CN111411404B - Preparation process of regenerated semi-dull cationic fiber - Google Patents
Preparation process of regenerated semi-dull cationic fiber Download PDFInfo
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- CN111411404B CN111411404B CN202010362531.0A CN202010362531A CN111411404B CN 111411404 B CN111411404 B CN 111411404B CN 202010362531 A CN202010362531 A CN 202010362531A CN 111411404 B CN111411404 B CN 111411404B
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- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/06—Conditioning or physical treatment of the material to be shaped by drying
- B29B13/065—Conditioning or physical treatment of the material to be shaped by drying of powder or pellets
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- 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
- D01D1/00—Treatment of filament-forming or like material
- D01D1/10—Filtering or de-aerating the spinning solution or melt
- D01D1/106—Filtering
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- 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
- D01D5/088—Cooling filaments, threads or the like, leaving the spinnerettes
- D01D5/092—Cooling filaments, threads or the like, leaving the spinnerettes in shafts or chimneys
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- 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
- D01D5/12—Stretch-spinning methods
- D01D5/16—Stretch-spinning methods using rollers, or like mechanical devices, e.g. snubbing pins
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- 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
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
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- 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
- D01F6/88—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
- D01F6/92—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of polyesters
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Abstract
The invention discloses a preparation process of a regenerated semi-dull cationic fiber, which comprises the following steps: (a) drying the PET master batch containing titanium dioxide; carrying out pre-crystallization drying on the regenerated PET cation slice; (b) blending the dried PET master batch and the pre-crystallized and dried regenerated PET cation slice; (c) conveying the premix to a screw extruder for heating and melting, then conveying a spinning melt into a spinning box, metering by a metering pump, and pressing into a spinning assembly for spinning to obtain nascent tows; (d) and (3) post-heating the primary tows, cooling by circular blowing, bundling and oiling, pre-networking, drafting and shaping, and winding by a drafting and winding device to obtain the regenerated semi-dull cationic fiber. The process is simple and easy to implement, and the prepared regenerated semi-dull cationic fiber has excellent physical properties and can meet the requirements of people on the regenerated semi-dull cationic fiber fabric.
Description
Technical Field
The invention relates to the technical field of polyester fiber production, in particular to a preparation process of a regenerated semi-dull cationic fiber.
Background
Compared with the common polyester fiber, the fabric woven by the cationic polyester fiber has the characteristics of bright color, good deep dyeing property, high color absorption rate, good sunlight fastness and washing color fastness when dyed by the cationic dye, good dye compatibility during color matching dyeing, good stability in a high-temperature dye bath, small contamination on other fibers including the common polyester fiber, no ring dyeing phenomenon and the like, and is more and more popular with consumers. However, since the cationic polyester fiber has excellent chemical inertness and is difficult to be degraded by microorganisms or air under natural conditions, a large amount of waste cationic polyester fiber products become a huge burden on the environment, and the demand for environment-friendly products is increasing along with the deep understanding of people on environment protection, so that the development and research of the regenerated cationic fiber are irrevocable responsibility of enterprises in the field and are important opportunities for enterprise development. In addition, because the water-containing slices can be hydrolyzed when being melted, the molecular weight of the polymer is reduced, the quality of the finished filaments is influenced, water is vaporized at high temperature to form bubbles, and spinning broken ends or broken filaments are easy to cause, the water-containing slices are in an amorphous structure, the softening point is low, and the phenomenon of ring-bonding and material resistance is easy to cause in the feeding section of the screw, so that the normal production is influenced.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provide a preparation process of the regenerated semi-dull cationic fiber, the process is simple and easy to implement, and the prepared regenerated semi-dull cationic fiber has excellent physical properties and can meet the requirements of people on the regenerated semi-dull cationic fiber fabric.
In order to achieve the purpose, the invention adopts the following technical scheme:
a preparation process of regenerated semi-dull cationic fibers comprises the following steps:
(a) adding PET master batch with the titanium dioxide content of 2.65% into a dryer for drying; adding the regenerated PET cation slices into a crystallization drying system for pre-crystallization drying; the drying temperature of the PET master batch is 80 ℃, and the drying air pressure is 0.1 MPa; the crystallization temperature of the regenerated PET cation slice is 152 ℃, the drying temperature is 155 ℃, and the drying wind pressure is 0.08 MPa;
(b) conveying the dried PET master batch and the pre-crystallized and dried regenerated PET cation slices to a master batch machine according to a required ratio for blending to obtain a premix, wherein the content of the PET master batch in the premix is 0.5%;
(c) conveying the premix to a screw extruder for heating and melting to obtain a spinning melt, then conveying the spinning melt into a spinning box, metering by a metering pump, pressing into a spinning assembly for spinning to obtain nascent tows;
(d) and (3) post-heating the primary tows, cooling by circular blowing, bundling and oiling, pre-networking, drafting and shaping, and winding by a drafting and winding device to obtain the regenerated semi-dull cationic fiber.
The intrinsic viscosity of the PET master batch is 0.632 dl/g; the intrinsic viscosity of the regenerated PET cationic chip was 0.58 dl/g.
In the step (c), the screw extruder is provided with five heating zones, and the heating temperature of each zone is respectively as follows: 278 ℃ in the first zone, 284 ℃ in the second zone, 286 ℃ in the third zone, 288 ℃ in the fourth zone and 288 ℃ in the fifth zone; the extrusion pressure of the screw extruder is 12MPa, and the pressure after filtration is 9.5 MPa.
In the step (c), the temperature of the spinning box body is 286.5 ℃, and the pump supply amount of the metering pump is 35.4 g/min.
In the step (c), the heating temperature of the spinning assembly is 300 ℃, the pressure of the assembly is 10.8MPa, the spinning assembly comprises a filtering sand layer and an 800-mesh filtering net arranged below the filtering sand layer, and the filtering sand layer is steel sand of 40-60 meshes.
In the step (d), the temperature of post-heating treatment is 310 ℃, the wind speed of circular blowing cooling treatment is 50m/s, the oiling height of cluster oiling treatment is 1000mm, and the concentration ratio of the oiling agent is 11%.
In the step (d), the pre-network pressure is 0.08 mpa; when in drafting and setting, the speed of the first drafting roller is 2690m/min, and the speed of the second drafting roller is 2700 m/min; in the winding process, the winding speed was 2679m/min and the winding tension was 12 cN.
In the step (a), the crystallization drying system comprises a fluidized bed for slicing and pre-crystallizing and a drying device for slicing and drying, the drying device comprises a tank body, a flow guide mechanism and a stirring mechanism which are respectively arranged in the tank body, and a driving mechanism which is arranged on one side outside the tank body and is used for driving the stirring mechanism to move up and down, the flow guide mechanism comprises a stand column fixed in the upper part of the tank body through a connecting rod, and a plurality of flow guide conical discs connected to the annular outer wall of the stand column at intervals from top to bottom, the outer diameter of the plurality of flow guide conical discs is sequentially increased from top to bottom, the stirring mechanism comprises a cross-shaped support, a main rotating shaft, a last rotating shaft, a next rotating shaft, a first paddle and a second paddle, wherein the cross-shaped support is slidably connected between the inner walls on the two sides of the tank body, the last rotating shaft is arranged in the upper part of the support and is vertically connected with the, Third paddle and fourth paddle that is connected with the perpendicular transmission in pivot middle part next time respectively, the main pivot is through locating the first motor drive rotation in support middle part one side, the direction of rotation of last pivot and pivot next time is opposite, first paddle, second paddle, third paddle and fourth paddle are the crisscross setting of circumference, the direction of rotation of first paddle and fourth paddle is the same, the direction of rotation of second paddle and third paddle is the same, the direction of rotation of first paddle and third paddle is opposite.
Actuating mechanism includes mounting bracket, push rod, installs cylinder cam, the drive cylinder cam pivoted second motor in the mounting bracket, push rod one end stretches into the jar internally and links firmly with the support, the push rod other end stretches into in the mounting bracket and this push rod tip through the connecting rod and the cylinder cam sliding connection that have the roller, cylinder cam circumferential direction drives the push rod up-and-down motion.
The invention has the beneficial effects that: the regenerated semi-dull cationic fiber is prepared by taking the regenerated PET cationic slices as raw materials and adjusting process parameters, the process is simple and easy to implement, and the prepared regenerated semi-dull cationic fiber has excellent physical properties and can meet the requirements of people on the regenerated semi-dull cationic fiber fabric; through the setting of the different external diameter size water conservancy diversion conical disks of multilayer, make the section progressively diffuse the whereabouts along every water conservancy diversion conical disk, make the section can fully contact with high temperature drying gas in the in-process that gets into the jar body, and then realize sliced primary drying, turn over through the mechanism of stirring that can reciprocate the limit stirring and turn over the section that gets into the jar body, and first paddle, the second paddle, third paddle and fourth paddle stir the direction with different turns over, can make the section incessantly overturn and fully contact with high temperature gas, realize sliced further drying, drying effect and drying efficiency are high, be favorable to improving production efficiency.
Drawings
FIG. 1 is a schematic view of a first angle of the drying apparatus of the present invention;
FIG. 2 is an enlarged view taken at A in FIG. 1;
FIG. 3 is a schematic view of a second angle of the drying apparatus of the present invention;
FIG. 4 is an enlarged view at B in FIG. 3;
fig. 5 is a schematic top view of the bracket of the present invention.
Detailed Description
The invention is further described with reference to the accompanying drawings and the detailed description below:
a preparation process of regenerated semi-dull cationic fibers comprises the following steps:
(a) adding PET master batch with the titanium dioxide content of 2.65% into a dryer for drying; adding the regenerated PET cation slices into a crystallization drying system for pre-crystallization drying; the drying temperature of the PET master batch is 80 ℃, and the drying air pressure is 0.1 MPa; the crystallization temperature of the regenerated PET cation slice is 152 ℃, the drying temperature is 155 ℃, and the drying wind pressure is 0.08 MPa; the drying speed can be accelerated and the drying time can be shortened due to the high drying temperature of the slices, but the slices are easy to bond due to too high temperature, so that macromolecules are degraded, and the uniformity of a spinning melt is influenced, so that the drying temperature is controlled to be the above temperature;
(b) conveying the dried PET master batch and the pre-crystallized and dried regenerated PET cation slices to a master batch machine according to a required ratio for blending to obtain a premix, wherein the content of the PET master batch in the premix is 0.5%; because the PET master batch contains higher content of titanium dioxide, the content of the titanium dioxide in the product is adjusted by controlling the proportion of the PET master batch and the regenerated PET cation slice, so that the product meets the requirement of semi-dull product gloss;
(c) conveying the premix to a screw extruder for heating and melting to obtain a spinning melt, then conveying the spinning melt into a spinning box, metering by a metering pump, pressing into a spinning assembly for spinning to obtain nascent tows;
(d) and (3) post-heating the primary tows, cooling by circular blowing, bundling and oiling, pre-networking, drafting and shaping, and winding by a drafting and winding device to obtain the regenerated semi-dull cationic fiber.
The intrinsic viscosity of the PET master batch is 0.632 dl/g; the intrinsic viscosity of the regenerated PET cationic chip was 0.58 dl/g. The regenerated PET cationic slice used in the invention is a regenerated PET cationic slice produced by Zhejiang good people new material Limited company, the terminal carboxyl content in the regenerated PET cationic slice is less than or equal to 25mol/t, and the diethylene glycol content is less than or equal to 1.2%.
In the step (c), the screw extruder is provided with five heating zones, and the heating temperature of each zone is respectively as follows: 278 ℃ in the first zone, 284 ℃ in the second zone, 286 ℃ in the third zone, 288 ℃ in the fourth zone and 288 ℃ in the fifth zone; the extrusion pressure of the screw extruder is 12MPa, and the pressure after filtration is 9.5 MPa.
In the step (c), the temperature of the spinning box body is 286.5 ℃, and the pump supply amount of the metering pump is 35.4 g/min.
In the step (c), the heating temperature of the spinning assembly is 300 ℃, the pressure of the assembly is 10.8MPa, the spinning assembly comprises a filtering sand layer and an 800-mesh filtering net arranged below the filtering sand layer, and the filtering sand layer is steel sand of 40-60 meshes. If the heating temperature of the spinning assembly is too high, the thermal degradation of polymer molecules is large, the polymer molecules are easy to inject during spinning, and the elongation of finished fibers is large; if the heating temperature of the spinning assembly is too low, the shearing stress is large, hard yarns are easily formed, and broken yarns and broken ends are easily generated during stretching.
In the step (d), the temperature of post-heating treatment is 310 ℃, the wind speed of circular blowing cooling treatment is 50m/s, the oiling height of cluster oiling treatment is 1000mm, and the concentration ratio of the oiling agent is 11%.
In the step (d), the pre-network pressure is 0.08 mpa; when in drafting and setting, the speed of the first drafting roller is 2690m/min, and the speed of the second drafting roller is 2700 m/min; in the winding process, the winding speed was 2679m/min and the winding tension was 12 cN. If the winding speed is too high, the speed gradient on the spinning line is increased, the friction resistance between the filament bundle and cold air is increased, the pre-orientation degree of the winding filament is larger, the internal stress of the fiber is increased, the boiling water shrinkage rate of the fiber is too high, if the winding speed is too low, the tension of the filament bundle is reduced, the filament bundle is easy to jump during winding, and the spinning stability is poor.
As shown in fig. 1 to 5, in the step (a), the crystallization drying system includes a fluidized bed for slicing pre-crystallization and a drying device for slicing drying, the drying device includes a tank body 1, a diversion mechanism 2 and a stirring mechanism 3 respectively disposed in the tank body 1, and a driving mechanism 4 disposed at one side outside the tank body 1 and used for driving the stirring mechanism 3 to move up and down, a feed inlet 12 and an air inlet 14 are disposed at the upper end of the tank body 1, a discharge outlet 13 and an air outlet 15 are disposed at the lower end of the tank body 1, high-temperature drying gas enters the tank body 1 from the air inlet 14 and is discharged out of the tank body 1 through the air outlet 15 to form a hot air circulation drying system, and an end cover of the tank body 1 is detachably connected, thereby facilitating the.
The stirring mechanism 3 comprises a cross-shaped bracket 31 connected between the inner walls of the two sides of the tank body 1 in a sliding manner, a main rotating shaft 32 arranged in the middle of the bracket 31, a last rotating shaft 33 arranged in the upper part of the bracket 31 and connected with the main rotating shaft 32 in a vertical transmission manner, a next rotating shaft 34 arranged in the lower part of the bracket 31 and connected with the main rotating shaft 32 in a vertical transmission manner, a first paddle 36 and a second paddle 37 respectively connected with the middle of the last rotating shaft 33 in a vertical transmission manner, and a third paddle 38 and a fourth paddle 39 respectively connected with the middle of the next rotating shaft 34 in a vertical transmission manner. The specific connection mode of the bracket 31 and the tank body 1 is as follows: guide rails 11 are symmetrically arranged on two sides of the inner wall of the tank body 1, and two end faces of the middle part of the bracket 31 are both sunken to form a groove 311 for embedding the guide rails 11; support 31's middle part, with support 31's upper portion and lower part be can dismantle the connection, and support 31's middle part both ends also are for dismantling the connection, remain on support 31 in addition for preventing when the section ejection of compact, support 31 middle part sets to hollow cylinder structure, and support 31 upper portion also sets to hollow cylinder structure and support 31 upper portion terminal surface sets to arc.
The main shaft 32 is rotated through the drive of the first motor 35 arranged in one side of the middle of the bracket 31, the rotation directions of the last rotating shaft 33 and the next rotating shaft 34 are opposite, the first paddle 36, the second paddle 37, the third paddle 38 and the fourth paddle 39 are circumferentially staggered, the rotation directions of the first paddle 36 and the fourth paddle 39 are the same, the rotation directions of the second paddle 37 and the third paddle 38 are the same, and the rotation directions of the first paddle 36 and the third paddle 38 are opposite.
A first bevel gear 321 is arranged in the middle of the main rotating shaft 32, the last rotating shaft 33 is rotatably connected between the upper end of the upper part of the bracket 31 and the middle of the bracket 31 through a bearing, a second bevel gear 331 and a third bevel gear 332 are correspondingly arranged at the lower part and the upper part of the last rotating shaft 33, the lower part of the last rotating shaft 33 is in meshing transmission connection with the main rotating shaft 32 through the second bevel gear 331 and the first bevel gear 321, the end part of the first blade 36 extends into one side of the upper part of the bracket 31 and is rotatably connected with the bracket 31 through a bearing, a sixth bevel gear 361 is arranged at the end part of the first blade 36, the first blade 36 is in meshing transmission connection with the last rotating shaft 33 through the sixth bevel gear 361 and the third bevel gear 332, the end part of the second blade 37 extends into the other side of the upper part of the bracket 31 and is rotatably connected with the bracket 31 through a bearing, a seventh bevel gear 371 is arranged at the end, the upper secondary rotating shaft 33 is rotatably connected between the upper end of the upper part of the bracket 31 and the middle part of the bracket 31 through a bearing, a fourth bevel gear 341 and a fifth bevel gear 342 are correspondingly installed at the upper part and the lower part of the lower secondary rotating shaft 34, the upper part of the lower secondary rotating shaft 34 is in meshing transmission connection with the main rotating shaft 32 through the fourth bevel gear 341 and the first bevel gear 321, the end part of the third blade 38 extends into one side of the lower part of the bracket 31 and is rotatably connected with the bracket 31 through the bearing, the end part of the third blade 38 is provided with an eighth bevel gear 381, the third blade 38 is in meshing transmission connection with the lower secondary rotating shaft 34 through the eighth bevel gear 381 and the fifth bevel gear 342, the end part of the fourth blade 39 extends into the other side of the lower part of the bracket 31 and is rotatably connected with the bracket 31 through the bearing, the end part of the fourth blade 39 is provided with a ninth bevel gear. When the first motor 35 drives the main rotating shaft 32 to rotate, the main rotating shaft 32 simultaneously drives the previous rotating shaft 33 and the next rotating shaft 34 to rotate, and the rotating directions of the previous rotating shaft 33 and the next rotating shaft 34 are opposite, at the same time, the previous rotating shaft 33 drives the first paddle 36 and the second paddle 37 to rotate, and the next rotating shaft 34 drives the third paddle 38 and the fourth paddle 39 to rotate.
The driving mechanism 4 comprises a mounting frame 41, a push rod 44, a cylindrical cam 42 installed in the mounting frame 41, and a second motor 43 for driving the cylindrical cam 42 to rotate, wherein one end of the push rod 44 extends into the tank body 1 and is fixedly connected with the support 31, the other end of the push rod 44 extends into the mounting frame 41, the end part of the push rod 44 is slidably connected with the cylindrical cam 42 through a connecting rod 45 with a roller 46, and the cylindrical cam 42 rotates in the circumferential direction to drive the push rod 44 to move up and down. The push rod 44 is sealed with the tank body 1 by the sealing ring 16, so that the leakage of high-temperature drying gas can be prevented, and the drying effect can be ensured. The outer wall of the cylindrical cam 42 is provided with a closed curve-shaped cam chute 421, the shape of the cam chute 421 is a sine curve or a cosine curve, and the roller 46 is embedded in the cam chute 421, so that the rotary motion of the cylindrical cam 42 is converted into the linear motion of the push rod 44, and the stirring mechanism 3 can move up and down.
The specific process of drying the slices by the drying device is as follows: the section gets into jar body 1 after the fluidized bed pre-crystallization to scatter the whereabouts all around along the upper surface of a plurality of water conservancy diversion conical disks 22, progressively store in jar body 1, when the section of jar in 1 reaches the material level of storing 80%, start first motor 35 and second motor 43 simultaneously, first motor 35 is through main pivot 32, last pivot 33, each paddle of pivot 34 drive rotates next time, meanwhile second motor 43 passes through cylindrical cam 42, connecting rod 45 drive push rod 44 reciprocates and then drives and stir mechanism 3 and reciprocate, stirring mechanism 3 can stir the section simultaneously at the in-process that reciprocates, the section can be more fully contacted with high temperature drying gas, drying efficiency has been improved greatly.
Table 1 shows statistics of physical property data of the regenerated semi-dull cationic fiber produced by the method of the present invention, and it can be known from table 1 that the regenerated semi-dull cationic fiber meets the performance index requirements of the cationic fiber.
TABLE 1
| Item | Index (I) | Test value of sample |
| Evenness of yarn evenness CV% | ≦1.1 | 0.62 |
| Fineness dtex | 132±1.5％ | 132.05 |
| Breaking strength cn/dtex | ≧1.74 | 1.83 |
| Coefficient of variation in breaking strength% | ≦5.0％ | 1.76 |
| Elongation at break% | 152±6.0 | 150.6 |
| Oil content% | 0.4％≥ | 0.47 |
| Thermal stress CN | 60±10 | 66.20 |
| Thermal stress CV | ≦5.0 | 1.72 |
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.
Claims (8)
1. A preparation process of regenerated semi-dull cationic fibers is characterized by comprising the following steps: the method comprises the following steps:
(a) adding PET master batch with the titanium dioxide content of 2.65% into a dryer for drying; adding the regenerated PET cation slices into a crystallization drying system for pre-crystallization drying; the drying temperature of the PET master batch is 80 ℃, and the drying air pressure is 0.1 MPa; the crystallization temperature of the regenerated PET cation slice is 152 ℃, the drying temperature is 155 ℃, and the drying wind pressure is 0.08 MPa;
(b) conveying the dried PET master batch and the pre-crystallized and dried regenerated PET cation slices to a master batch machine according to a required ratio for blending to obtain a premix, wherein the content of the PET master batch in the premix is 0.5%;
(c) conveying the premix to a screw extruder for heating and melting to obtain a spinning melt, then conveying the spinning melt into a spinning box, metering by a metering pump, pressing into a spinning assembly for spinning to obtain nascent tows;
(d) post-heating, circularly blowing, cooling, bundling and oiling the primary tows, and then pre-networking, drafting and shaping, winding and forming the primary tows by a drafting and winding device to obtain regenerated semi-dull cationic fibers;
in step (a), the crystallization drying system includes the fluidized bed that is used for the section precrystallization and the drying device that is used for the section drying, drying device includes jar body (1), sets up water conservancy diversion mechanism (2) and stirring mechanism (3) in jar body (1) respectively, sets up being used for of jar body (1) outside one side drive mechanism (4) that the mechanism (3) reciprocated that stir, water conservancy diversion mechanism (2) are including fixing stand (21) in jar body (1) upper portion through connecting rod (23), from top to bottom interval connection at a plurality of water conservancy diversion conical disks (22) of stand (21) annular outer wall, and is a plurality of the external diameter size of water conservancy diversion conical disk (22) increases from top to bottom in proper order, stirring mechanism (3) are including cross support (31) of sliding connection between jar body (1) both sides inner wall, main shaft (32) of locating in support (31) middle part, The upper rotating shaft (33) is arranged in the upper part of the bracket (31) and is in vertical transmission connection with the main rotating shaft (32), the lower rotating shaft (34) is arranged in the lower part of the bracket (31) and is in vertical transmission connection with the main rotating shaft (32), the first paddle (36) and the second paddle (37) are respectively in vertical transmission connection with the middle part of the upper rotating shaft (33), the third paddle (38) and the fourth paddle (39) are respectively in vertical transmission connection with the middle part of the lower rotating shaft (34), the main rotating shaft (32) is driven to rotate by a first motor (35) arranged in one side of the middle part of the bracket (31), the rotating directions of the upper rotating shaft (33) and the lower rotating shaft (34) are opposite, the first paddle (36), the second paddle (37), the third paddle (38) and the fourth paddle (39) are arranged in a circumferential staggered manner, and the rotating directions of the first paddle (36) and the fourth paddle (39) are the same, the rotation directions of the second blade (37) and the third blade (38) are the same, and the rotation directions of the first blade (36) and the third blade (38) are opposite.
2. The process for preparing regenerated semi-dull cationic fiber according to claim 1, wherein: the intrinsic viscosity of the PET master batch is 0.632 dl/g; the intrinsic viscosity of the regenerated PET cationic chip was 0.58 dl/g.
3. The process for preparing regenerated semi-dull cationic fiber according to claim 1, wherein: in the step (c), the screw extruder is provided with five heating zones, and the heating temperature of each zone is respectively as follows: 278 ℃ in the first zone, 284 ℃ in the second zone, 286 ℃ in the third zone, 288 ℃ in the fourth zone and 288 ℃ in the fifth zone; the extrusion pressure of the screw extruder is 12MPa, and the pressure after filtration is 9.5 MPa.
4. The process for preparing regenerated semi-dull cationic fiber according to claim 1, wherein: in the step (c), the temperature of the spinning box body is 286.5 ℃, and the pump supply amount of the metering pump is 35.4 g/min.
5. The process for preparing regenerated semi-dull cationic fiber according to claim 1, wherein: in the step (c), the heating temperature of the spinning assembly is 300 ℃, the pressure of the assembly is 10.8MPa, the spinning assembly comprises a filtering sand layer and an 800-mesh filtering net arranged below the filtering sand layer, and the filtering sand layer is steel sand of 40-60 meshes.
6. The process for preparing regenerated semi-dull cationic fiber according to claim 1, wherein: in the step (d), the temperature of post-heating treatment is 310 ℃, the wind speed of circular blowing cooling treatment is 50m/s, the oiling height of cluster oiling treatment is 1000mm, and the concentration ratio of the oiling agent is 11%.
7. The process for preparing regenerated semi-dull cationic fiber according to claim 1, wherein: in the step (d), the pre-network pressure is 0.08 mpa; when in drafting and setting, the speed of the first drafting roller is 2690m/min, and the speed of the second drafting roller is 2700 m/min; in the winding process, the winding speed was 2679m/min and the winding tension was 12 cN.
8. The process for preparing regenerated semi-dull cationic fiber according to claim 1, wherein: actuating mechanism (4) include mounting bracket (41), push rod (44), install cylinder cam (42), drive cylinder cam (42) pivoted second motor (43) in mounting bracket (41), push rod (44) one end stretches into jar body (1) and links firmly with support (31), push rod (44) other end stretches into in mounting bracket (41) and this push rod (44) tip through connecting rod (45) and cylinder cam (42) sliding connection who has roller (46), cylinder cam (42) circumferential direction drives push rod (44) up-and-down motion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
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