-300m/min;Setting temperature is 85-105 DEG C.
Further, in step (4), the process of POY tow is made in spun filament are as follows: spun filament is successively filled through supercooling It sets, oil, spinning shaft, draw-off godet and up- coiler, rolled machine wind to obtain POY tow, spinning speed 2500-3000m/ min;
Cooling device includes cross air blowing device and changes blowing device, and the wind speed of cross air blasting is 0.5-0.65m/s, side-blown air-cooled But temperature is 25-28 DEG C, and the relative humidity of side-blown air cooling is 85-90%.
Further, in step (1), the PET dry chip of moisture content < 30ppm is made in PET slice, enters the later One screw extruder melt extruded become can spinning PET melt, which is transported to spinning manifold after prefilter In, and it is evenly distributed to by metering pump A the spinneret orifice of island composite component;
The melt extruded process of first screw extruder is equipped with five sections of heating zones, and the heating temperature in each area is 283 DEG C, 285 ℃,287℃,289℃,287℃;Condition of spinning manifold temperature is 285 DEG C;
The range of viscosities of PET slice is 0.5-0.75dl/g, and fusing point is 252-260 DEG C.
Further, in step (2), PE slice by the melt extruded of the second screw extruder become can spinning PE Melt leads to metering pump B by the PE melt conveying into spinning manifold, and is evenly distributed in the composite component spinneret orifice of island;
The melt extruded process of second screw extruder is equipped with five sections of heating zones, and the heating temperature in each area is 200 DEG C, 210 ℃,220℃,225℃,230℃;
The melt index range of PE slice is 48.0-60dl/g, and melting range is 105-125 DEG C.
The invention has the benefit that
Sea-island fibre of the invention, due to the resistance to most of organic solvents of PET ingredient, works as sea-island fibre using PET ingredient as island Sea component when being extracted by organic solvent, the ingredient on island is unaffected, also, the ingredient in sea is extracted by organic solvent, extraction Regeneration PE component can be recycled afterwards, can be recycled.
In preparation method of the invention, contained with PE slice and PET slice through spinning POY long filament, POY long filament bobbin boundling Bucket, rear spin process three-steps process route, can produce figured islands-in-sea POY long using the compound spinning production line of POY of excess capacity The island Si Bunian, through boundling, post-processing at figured type staple fiber.Also, the two-step process route in compared with the existing technology, island The case where sticking together is few.
Specific embodiment
Technical solution of the present invention is further illustrated below with reference to attached specific embodiment.
A kind of PE/PET figured islands-in-sea fiber, sea-island fibre are formed by the island Hai He, extra large ingredient be PE component, island at It is divided into PET component.
PET material in wider temperature range have excellent physical mechanical property, creep resistance, fatigue durability, Rub resistance, dimensional stability are all fine.PET has ester bond, resistance to most of organic solvents, good weatherability.PET can be at 55-60 DEG C It is used for a long time in temperature range, short-period used is resistant to 65 DEG C of high temperature, is resistant to -70 DEG C of low temperature, and to its mechanical performance when high and low temperature Influence very little.
Due to the resistance to most of organic solvents of PET ingredient, when the sea component of sea-island fibre is extracted by organic solvent, island at It is point unaffected, also, the ingredient in sea is extracted by organic solvent, be can be recycled after extraction and is regenerated PE component.
It further, include coloring components in PET component.The present invention replaces the prior art in the form of PET original liquid coloring Sea-island fibre water after super fiber leather product be made dye, sea-island fibre of the invention dyes after super fiber leather product is made without water, It is environmentally protective.
Further, the filament number of sea-island fibre is 0.04-0.06detx, belongs to superfine fibre, has excellent properties, Manufactured fabrics feel soft, smooth, drapability is good, plentiful, bulk, good permeability, villus are uniformly and with writing effect.
Further, there is the island 30-40 on the cross section of sea-island fibre.By limiting the quantity on the island of sea-island fibre, so that Sea-island fibre prevents the adhesion on island during the spinning process.
Further, in sea-island fibre, the weight ratio on the island Hai Yu is 3:7-5:5.By limiting the weight ratio on the island Hai Yu, In the case that the dosage in guarantee sea is relatively small and guarantee that there is enough anti-sticking distances between each island, if the distance between each island mistake Greatly, then consumption of organic solvent when extracting sea is excessive, not only causes the waste of organic solvent, also reduces the yield of finished silk;If The distance between each island is too small, then one sticks together during the spinning process, influences the performance of sea-island fibre.
The preparation method of above-mentioned PE/PET figured islands-in-sea fiber, comprising the following steps:
(1), by PET slice melt extruded become can spinning PET melt, which is transported to manifold and uniform Distribution is island phase to island composite component spinneret orifice;
(2), by PE slice melt extruded become can spinning PE melt, which to manifold and is evenly distributed It is marine facies to island composite component spinneret orifice;
(3), PET melt and PE melt are uniformly extruded as spun filament from island composite component spinneret orifice simultaneously;
(4), POY tow is made in spun filament, and POY tow enters fiber barrel by creel and feeding machine, will contain silk later Bucket in tow successively pass through boundling, oil, heat, drawing-off, curling, sizing, cutting, obtain PE/PET figured islands-in-sea fiber at Product.
In preparation method of the invention, contained with PE slice and PET slice through imitated POY long filament, POY long filament bobbin boundling Bucket, rear spin process three-steps process route, can produce figured islands-in-sea POY long using the compound spinning production line of POY of excess capacity The island Si Bunian, through boundling, post-processing at figured type staple fiber.Also, the two-step process route in compared with the existing technology, island The case where sticking together is few.
The spinning manifold of sea-island fibre has 6 or 8 spinning parts, and each spinning part has 8,10 or 12 spinning groups Part, cabinet can guarantee that each position melt quality is identical.Melt enters cabinet, passes through the pipeline of 6 same diameters and length point Not Tong Guo respective transmission device and metering pump quantitatively input composite spining module.Each composite spining module has one piece of spinneret Plate, there are about 48 holes, every 37 islands Kong You for every block of spinneret.
Further, in step (4), the drawing temperature of drafting step is 60-85 DEG C, drafting multiple 1.3-1.75, Draft speed 150-300m/min;Setting temperature is 85-105 DEG C.By limiting drawing-off parameter and setting temperature, so that fiber is stretched It is straight parallel, guarantee the uniformity of drawing of fiber.
Further, in step (4), the process of POY tow is made in spun filament are as follows: spun filament is successively filled through supercooling It sets, oil, spinning shaft, draw-off godet and up- coiler, rolled machine wind to obtain POY tow, spinning speed 2500-3000m/ min;
Cooling device includes cross air blowing device and changes blowing device, and the wind speed of cross air blasting is 0.5-0.65m/s, and circular blow is air-cooled But temperature is 25-28 DEG C, and the relative humidity of side-blown air cooling is 85-90%.
Further, in step (1), the PET dry chip of moisture content < 30ppm is made in PET slice, enters the later One screw extruder melt extruded become can spinning PET melt, which is transported to spinning manifold after prefilter In, and it is evenly distributed to by metering pump A the spinneret orifice of island composite component;
The melt extruded process of first screw extruder is equipped with five sections of heating zones, and the heating temperature in each area is 283 DEG C, 285 ℃,287℃,289℃,287℃;Condition of spinning manifold temperature is 285 DEG C;
The range of viscosities of PET slice is 0.5-0.75dl/g, and fusing point is 252-260 DEG C.
Further, in step (2), PE slice by the melt extruded of the second screw extruder become can spinning PE Melt leads to metering pump B by the PE melt conveying into spinning manifold, and is evenly distributed in the composite component spinneret orifice of island;
The melt extruded process of second screw extruder is equipped with five sections of heating zones, and the heating temperature in each area is 200 DEG C, 210 ℃,220℃,225℃,230℃;
The melt index range of PE slice is 48.0-60dl/g, and melting range is 105-125 DEG C.
The present invention is further explained by the following examples.
Embodiment 1
The PE/PET figured islands-in-sea fiber of the present embodiment is formed by the island Hai He, extra large ingredient be PE component, state island at It is divided into PET component;It include coloring components in PET component;The filament number of sea-island fibre is 0.04detx;Sea-island fibre it is transversal 37 island face Shang You;In sea-island fibre, the weight ratio on the island Hai Yu is 3:7.
The preparation method of above-mentioned PE/PET figured islands-in-sea fiber, comprising the following steps:
Step (1), the PET dry chip that PET slice is made to moisture content < 30ppm, enter the first screw extruder later Melt extruded become can spinning PET melt, which is transported in spinning manifold after prefilter, and passes through metering Pump A is evenly distributed to the spinneret orifice of island composite component, is island phase;
The melt extruded process of first screw extruder is equipped with five sections of heating zones, and the heating temperature in each area is 283 DEG C, 285 ℃,287℃,289℃,287℃;Condition of spinning manifold temperature is 285 DEG C;
The range of viscosities of PET slice is 0.5-0.75dl/g, and fusing point is 252-260 DEG C.
Step (2), PE slice by the melt extruded of the second screw extruder become can spinning PE melt, lead to metering pump The PE melt conveying into spinning manifold, and is evenly distributed in the composite component spinneret orifice of island by B, is marine facies;
The melt extruded process of second screw extruder is equipped with five sections of heating zones, and the heating temperature in each area is 200 DEG C, 210 ℃,220℃,225℃,230℃;
The melt index range of PE slice is 48.0-60dl/g, and melting range is 105-125 DEG C.
Step (3), PET melt and PE melt are uniformly extruded as spun filament from island composite component spinneret orifice simultaneously;
POY tow is made in step (4), spun filament, and POY tow enters fiber barrel by creel and feeding machine, later will Tow in fiber barrel successively passes through boundling, oils, heats, drawing-off, curling, sizing, obtain PE/PET figured islands-in-sea fiber at Product.
In step (4), the drawing temperature of drafting step is 85 DEG C, drafting multiple 1.5, draft speed 150m/min; Setting temperature is 95 DEG C.The process of POY tow is made in spun filament are as follows: spun filament successively through apparatus for supercooling, oil, spinning river in Zhejiang Province Road, draw-off godet and up- coiler, rolled machine wind to obtain POY tow, spinning speed 2900-3000m/min;Cooling device includes Cross air blowing device and change blowing device, the wind speed of cross air blasting is 0.5-0.65m/s, and the temperature of ring wind quenching is 25-28 DEG C, side The relative humidity of quenching is 85-90%.
Embodiment 2
The PE/PET figured islands-in-sea fiber of the present embodiment and preparation method thereof substantially the same manner as Example 1, difference It is:
The filament number of sea-island fibre is 0.06detx, 37 island cross section Shang You of sea-island fibre, in sea-island fibre, sea with The weight ratio on island is 7:13;
The preparation method the step of in (4), the drawing temperature of drafting step is 60-70 DEG C, drafting multiple 1.75, drawing-off Speed 300m/min;Setting temperature is 105 DEG C.The spinning speed that POY tow is made in spun filament is 2700-2800m/min.
Embodiment 3
The PE/PET figured islands-in-sea fiber of the present embodiment and preparation method thereof substantially the same manner as Example 1, difference It is:
The filament number of sea-island fibre is 0.05detx, 37 island cross section Shang You of sea-island fibre, in sea-island fibre, sea with The weight ratio on island is 4:6;
The preparation method the step of in (4), the drawing temperature of drafting step is 70-75 DEG C, drafting multiple 1.6, drawing-off Speed 200m/min;Setting temperature is 100 DEG C.The spinning speed that POY tow is made in spun filament is 2850-2950m/min.
Embodiment 4
The PE/PET figured islands-in-sea fiber of the present embodiment and preparation method thereof substantially the same manner as Example 1, difference It is:
The filament number of sea-island fibre is 0.05detx, 37 island cross section Shang You of sea-island fibre, in sea-island fibre, sea with The weight ratio on island is 9:11;
The preparation method the step of in (4), the drawing temperature of drafting step is 75 DEG C, drafting multiple 1.7, draft speed 250m/min;Setting temperature is 90 DEG C.The spinning speed that POY tow is made in spun filament is 3000m/min.
Embodiment 5
The PE/PET figured islands-in-sea fiber of the present embodiment and preparation method thereof substantially the same manner as Example 1, difference It is:
The filament number of sea-island fibre is 0.05detx, 37 island cross section Shang You of sea-island fibre, in sea-island fibre, sea with The weight ratio on island is 5:5;
The preparation method the step of in (4), the drawing temperature of drafting step is 65 DEG C, drafting multiple 1.3, draft speed 300m/min;Setting temperature is 85 DEG C.The spinning speed that POY tow is made in spun filament is 2500m/min.
The PE/PET figured islands-in-sea fiber of embodiment 1-5 is tested for the property, test result is as follows shown in table.
Example Breaking strength Elongation at break Yarn unevenness CV value The fibre density of single fiber
Embodiment 1 ≥3.5CN/dtex 45-55% < 0.8% 1.00g/cm3
Embodiment 2 ≥3.5CN/dtex 45-55% < 0.8% 0.96g/cm3
Embodiment 3 ≥3.5CN/dtex 45-55% < 0.8% 0.92g/cm3
Embodiment 4 ≥3.5CN/dtex 45-55% < 0.8% 0.85g/cm3
Embodiment 5 ≥3.5CN/dtex 45-55% < 0.8% 1.02g/cm3
As seen from the above table, the better performances of the sea-island fibre of embodiment 1-5.
The technical principle of the invention is described above in combination with a specific embodiment.These descriptions are intended merely to explain of the invention Principle, and shall not be construed in any way as a limitation of the scope of protection of the invention.Based on the explanation herein, the technology of this field Personnel can associate with other specific embodiments of the invention without creative labor, these modes are fallen within Within protection scope of the present invention.

Claims (10)

1. a kind of PE/PET figured islands-in-sea fiber, which is characterized in that the sea-island fibre is formed by the island Hai He, it is described sea at It is divided into PE component, the ingredient on the island is PET component.
2. PE/PET figured islands-in-sea fiber according to claim 1, which is characterized in that include in the PET component Color ingredient.
3. PE/PET figured islands-in-sea fiber according to claim 1, which is characterized in that the monofilament of the sea-island fibre is fine Degree is 0.04-0.06detx.
4. PE/PET figured islands-in-sea fiber according to claim 1, which is characterized in that the cross section of the sea-island fibre On have the island 30-40.
5. PE/PET figured islands-in-sea fiber according to claim 1, which is characterized in that in the sea-island fibre, sea with The weight ratio on island is 3:7-5:5.
6. the preparation method of any one of the claim 1-5 PE/PET figured islands-in-sea fiber, which is characterized in that including following Step:
(1), by PET slice melt extruded become can spinning PET melt, which is transported to manifold and is evenly distributed It is island phase to island composite component spinneret orifice;
(2), by PE slice melt extruded become can spinning PE melt, by the PE melt conveying to manifold and evenly distribute to institute Island composite component spinneret orifice is stated, is marine facies;
(3), PET melt and PE melt are uniformly extruded as spun filament from the island composite component spinneret orifice simultaneously;
(4), POY tow is made in the spun filament, and the POY tow enters fiber barrel by creel and feeding machine, later will Tow in the fiber barrel successively passes through boundling, oils, heats, drawing-off, curling, sizing, cutting, obtains PE/PET figured type sea Island fibrous finished product.
7. preparation method according to claim 6, which is characterized in that in the step (4), the drafting step is led Stretching temperature is 60-85 DEG C, drafting multiple 1.3-1.75, draft speed 150-300m/min;Setting temperature is 85-105 DEG C.
8. preparation method according to claim 6, which is characterized in that in the step (4), the spun filament is made The process of POY tow are as follows: the spun filament successively through apparatus for supercooling, oil, spinning shaft, draw-off godet and up- coiler, through rolling up POY tow, spinning speed 2500-3000m/min are wound to obtain around machine;
The cooling device includes cross air blowing device, and the wind speed of cross air blasting is 0.5-0.65m/s, and the temperature of side-blown air cooling is 25-28 DEG C, the relative humidity of side-blown air cooling is 85-90%.
9. preparation method according to claim 6, which is characterized in that in the step (1), the PET is sliced and is made At the PET dry chip of moisture content < 30ppm, later enter the first screw extruder melt extruded become can spinning PET melt, should PET melt is transported in spinning manifold after prefilter, and is evenly distributed to the island composite component by metering pump A Spinneret orifice;
The melt extruded process of first screw extruder is equipped with five sections of heating zones, and the heating temperature in each area is 283 DEG C, 285 ℃,287℃,289℃,287℃;Condition of spinning manifold temperature is 285 DEG C;
The range of viscosities of the PET slice is 0.5-0.75dl/g, and fusing point is 252-260 DEG C.
10. preparation method according to claim 6, which is characterized in that in the step (2), the PE slice passes through The melt extruded of second screw extruder become can spinning PE melt, lead to metering pump B for the PE melt conveying to spinning manifold In, and be evenly distributed in the island composite component spinneret orifice;
The melt extruded process of second screw extruder is equipped with five sections of heating zones, and the heating temperature in each area is 200 DEG C, 210 ℃,220℃,225℃,230℃;
The melt index range of the PE slice is 48.0-60dl/g, and melting range is 105-125 DEG C.
CN201910145654.6A 2019-02-27 2019-02-27 A kind of PE/PET figured islands-in-sea fiber and preparation method thereof Pending CN109943909A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910145654.6A CN109943909A (en) 2019-02-27 2019-02-27 A kind of PE/PET figured islands-in-sea fiber and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910145654.6A CN109943909A (en) 2019-02-27 2019-02-27 A kind of PE/PET figured islands-in-sea fiber and preparation method thereof

Publications (1)

Publication Number Publication Date
CN109943909A true CN109943909A (en) 2019-06-28

Family

ID=67008074

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910145654.6A Pending CN109943909A (en) 2019-02-27 2019-02-27 A kind of PE/PET figured islands-in-sea fiber and preparation method thereof

Country Status (1)

Country Link
CN (1) CN109943909A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111074376A (en) * 2019-12-23 2020-04-28 江苏华峰超纤材料有限公司 High-crimp sea-island synthetic fiber and preparation method thereof

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54151618A (en) * 1978-05-18 1979-11-29 Kuraray Co Ltd Fibrous material and fabric comprising it
CN1505702A (en) * 2001-04-26 2004-06-16 ��ʽ�����¡ A sea-island typed conjugate multi filament comprising dope dyeing component, and a process of preparing for the same
JP3970440B2 (en) * 1998-10-02 2007-09-05 株式会社クラレ Sea-island structure fiber and manufacturing method thereof
CN101333690A (en) * 2008-06-30 2008-12-31 何国仙 Superfine multicolor terylene for lining of automobile internal decoration
CN101665994A (en) * 2009-09-30 2010-03-10 山东同大海岛新材料股份有限公司 Figured islands-in-sea composite fiber and production method thereof
CN102071495A (en) * 2010-07-28 2011-05-25 烟台万华超纤股份有限公司 Figured sea-island super-fine fiber, and preparation method thereof and synthetic leather preparing process method using same
CN102776602A (en) * 2012-07-27 2012-11-14 烟台万华超纤股份有限公司 Figured island superfine fiber, figured island superfine fiber synthetic leather base cloth, suede leather for clothes, smooth synthetic leather for clothes and production method of fiber, base cloth, suede leather and smooth synthetic leather
CN103820872A (en) * 2014-03-03 2014-05-28 晋江市闽高纺织科技有限公司 Figured sea-island ultrafine fiber, preparing method and process method of synthetic leather of figured sea-island ultrafine fiber
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
US20180223454A1 (en) * 2017-02-07 2018-08-09 Earth Renewable Technologies Bicomponent fiber additive delivery composition

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54151618A (en) * 1978-05-18 1979-11-29 Kuraray Co Ltd Fibrous material and fabric comprising it
JP3970440B2 (en) * 1998-10-02 2007-09-05 株式会社クラレ Sea-island structure fiber and manufacturing method thereof
CN1505702A (en) * 2001-04-26 2004-06-16 ��ʽ�����¡ A sea-island typed conjugate multi filament comprising dope dyeing component, and a process of preparing for the same
CN101333690A (en) * 2008-06-30 2008-12-31 何国仙 Superfine multicolor terylene for lining of automobile internal decoration
CN101665994A (en) * 2009-09-30 2010-03-10 山东同大海岛新材料股份有限公司 Figured islands-in-sea composite fiber and production method thereof
CN102071495A (en) * 2010-07-28 2011-05-25 烟台万华超纤股份有限公司 Figured sea-island super-fine fiber, and preparation method thereof and synthetic leather preparing process method using same
CN102776602A (en) * 2012-07-27 2012-11-14 烟台万华超纤股份有限公司 Figured island superfine fiber, figured island superfine fiber synthetic leather base cloth, suede leather for clothes, smooth synthetic leather for clothes and production method of fiber, base cloth, suede leather and smooth synthetic leather
CN103820872A (en) * 2014-03-03 2014-05-28 晋江市闽高纺织科技有限公司 Figured sea-island ultrafine fiber, preparing method and process method of synthetic leather of figured sea-island ultrafine fiber
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
US20180223454A1 (en) * 2017-02-07 2018-08-09 Earth Renewable Technologies Bicomponent fiber additive delivery composition
WO2018148165A1 (en) * 2017-02-07 2018-08-16 Earth Renewable Technologies Bicomponent fiber additive delivery composition

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111074376A (en) * 2019-12-23 2020-04-28 江苏华峰超纤材料有限公司 High-crimp sea-island synthetic fiber and preparation method thereof

Similar Documents

Publication Publication Date Title
CN101126180A (en) Elastic polyester fibre and preparation method thereof
CN102650081B (en) Color fixed island composite short fiber and preparation method thereof
CN106757504B (en) A kind of composite elastic fiber and preparation method thereof
CN103436972A (en) Method for preparing multi-component composite fibers
CN102168320A (en) Production technology for producing porous fine denier colored terylene pre-oriented filament by utilizing recycled polyester bottle flakes
CN107723838B (en) Hot-melt adhesive composite fiber and preparation method thereof
CN101962819A (en) Ultrawhite ultrahigh-molecular weight ultrahigh-modulus polyethylene fibers and preparation process thereof
CN102828266A (en) Terylene superfine flat yarn production method and product
CN103088500A (en) One-step preparation method and device of fully drawn yarn (FDY) or FDY differential shrinkage combined filament yarn
CN105839248A (en) Differential-shrinkage superfine composite draw textured yarn and processing technology thereof
CN106591978A (en) Curly two-color nylon fiber processing technology
CN104060343A (en) Fine-denier and super-fine-denier chinlon 6 fibers and manufacturing method thereof
CN102995147B (en) Manufacture method of ultrathin single-fiber polyamide drawn textured yarn (6DTY)
JP2022552567A (en) Polyamide sea-island fibers, methods of making the same, and uses thereof
CN104963009A (en) Production method for colored PET industrial filaments
CN105908273B (en) A kind of bi-component composite fiber of high anti-fluffing and anti-pilling and high abrasion and preparation method thereof
CN105862149B (en) A kind of superfine composite adds elater and its processing technology
CN104480556A (en) Production process of high-speed spinning type potential crinkled polyester filament yarns
CN105155008A (en) Preparation method and special spinneret plate of stereo color elastic fiber
CN101205632A (en) Technique for producing medium strong polyester filament yarn by melt direct spinning
CN109023564A (en) A kind of preparation method of polylactic acid coloured cut staple
CN104988588B (en) A kind of production method of modified high-strength polyester industrial yarn
CN103225117A (en) Spinning method for polyester cationic composite yarns
CN109234820A (en) A kind of preparation method of polylactic acid short-fiber
CN102071480A (en) Method for producing POY of tight heavy fleece

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20190628