CN204174330U - The production system of energy-saving different dye fine count fiber - Google Patents
The production system of energy-saving different dye fine count fiber Download PDFInfo
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- CN204174330U CN204174330U CN201420495720.5U CN201420495720U CN204174330U CN 204174330 U CN204174330 U CN 204174330U CN 201420495720 U CN201420495720 U CN 201420495720U CN 204174330 U CN204174330 U CN 204174330U
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Abstract
The utility model discloses a kind of production system of energy-saving different dye fine count fiber, belong to spinning technique apparatus field, in the production system of a kind of energy-saving different dye fine count fiber disclosed in the utility model, by carrying out adaptability reform to the multiple parts in production system and carrying out the optimization of technique, thus both overcome the different dye fiber adopting production system of the prior art to make and longitudinally have obvious thickness to save, cause the problem bringing certain difficulty to weaving process, the different dye fiber also overcomed owing to adopting production system of the prior art to make causes the fabric that is made into more coarse, the problem of Silk weak effect, and then the fabric making the different dye fiber adopting production system of the present utility model to obtain make not only has feel as real silk and gloss, there is the style that nature is adopted more simultaneously, depth line contrast, length etc. all can be followed one's inclinations design as required, further meet the requirement of different user well.
Description
Technical field
The utility model relates to a kind of spinning production system of different dye fine count fiber, particularly relates to a kind of production system of energy-saving different dye fine count fiber.
Background technology
Along with improving constantly of people's living standard, people also improve constantly the personalization of clothes, variation and cheap and good-quality requirement.A kind of there is feel as real silk, light weight, the polyester filament at colorful, thin dawn be widely used in the exploitation of the new fabric of various Silk-Like.
The polyester filament of the different dye of longitudinal direction popular in the market often utilizes uneven pulling can change the theory of fibril aggregation state structure and obtain, and has one-step method and two step method in conventional production system.Obtained fiber has the features such as axially different dye, iso-fineness, different contraction, and be therefore also referred to as thickness joint silk, the fabric that fibrid is made into thus has picotement.
But, existing different dye fiber obtains often through employing uneven pulling, therefore different dye fiber longitudinally has obvious thickness to save, the elongation at break of fiber is more than 60%, boiling water shrinkage is more than 20%, and this brings certain difficulty to weaving process, and the fabric be simultaneously made into is more coarse, Silk weak effect, fabric and direct skin contact can feel significantly uncomfortable.
Utility model content
For above-mentioned Problems existing, the utility model provides a kind of production system of energy-saving different dye fine count fiber, longitudinally obvious thickness is had to save to overcome the different dye fiber adopting production system of the prior art to make, cause the problem bringing certain difficulty to weaving process, also the different dye fiber overcome owing to adopting production system of the prior art to make causes the fabric that is made into more coarse, the problem of Silk weak effect, thus the fabric making the different dye fiber adopting production system of the present utility model to obtain make not only has feel as real silk and gloss, there is the style that nature is adopted more simultaneously, depth line contrast, length etc. all can be followed one's inclinations design as required, and then meet the requirement of different user well.
To achieve these goals, the technical scheme that the utility model is taked is:
A production system for energy-saving different dye fine count fiber, wherein, comprises successively:
For carrying out pre-crystallized crystallization apparatus to section raw material;
For carrying out dry drying device to the section raw material after pre-crystallized;
For carrying out the screw extruder of melting, extruding, mixing and homogenizing to dried section raw material;
For the filter filtered the melt after screw extruder;
For carrying out mixed uniformly filter melt pipe to the melt after filtration;
For carrying out the spinning manifold of spinning technique to the melt after melt pipe;
For the cross air blowing device of cooling curing;
For the oil nozzle oiled;
For batching half-finished coiler device;
For carrying out the flat traction machine of drawing-off to spinning semi-finished product;
Wherein, described flat traction machine comprises wire feed roller, the first heat dish, the second heat dish, the 3rd heat dish and winding.
The production system of above-mentioned energy-saving different dye fine count fiber, wherein, described spinning manifold comprises: for the biphenyl system of cabinet insulation, for the measuring pump of the melt of accurate-metering after described melt pipe, for spraying the filament spinning component of one-to-two or one point of three or two points of three spinning.
The production system of above-mentioned energy-saving different dye fine count fiber, wherein, the biphenyl heating for manifold insulation adopts the power save mode of heat-conducting oil heating biphenyl.
The production system of above-mentioned energy-saving different dye fine count fiber, wherein, described measuring pump comprises motors of metering pumps and frequency converter, and between described motors of metering pumps and frequency converter, foundation has closed-loop control system.
The production system of above-mentioned energy-saving different dye fine count fiber, wherein, described oil nozzle adopts the thin dawn oil nozzle in Japanese Tang Qian road.
The production system of above-mentioned energy-saving different dye fine count fiber, wherein, the cam of the winding head of described coiler device is evenly provided with the groove of multiple repetition.
The production system of above-mentioned energy-saving different dye fine count fiber, wherein, the 3rd heat dish outer surface of the flat traction machine of described rear road stretching is arranged with the stainless steel sleeve of different zigzag fashion, to carry out irregular sizing to tow.
The production system of above-mentioned energy-saving different dye fine count fiber, wherein, the front end of described screw extruder is provided with low temperature mixing refining head, to realize segmentation and regionalization heating.
Technique scheme tool has the following advantages or beneficial effect:
In the production system of the energy-saving different dye fine count fiber that the utility model provides, by carrying out adaptability reform to the multiple parts in production system and carrying out the optimization of technique, thus both overcome the different dye fiber adopting production system of the prior art to make and longitudinally have obvious thickness to save, cause the problem bringing certain difficulty to weaving process, the different dye fiber also overcomed owing to adopting production system of the prior art to make causes the fabric that is made into more coarse, the problem of Silk weak effect, and then the fabric making the different dye fiber adopting production system of the present utility model to obtain make not only has feel as real silk and gloss, there is the style that nature is adopted more simultaneously, depth line contrast, length etc. all can be followed one's inclinations design as required, further meet the requirement of different user well.
Accompanying drawing explanation
By reading the detailed description done non-limiting example with reference to the following drawings, the utility model and feature, profile and advantage will become more apparent.Mark identical in whole accompanying drawing indicates identical part.Deliberately proportionally do not draw accompanying drawing, focus on purport of the present utility model is shown.
The structural representation of the production system of the energy-saving different dye fine count fiber that Fig. 1 provides for the utility model embodiment 1;
Fig. 2 is the structural representation of the flat traction machine in the production system of the energy-saving different dye fine count fiber provided in prior art;
Fig. 3 is the structural representation of the flat traction machine in the production system of the energy-saving different dye fine count fiber that the utility model embodiment 1 provides;
Fig. 4 is the structural representation of the 3rd heat dish in the production system of the energy-saving different dye fine count fiber that the utility model embodiment 1 provides.
Detailed description of the invention
Below in conjunction with accompanying drawing and specific embodiment, the utility model is further described, but not as restriction of the present utility model.
Embodiment 1:
The structural representation of the production system of the energy-saving different dye fine count fiber that Fig. 1 provides for the utility model embodiment 1, as shown in the figure, the production system of the energy-saving different dye fine count fiber that the utility model embodiment 1 provides comprises: for carrying out pre-crystallized crystallization apparatus 101 to section raw material, for carrying out dry drying device 102 to the section raw material after pre-crystallized, for carrying out melting to dried section raw material, extruding, the screw extruder 103 of mixing and homogenizing, for the filter 107 filtered the melt after screw extruder, for carrying out mixed uniformly filter melt pipe 105 to the melt after filtration, for carrying out the spinning manifold 104 of spinning technique to the melt after melt pipe, for the cross air blowing device 108 to spinning cooling curing, for the oil nozzle (not shown) oiled, for the coiler device 106 of tow winding and the flat traction machine (flat traction machine as shown in Figure 3) for carrying out drawing-off to spinning semi-finished product, wherein, flat traction machine comprises wire feed roller 10, first heat dish 11, second heat dish the 12, the 3rd heat dish 13 and winding 14.The speed of spinning silk winding is at 1800m/min ~ 3200m/min, and putting down and leading winding speed is 300m/min ~ 800m/min, all can adjust according to different-style; Section raw material adopts conventional PET to cut into slices or modified PET section (as cationic-dyeable) comprises conventional half light section (FD), High Temperature High Pressure can contaminate CATION section (CDP), the section of normal-temperature normal-pressure dyeable CATION (ECDP), full-dull polyester (SD), large bright chip etc., can select according to the needs of client, simultaneously, carrying out in drying process, the pre-crystallization temperature of FD is 170-175 DEG C, baking temperature is 160-165 DEG C, drying time is 4-6 hour, dry air dew point≤-70 DEG C; The pre-crystallization temperature of CDP is 155-160 DEG C, baking temperature is 140-150 DEG C, drying time is 5-7 hour, dry air dew point≤-70 DEG C; The pre-crystallization temperature of ECDP is 140-145 DEG C, baking temperature is 160-170 DEG C, drying time is 5-7 hour, dry air dew point≤-70 DEG C; The pre-crystallization temperature of SD is 160-170 DEG C, baking temperature is 150-160 DEG C, drying time is 5-7 hour, dry air dew point≤-70 DEG C; After chip drying, moisture content≤0.002% of FD, SD section, moisture content≤0.003% of CDP, ECDP section.
In the production system of the energy-saving different dye fine count fiber provided in the utility model embodiment 1, the front end of screw extruder 103 is provided with low temperature mixing refining head, to realize segmentation and regionalization heating; FD screw rod five district temperature is between 290-300 DEG C, higher than heavy denier yarn 5 ~ 10 DEG C; CDP screw rod five district temperature is between 280-295 DEG C; ECDP screw rod five district temperature is between 275-293 DEG C; SD screw rod five district temperature is respectively between 285-295 DEG C.In a word, the selection of spinning temperature is higher than heavy denier yarn 5 ~ 10 DEG C, to improve fluidity of molten, thus meets fine denier filament production requirement.
In the production system of the energy-saving different dye fine count fiber provided in the utility model embodiment 1, filter 107 adopts the filter of 25 below μ, and after setting filter, pressure is more than 12MPa.
In the production system of the energy-saving different dye fine count fiber provided in the utility model embodiment 1, spinning manifold 104 comprises: for the measuring pump (not shown) of the melt of accurate-metering after described melt pipe, for spraying the filament spinning component (not shown) of tow, wherein, measuring pump comprises motors of metering pumps and frequency converter, and between motors of metering pumps and frequency converter, foundation has closed-loop control system; Simultaneously, coiler device 106 corresponds to the one-to-two of filament spinning component or the increase of one point of three or two points of third-class tow, accordingly oil nozzle, the nozzle of interlace, thread guide etc. are increased, again make to increase groove number to match with spinning head quantity to winding head cam simultaneously.
In the production system of the energy-saving different dye fine count fiber provided in the utility model embodiment 1, coiler device 106 comprises the pre-the nozzle of interlace 65 for pre-network spray silk, for the godet roller 62 of seal wire, for reeling and being evenly provided with the cam 63 (according to spinning cake Thickness Design groove) of the groove of multiple repetition, and the spinning cake 64 of winding shaping.
In the production system of the energy-saving different dye fine count fiber provided in the utility model embodiment 1, oil nozzle adopts the thin dawn oil nozzle in Japanese Tang Qian road, the thin dawn oil nozzle in Japanese Tang Qian road is adopted to make to oil evenly, few to tow wearing and tearing, oil content controls between 0.6-0.8%, and the spinning tension that can reduce tow is also conducive to oiling evenly simultaneously.
Wherein, cross air blowing device 108 is provided with pressure stabilizing chamber at the rear portion of spinning window, the air outlet position of pressure stabilizing chamber is positioned at the rear portion of spinning window spinning, the air outlet place of pressure stabilizing chamber is fixed with one group of stainless steel cloth successively, one deck cellular board and one deck stainless steel cloth, cellular board is evenly equipped with some apertures, one group of stainless steel cloth is made up of three layers of stainless steel cloth, three layers of stainless steel cloth are left layer stainless steel cloth, intermediate layer stainless steel cloth, right layer stainless steel cloth, and intermediate layer stainless steel cloth mesh is finer and closely woven than the mesh of left and right layer stainless steel cloth.Its blowing evenly, and reduces the consumption of cooling air under identical cooling effect, improves the quality homogeneity of tow.The size of lateral blowing according to rolled product variety adjustment, generally within the scope of 0.35 ~ 0.55m/min.
Simultaneously, filament spinning component is transformed into the spinning pack of one-to-two or one point of three or two points of three spinning by the spinning pack of former single component one synnema, the key of this transformation is the uniformity keeping every bundle fiber fiber number, therefore to the deflector of filament spinning component, distribution plate design and component filters medium, the control of filter condition, fully to keep melt isostasy in assembly, simultaneously, adopt the good metal sand of strainability as filtering material, the order number of metal sand is between 60 ~ 120 orders, and can adjust according to description, Assurance component initial pressure is at more than 15MPa, spinnerets hole shape can design as required, circular or special-shaped, and how little hole count is also can design arbitrarily as required, in addition, because measuring pump control model is frequency converter adjusted open loop before transformation, the speed error of measuring pump can not be revised in real time, a more serious problem concerning spinning thin denier monofilaments, add that the utility model patented product is again a point fibril, therefore we set up closed-loop control system by between motors of metering pumps and frequency converter, the rotating speed of motors of metering pumps can be revised in real time, thus ensure that the homogeneous constant of spinning melt output quantity, meanwhile, in the process, electrical heating biphenyl mode changes the power save mode of heat-conducting oil heating biphenyl into, thus makes biphenyl heating electric expense reduce by more than 1/3 ~ 2/3, greatly reduces energy consumption.
Fig. 2 is the structural representation of the flat traction machine in the production system of the energy-saving different dye fine count fiber provided in prior art; As shown in the figure, the flat traction machine in the production system of the different dye fine count fiber provided in prior art comprises: wire feed roller 00, heat dish 01, hot plate 02, cold dish 03 and winding 04; Fig. 3 is the structural representation of the flat traction machine in the production system of the energy-saving different dye fine count fiber that the utility model embodiment 1 provides; Fig. 4 is the structural representation of the 3rd heat dish in the production system of the energy-saving different dye fine count fiber that the utility model embodiment 1 provides; As shown in the figure, the flat traction machine in the production system of energy-saving different dye fine count fiber that provides of the utility model embodiment 1 comprises: wire feed roller 10, first heat dish 11, second heat dish the 12, the 3rd heat dish 13 and winding 14; In the production system of the different dye fine count fiber of efficient bull provided in the utility model embodiment 1; relevant transformation has been carried out to rear road flat traction machine; specifically comprise: remove the hot plate 02 in existing system; hot plate position 02 increases by one group of second heat dish 12; cold dish 03 originally changes the 3rd heat dish 13 into; control degree temperature range is in normal temperature ~ 250 DEG C, and the outer surface of the 3rd heat dish 13 is arranged with the stainless steel sleeve 130 of different zigzag fashion, to carry out irregular sizing to spinning.
When adopting flat traction machine to carry out drawing-off, speed is at 300m/min ~ 800m/min, and the temperature of the first heat dish 11 controls between 70 ~ 90 DEG C, and the tow wrapping wire number of turns is 3 ~ 5 circles; The temperature of the second heat dish 12 controls between normal temperature ~ 150 DEG C, and the tow wrapping wire number of turns is 3 ~ 8 circles; The temperature of the 3rd heat dish 13 controls between 150 ~ 280 DEG C, and the tow wrapping wire number of turns is 1 ~ 3 circle; DR1 (the first heat dish 11 compares with the linear velocity of wire feed roller 10) is 0.011; DR2 (the second heat dish 12 and the first heat coil the linear velocity ratio of 11) is between 1.5 ~ 3.0; OF1 (the second heat dish 12 overfeedings the 3rd heat dish 13), between 1-10%, regulates according to product style; Between OF2 (the 3rd heat dish 13 overfeeding winding 14) 1-10%, according to shaping adjustment winding tension; Wherein, 3rd heat dish 13 is mainly fiber sizing and uses, and adopt the stainless steel sleeve 130 of overcoat one square odontoid, object be make fiber in type-approval process fiber axis to not by continuously by HEAT SETTING, thus make fiber axis variant to macromolecular structure, by the segment of fiber of being heated because of high-temperature shaping, make macromolecule internal degree of crystallinity higher than the degree of crystallinity of non-bringing-up section fiber, cause fiber in the use procedure of rear road, produce different dye effect, the depth of different dye controls by draw ratio and setting temperature.
When the production system of the energy-saving different dye fine count fiber adopting the utility model embodiment 1 to provide is produced, section raw material is through conveying, pre-crystallized, dry, enter screw extruder, extrude from head after melting, extruding, mixing, homogenizing in screw extruder, enter spinning manifold carry out spinning through filter, melt pipe; Melt, after spinning pump accurate-metering, is sprayed from spinnerets by filament spinning component, and after cross air blowing device cooling curing, through oiling, after godet roller, pre-the nozzle of interlace, winding shaping obtains POY or MOY silk semi-finished product; Then on flat traction machine, carry out drawing-off, thus obtain final spinning.
So, in the production system of the energy-saving different dye fine count fiber that the utility model provides, by carrying out adaptability reform to the multiple parts in production system and carrying out the optimization of technique, thus both overcome the different dye fiber adopting production system of the prior art to make and longitudinally have obvious thickness to save, cause the problem bringing certain difficulty to weaving process, the different dye fiber also overcomed owing to adopting production system of the prior art to make causes the fabric that is made into more coarse, the problem of Silk weak effect, and then the fabric making the different dye fiber adopting production system of the present utility model to obtain make not only has feel as real silk and gloss, there is the style that nature is adopted more simultaneously, depth line contrast, length etc. all can be followed one's inclinations design as required, further meet the requirement of different user well.
It should be appreciated by those skilled in the art that those skilled in the art can realize described change case in conjunction with prior art and above-described embodiment, do not repeat them here.Such change case does not affect flesh and blood of the present utility model, does not repeat them here.
Above preferred embodiment of the present utility model is described.It is to be appreciated that the utility model is not limited to above-mentioned particular implementation, the equipment wherein do not described in detail to the greatest extent and structure are construed as to be implemented with the common mode in this area; Any those of ordinary skill in the art, make many possible variations and modification not departing from technical solutions of the utility model, or be revised as the Equivalent embodiments of equivalent variations, this does not affect flesh and blood of the present utility model.Therefore, every content not departing from technical solutions of the utility model, according to technical spirit of the present utility model to any simple modification made for any of the above embodiments, equivalent variations and modification, all still belongs in the scope of technical solutions of the utility model protection.
Claims (8)
1. a production system for energy-saving different dye fine count fiber, is characterized in that, comprise successively:
For carrying out pre-crystallized crystallization apparatus to section raw material;
For carrying out dry drying device to the section raw material after pre-crystallized;
For carrying out the screw extruder of melting, extruding, mixing and homogenizing to dried section raw material;
For the filter filtered the melt after screw extruder;
For the melt pipe carried the melt after filtration;
For carrying out the spinning manifold of spinning to the melt after melt pipe;
For the cross air blowing device of cooling curing;
For the oil nozzle oiled;
For batching half-finished coiler device;
For carrying out the flat traction machine of drawing-off to spinning semi-finished product;
Wherein, described flat traction machine comprises wire feed roller, the first heat dish, the second heat dish, the 3rd heat dish and winding.
2. the production system of energy-saving different dye fine count fiber as claimed in claim 1, is characterized in that, institute
State spinning manifold to comprise: for the biphenyl system of cabinet insulation, for accurate-metering through described melt pipe
After the measuring pump of melt, for spraying the filament spinning component of one-to-two or one point of three or two points of three spinning.
3. the production system of energy-saving different dye fine count fiber as claimed in claim 2, is characterized in that, uses
In the power save mode of the biphenyl heating employing heat-conducting oil heating biphenyl of manifold insulation.
4. the production system of energy-saving different dye fine count fiber as claimed in claim 2, is characterized in that, institute
State measuring pump and comprise motors of metering pumps and frequency converter, and between described motors of metering pumps and frequency converter, foundation is closed
Ring control system.
5. the production system of energy-saving different dye fine count fiber as claimed in claim 1, is characterized in that, institute
State oil nozzle and adopt the thin dawn oil nozzle in Japanese Tang Qian road.
6. the production system of energy-saving different dye fine count fiber as claimed in claim 1, is characterized in that, institute
The cam stating the winding head of coiler device is evenly provided with the groove of multiple repetition.
7. the production system of energy-saving different dye fine count fiber as claimed in claim 1, is characterized in that, institute
The 3rd heat dish outer surface stating flat traction machine is arranged with the stainless steel sleeve of different zigzag fashion, with
Irregular sizing is carried out to tow.
8. the production system of energy-saving different dye fine count fiber as claimed in claim 1, is characterized in that, institute
The front end stating screw extruder is provided with low temperature mixing refining head, to realize segmentation and regionalization heating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420495720.5U CN204174330U (en) | 2014-08-29 | 2014-08-29 | The production system of energy-saving different dye fine count fiber |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420495720.5U CN204174330U (en) | 2014-08-29 | 2014-08-29 | The production system of energy-saving different dye fine count fiber |
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| CN204174330U true CN204174330U (en) | 2015-02-25 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104195661A (en) * | 2014-08-29 | 2014-12-10 | 绍兴文理学院 | Energy-saving metachromatic fine denier fiber production system |
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2014
- 2014-08-29 CN CN201420495720.5U patent/CN204174330U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104195661A (en) * | 2014-08-29 | 2014-12-10 | 绍兴文理学院 | Energy-saving metachromatic fine denier fiber production system |
| CN104195661B (en) * | 2014-08-29 | 2017-01-11 | 绍兴文理学院 | Energy-saving metachromatic fine denier fiber production system |
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