CN103388184B - Spinning Process of Low Melting Point Polymer - Google Patents
Spinning Process of Low Melting Point Polymer Download PDFInfo
- Publication number
- CN103388184B CN103388184B CN201310336181.0A CN201310336181A CN103388184B CN 103388184 B CN103388184 B CN 103388184B CN 201310336181 A CN201310336181 A CN 201310336181A CN 103388184 B CN103388184 B CN 103388184B
- Authority
- CN
- China
- Prior art keywords
- polymer
- temperature
- silk
- spinning
- melting point
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Artificial Filaments (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Abstract
Description
技术领域technical field
本发明涉及纺丝工艺,特别涉及一种低熔点聚合物的纺丝工艺。The invention relates to a spinning process, in particular to a low-melting point polymer spinning process.
背景技术Background technique
现有的低熔点聚合物的纺丝工艺通常采用聚酯(PET)、聚酰胺(PA)、聚乙烯(PE)、丙烯(PP)等作为原料。The existing low-melting point polymer spinning process usually uses polyester (PET), polyamide (PA), polyethylene (PE), propylene (PP) and the like as raw materials.
对于熔点50℃-70℃的聚合物,由于其低熔点和低温度结晶的特性,使得聚合物的纺丝工艺控制要求较高。尤其对于聚己内酯(PCL)这种低熔点热塑性聚合物,其吸水性很强,且熔点只有60℃-63℃,把其作为原料的纺丝工艺尚未见报。For polymers with a melting point of 50°C-70°C, due to their low melting point and low-temperature crystallization characteristics, the requirements for polymer spinning process control are relatively high. Especially for this low-melting thermoplastic polymer of polycaprolactone (PCL), its water absorption is very strong, and its fusing point is only 60 ℃-63 ℃, and the spinning process using it as raw material has not been reported yet.
发明内容Contents of the invention
本发明所要解决的技术问题在于提供一种低熔点聚合物的纺丝工艺。The technical problem to be solved by the present invention is to provide a spinning process for low-melting polymers.
在本发明还提供一种低熔点聚合物的纺丝工艺,用熔点50℃-70℃的聚合物原料,通过纺丝设备,纺制出熔点为50℃-70℃的聚合物长丝,其工艺流程如下:The present invention also provides a low-melting-point polymer spinning process, using polymer raw materials with a melting point of 50°C-70°C, through spinning equipment, to spin polymer filaments with a melting point of 50°C-70°C, which The process flow is as follows:
S1:将聚合物真空干燥,干燥后聚合物的湿度为1%-20%,温度40℃-50℃;S2:采用熔融纺丝机,将干燥后的聚合物倒入料桶,采用熔融温度为200℃-300℃,熔融5-10分钟,此时聚合物变成流体,经螺杆挤出,过喷丝头喷出丝线,丝线需经过工业空调的风道冷却,使丝线温度降为-20℃-20℃;S3:将冷却后的丝线导入分丝辊拉伸,然后导入冷辊,经分丝辊可将丝线拉伸2-10倍,拉伸时温度为20℃-40℃;S4:收丝时采用工业的卷绕头,卷绕头的卷绕速度为1000m/min-5000m/min,收丝时冷辊的温度为10℃-20℃。S1: Dry the polymer in vacuum, the humidity of the dried polymer is 1%-20%, and the temperature is 40°C-50°C; S2: Use a melt spinning machine, pour the dried polymer into the barrel, and use the melting temperature The temperature is 200℃-300℃, melting for 5-10 minutes, at this time, the polymer becomes fluid, extruded by the screw, and the silk is sprayed out through the spinneret, and the silk needs to be cooled by the air duct of the industrial air conditioner to reduce the temperature of the silk to - 20°C-20°C; S3: Lead the cooled thread to the splitting roller for stretching, and then lead it to the cooling roll, the thread can be stretched 2-10 times through the splitting roller, and the temperature during stretching is 20°C-40°C; S4: An industrial winding head is used for winding, the winding speed of the winding head is 1000m/min-5000m/min, and the temperature of the cold roll is 10°C-20°C during winding.
进一步地,所述熔融温度为200℃,熔融5分钟,所述拉伸时温度为20℃,收丝时所述冷辊的温度为10℃。Further, the melting temperature is 200° C. for 5 minutes, the temperature during stretching is 20° C., and the temperature of the cooling roll is 10° C. during drawing.
进一步地,所述熔融温度为300℃,熔融10分钟,所述拉伸时温度为40℃,收丝时所述冷辊的温度为20℃。Further, the melting temperature is 300° C. for 10 minutes, the temperature during stretching is 40° C., and the temperature of the cooling roll is 20° C. during drawing.
进一步地,所述熔融温度为250℃,熔融8分钟,所述拉伸时温度为30℃,收丝时所述冷辊的温度为15℃。Further, the melting temperature is 250°C for 8 minutes, the stretching temperature is 30°C, and the cooling roll temperature is 15°C when drawing.
进一步地,所述聚合物是聚己内酯。Further, the polymer is polycaprolactone.
进一步地,所述纺丝工艺原料采用100份聚己内酯与0.1份-1份的增韧剂和0.1份-1份的老化剂混合均匀。Further, 100 parts of polycaprolactone, 0.1-1 part of toughening agent and 0.1-1 part of aging agent are uniformly mixed as raw materials for the spinning process.
采用本发明提供的低熔点聚合物的纺丝工艺,工艺流程简单实用,可将熔点50℃-70℃的聚合物纺织成工业级的丝线。By adopting the spinning process of the low-melting polymer provided by the invention, the technological process is simple and practical, and the polymer having a melting point of 50°C-70°C can be spun into industrial-grade silk.
附图说明Description of drawings
此处所说明的附图用来提供对本发明的进一步理解,构成本申请的一部分,本发明的示意性实施例及其说明用于解释本发明,并不构成对本发明的不当限定。在附图中:The accompanying drawings described here are used to provide a further understanding of the present invention and constitute a part of the application. The schematic embodiments of the present invention and their descriptions are used to explain the present invention and do not constitute improper limitations to the present invention. In the attached picture:
图1示意性示意出本发明实施例子给出的纺丝设备。Fig. 1 schematically shows the spinning equipment given in the embodiment example of the present invention.
具体实施方式detailed description
下面将参考附图并结合实施例,来详细说明本发明。The present invention will be described in detail below with reference to the accompanying drawings and in combination with embodiments.
实施例1Example 1
在本实施例提供一种纺丝设备,包括熔融纺丝机1、喷丝头2、工业空调及其风道3、分丝设备4和收丝设备7,分丝设备上4设置有分丝辊5和冷辊6,收丝设备7上设置有卷绕头8。物料通过熔融纺丝机1熔融作用后变成流体,经螺杆挤出,过喷丝头2喷出丝线,丝线进入风道3,风道3由工业空调制冷,温度为0℃-15℃;物料从风道3出来通过分丝辊5和冷辊6,到达卷绕头8收丝。In this embodiment, a kind of spinning equipment is provided, including a melt spinning machine 1, a spinneret 2, an industrial air conditioner and its air duct 3, a splitting device 4 and a spinning device 7, and the splitting device 4 is provided with a splitting The roll 5 and the cold roll 6 are provided with a winding head 8 on the wire-receiving device 7 . The material becomes a fluid after being melted by the melt spinning machine 1, extruded by the screw, and the silk thread is sprayed out through the spinneret 2, and the thread enters the air duct 3, and the air duct 3 is refrigerated by the industrial air conditioner, and the temperature is 0°C-15°C; The material comes out from the air channel 3, passes through the splitting roller 5 and the cooling roller 6, and reaches the winding head 8 for winding.
在本实施例还提供一种低熔点聚合物的纺丝工艺,用熔点50℃-70℃的聚合物原料,通过上述纺丝设备,纺制出熔点为50℃-70℃的聚合物长丝,其工艺流程如下:This embodiment also provides a low-melting point polymer spinning process, using polymer raw materials with a melting point of 50°C-70°C, through the above spinning equipment, to spin polymer filaments with a melting point of 50°C-70°C , its technological process is as follows:
S1:将聚合物真空干燥,干燥后聚合物的湿度为1%-20%,温度40℃-50℃,时间视干燥机的性能而定,这样,干燥后的聚合物能达到纺丝级用;S1: Dry the polymer in vacuum. After drying, the humidity of the polymer is 1%-20%, and the temperature is 40°C-50°C. The time depends on the performance of the dryer. In this way, the dried polymer can reach the spinning grade. ;
S2:采用熔融纺丝机1,将干燥后的聚合物倒入料桶,采用熔融温度为200℃,熔融5分钟,此时聚合物变成流体,经螺杆挤出,经喷丝头2喷出丝线,调整计量泵来控制丝的粗细;丝线需经过工业空调的风道3冷却,使丝线温度降为-20℃-20℃;S2: Using melt spinning machine 1, pour the dried polymer into the material barrel, adopt a melting temperature of 200°C, and melt for 5 minutes. At this time, the polymer becomes fluid, extruded through the screw, and sprayed through the spinneret 2 Out of the silk thread, adjust the metering pump to control the thickness of the thread; the silk thread needs to be cooled by the air duct 3 of the industrial air conditioner to reduce the temperature of the thread to -20°C-20°C;
S3:将冷却后的丝线导入分丝辊5拉伸,然后导入冷辊6,经分丝辊5可将丝线拉伸2-10倍,这样可增加丝的强度和韧度,拉伸时温度为20℃,拉伸过程需要上油;S3: Lead the cooled silk thread to the splitting roller 5 for stretching, and then lead it to the cooling roller 6. The thread can be stretched 2-10 times through the splitting roller 5, which can increase the strength and toughness of the thread. 20°C, oiling is required during the stretching process;
S4:收丝时采用工业的卷绕头8,卷绕头8的转速需与分丝辊5和冷辊6的速度一致,卷绕速度为1000m/min-5000m/min,以免在收丝过程中断丝,收丝时冷辊6的温度为10℃,收丝后成品在0℃-50℃的条件下存放。S4: Industrial winding head 8 is used for winding. The speed of winding head 8 must be consistent with the speed of splitting roller 5 and cooling roller 6. The winding speed is 1000m/min-5000m/min to avoid The temperature of the cold roll 6 is 10°C when the wire is cut, and the finished product is stored at 0°C-50°C after the wire is collected.
实施例2Example 2
在本发明实施例提供一种低熔点聚合物的纺丝工艺,用熔点50℃-70℃的聚合物原料,通过上述纺丝设备,纺制出熔点为50℃-70℃的聚合物长丝,其工艺流程如下:In the embodiment of the present invention, a low-melting-point polymer spinning process is provided, using polymer raw materials with a melting point of 50°C-70°C, through the above-mentioned spinning equipment, to spin polymer filaments with a melting point of 50°C-70°C , its technological process is as follows:
S1:将聚合物真空干燥,干燥后聚合物的湿度为1%-20%,温度40℃-50℃,时间视干燥机的性能而定,这样,干燥后的聚合物能达到纺丝级用;S1: Dry the polymer in vacuum. After drying, the humidity of the polymer is 1%-20%, and the temperature is 40°C-50°C. The time depends on the performance of the dryer. In this way, the dried polymer can reach the spinning grade. ;
S2:采用熔融纺丝机1,将干燥后的聚合物倒入料桶,采用熔融温度为300℃,熔融10分钟,此时聚合物变成流体,经螺杆挤出,经喷丝头2喷出丝线,调整计量泵来控制丝的粗细;丝线需经过工业空调的风道3冷却,使丝线温度降为-20℃-20℃;S2: Using melt spinning machine 1, pour the dried polymer into the material barrel, adopt a melting temperature of 300°C, and melt for 10 minutes. At this time, the polymer becomes fluid, extruded through the screw, and sprayed through the spinneret 2 Out of the silk thread, adjust the metering pump to control the thickness of the thread; the thread needs to be cooled by the air duct 3 of the industrial air conditioner, so that the temperature of the thread will drop to -20°C-20°C;
S3:将冷却后的丝线导入分丝辊5拉伸,然后导入冷辊6,经分丝辊5可将丝线拉伸2-10倍,这样可增加丝的强度和韧度,拉伸时温度为40℃,拉伸过程需要上油;S3: Lead the cooled silk thread to the splitting roller 5 for stretching, and then lead it to the cooling roller 6. The thread can be stretched 2-10 times through the splitting roller 5, which can increase the strength and toughness of the thread. 40°C, oiling is required during the stretching process;
S4:收丝时采用工业的卷绕头8,卷绕头8的转速需与分丝辊5和冷辊6的速度一致,卷绕速度为1000m/min-5000m/min,以免在收丝过程中断丝,收丝时冷辊6的温度为20℃,收丝后成品在0℃-50℃的条件下存放。S4: Industrial winding head 8 is used for winding. The speed of winding head 8 must be consistent with the speed of splitting roller 5 and cooling roller 6. The winding speed is 1000m/min-5000m/min to avoid The temperature of the cold roll 6 is 20°C when the wire is cut, and the finished product is stored at 0°C-50°C after the wire is collected.
实施例3Example 3
在本发明实施例提供一种低熔点聚合物的纺丝工艺,用熔点50℃-70℃的聚合物原料,通过上述纺丝设备,纺制出熔点为50℃-70℃的聚合物长丝,其工艺流程如下:In the embodiment of the present invention, a low-melting-point polymer spinning process is provided, using polymer raw materials with a melting point of 50°C-70°C, through the above-mentioned spinning equipment, to spin polymer filaments with a melting point of 50°C-70°C , its technological process is as follows:
S1:将聚合物真空干燥,干燥后聚合物的湿度为1%-20%,温度40℃-50℃,时间视干燥机的性能而定,这样,干燥后的聚合物能达到纺丝级用;S1: Dry the polymer in vacuum. After drying, the humidity of the polymer is 1%-20%, and the temperature is 40°C-50°C. The time depends on the performance of the dryer. In this way, the dried polymer can reach the spinning grade. ;
S2:采用熔融纺丝机1,将干燥后的聚合物倒入料桶,采用熔融温度为250℃,熔融8分钟,此时聚合物变成流体,经螺杆挤出,经喷丝头2喷出丝线,调整计量泵来控制丝的粗细;丝线需经过工业空调的风道3冷却,使丝线温度降为-20℃-20℃;S2: Using melt spinning machine 1, pour the dried polymer into the material barrel, adopt a melting temperature of 250°C, and melt for 8 minutes. At this time, the polymer becomes fluid, extruded through the screw, and sprayed through the spinneret 2 Out of the silk thread, adjust the metering pump to control the thickness of the thread; the silk thread needs to be cooled by the air duct 3 of the industrial air conditioner to reduce the temperature of the thread to -20°C-20°C;
S3:将冷却后的丝线导入分丝辊5拉伸,然后导入冷辊6,经分丝辊5可将丝线拉伸2-10倍,这样可增加丝的强度和韧度,拉伸时温度为30℃,拉伸过程需要上油;S3: Lead the cooled silk thread to the splitting roller 5 for stretching, and then lead it to the cooling roller 6. The thread can be stretched 2-10 times through the splitting roller 5, which can increase the strength and toughness of the thread. 30°C, oiling is required during the stretching process;
S4:收丝时采用工业的卷绕头8,卷绕头8的转速需与分丝辊5和冷辊6的速度一致,卷绕速度为1000m/min-5000m/min,以免在收丝过程中断丝,收丝时冷辊6的温度为15℃,收丝后成品在0℃-50℃的条件下存放。S4: Industrial winding head 8 is used for winding. The speed of winding head 8 must be consistent with the speed of splitting roller 5 and cooling roller 6. The winding speed is 1000m/min-5000m/min to avoid The temperature of the cold roll 6 is 15°C when the wire is cut, and the finished product is stored under the condition of 0°C-50°C after the wire is collected.
实施例4Example 4
在本实施例提供一种低熔点聚合物的纺丝工艺,用熔点60℃-63℃的聚己内酯作为原料,通过上述纺丝设备,纺制出熔点为60℃-63℃的聚合物长丝。In this embodiment, a spinning process of a low-melting polymer is provided, using polycaprolactone with a melting point of 60°C-63°C as a raw material, and spinning a polymer with a melting point of 60°C-63°C through the above-mentioned spinning equipment filament.
相对于实施例1,作为原料的聚己内酯吸水性较强,因此采用100份聚己内酯原料与0.1份-1份的增韧剂和0.1份-1份的老化剂混合均匀,使聚己内酯改性。Compared with Example 1, polycaprolactone as a raw material has stronger water absorption, so 100 parts of polycaprolactone raw materials are used to mix evenly with 0.1-1 part of toughening agent and 0.1-1 part of aging agent, so that Polycaprolactone modified.
从以上描述可以看出,采用本发明提供的低熔点聚合物的纺丝工艺,达到以下技术效果:工艺流程简单实用,可以将熔点50℃-70℃的聚合物纺织成工业级的丝线。It can be seen from the above description that the spinning process of the low-melting point polymer provided by the present invention achieves the following technical effects: the process flow is simple and practical, and the polymer with a melting point of 50°C-70°C can be spun into industrial-grade silk.
以上所述仅为本发明的优选实施例而已,并不用于限制本发明,对于本领域的技术人员来说,本发明可以有各种更改和变化。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. For those skilled in the art, the present invention may have various modifications and changes. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included within the protection scope of the present invention.
Claims (6)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310336181.0A CN103388184B (en) | 2013-08-05 | 2013-08-05 | Spinning Process of Low Melting Point Polymer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310336181.0A CN103388184B (en) | 2013-08-05 | 2013-08-05 | Spinning Process of Low Melting Point Polymer |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103388184A CN103388184A (en) | 2013-11-13 |
CN103388184B true CN103388184B (en) | 2016-02-24 |
Family
ID=49532601
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310336181.0A Expired - Fee Related CN103388184B (en) | 2013-08-05 | 2013-08-05 | Spinning Process of Low Melting Point Polymer |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103388184B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103643475A (en) * | 2013-11-30 | 2014-03-19 | 常熟涤纶有限公司 | Production process of cool cotton-feel polyester low stretch yarns |
CN104862820A (en) * | 2015-05-18 | 2015-08-26 | 中国水产科学研究院东海水产研究所 | Method for preparing filaments for net weaving |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0491947A1 (en) * | 1989-08-04 | 1992-07-01 | Kao Corporation | Polyester fiber |
CN1810303A (en) * | 2006-02-24 | 2006-08-02 | 东华大学 | Tissue engineering carrier material of polycaprolactone and its prepn process |
CN101302651A (en) * | 2008-06-05 | 2008-11-12 | 江苏盛虹化纤有限公司 | Processing method of nylon monofilament |
CN101555646A (en) * | 2008-04-10 | 2009-10-14 | 周焕民 | Processing method for fibre-forming of low-melting chinlon bonding fibre |
-
2013
- 2013-08-05 CN CN201310336181.0A patent/CN103388184B/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0491947A1 (en) * | 1989-08-04 | 1992-07-01 | Kao Corporation | Polyester fiber |
CN1810303A (en) * | 2006-02-24 | 2006-08-02 | 东华大学 | Tissue engineering carrier material of polycaprolactone and its prepn process |
CN101555646A (en) * | 2008-04-10 | 2009-10-14 | 周焕民 | Processing method for fibre-forming of low-melting chinlon bonding fibre |
CN101302651A (en) * | 2008-06-05 | 2008-11-12 | 江苏盛虹化纤有限公司 | Processing method of nylon monofilament |
Non-Patent Citations (1)
Title |
---|
低熔点聚酯纤维的纺丝工艺研究;曾新;《合成纤维》;20040131;第33卷(第1期);第19-21页 * |
Also Published As
Publication number | Publication date |
---|---|
CN103388184A (en) | 2013-11-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103590139B (en) | A kind of powerful three-dimensional crimp memory fiber and manufacture method thereof | |
CN104018239B (en) | Production method of antibacterial polyester industrial yarn | |
CN107012522B (en) | Produce the production line and its production technology of the compound short fibre of Three-dimensional crimped hollow type terylene | |
CN101792938B (en) | Novel preparation technology of polyoxymethylene fiber | |
CN104178844A (en) | Aromatic chinlon-spandex air wrapped yarn and production method thereof | |
CN106192067A (en) | Bicomponent composite fiber, composite yarn and fabric having high crimp property | |
CN104894686A (en) | Sheath-core type low-melting-point copolyamide composite fiber and preparation method thereof | |
CN101922053B (en) | Manufacturing process of fine denier nylon 6 fully-drawn fibers | |
CN104727015A (en) | Manufacturing method for melt-blown nonwoven fabric | |
CN105862152A (en) | Production method for high-speed spinning low-stretching high-modulus low-shrinkage polyester industrial filaments | |
CN106120003A (en) | A kind of spinneret, abnormity nylon-6 fiber and preparation method thereof | |
CN103388184B (en) | Spinning Process of Low Melting Point Polymer | |
CN105369382A (en) | Polyolefin blend modified elastic yarn slice and elastic yarn preparation method | |
CN107723838A (en) | A kind of hot melt adhesive composite fibre and preparation method thereof | |
CN101922055A (en) | A production process of 9-14 dtex nylon 6 full-dull full-drawn fiber | |
CN108166160A (en) | A kind of preparation process of agriculture and garden ecological, environmental protective polypropylene non-woven fabric | |
CN104532366A (en) | Method for producing regenerative ultrahigh-strength industrial filaments with recycled polyester as raw material | |
CN104593883A (en) | A method for preparing differentiated melt-spun spandex filaments with high resilience and low draft | |
CN102002763B (en) | 40-denier nylon 66 full dull full drawn fiber production process | |
CN103668511A (en) | Method for manufacturing bottle piece spinning return material recycled polyester moisture-absorbing sweat-releasing POY filament | |
CN108624986A (en) | Novel PLA/PET bi-component sheath-cores structural fibers and preparation method thereof | |
CN103233283B (en) | High-strength height stretches the manufacture method of polyester tire tire cord, tire cord and cord fabric thread | |
CN103696034A (en) | Production method of full-dull fine denier or ultrafine denier nylon 6 FDY filaments | |
CN102277630B (en) | A kind of preparation method of differentiated polyester fiber | |
CN104562275A (en) | Porous micro-fine denier nylon 6 POY filament yarns and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160224 Termination date: 20180805 |