CN1046558C - Processing tech. for active health fibre - Google Patents
Processing tech. for active health fibre Download PDFInfo
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- CN1046558C CN1046558C CN95112193A CN95112193A CN1046558C CN 1046558 C CN1046558 C CN 1046558C CN 95112193 A CN95112193 A CN 95112193A CN 95112193 A CN95112193 A CN 95112193A CN 1046558 C CN1046558 C CN 1046558C
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Abstract
The present invention relates to a technology for processing synthetic fibers, namely a technology for processing active health care fibers. The technology is completed by the processes of slicing, drying, spinning and post processing. The present invention is characterized in that in slicing, polypropylene mother particles, after far infrared powder, spinning-helping agents and stabilizing agents are evenly mixed proportionally, prepared particles are dried. The present invention has the advantages of simple and reasonable technology and wide source of raw materials. Products enable self temperature to be raised to send out far infrared through reflection because of the characteristic of far infrared absorption, and have the functions of disease prevention and treatment, enhancement of blood circulation and promotion of metabolism. The Products are suitable for tailoring various clothes for people in middle and old age and athletes, the goals of body building, disease prevention and health care are reaches, and thereby, the elimination of fatigue and the enhancement of activity are reached.
Description
The invention belongs to a kind of processing technology of producing synthetic fiber, its name is called the active health fibre processing technology.
At present, real silk health fiber and terylene health fiber occur in succession, do not set up in a wide range but all extensively be pushed, there is not suitable technology to make it in the certain scale of industrial formation, and its price is too high, complex process, cocoon fiber price in 1994 once reached 300,000 yuan/ton, and raw material sources are narrow.Yet polypropylene fiber is soft, along with the development of oil industry, raw material sources are more extensive, and price is more cheap, because the degree of crystallinity of polypropylene fiber is very high, lack the polar reaction group again, so improved polypropylene fiber does not form the large-scale production of industry so far.Increasing fiber expert, the processing technology of the health care polypropylene fiber of a kind of suitability for industrialized production of concentrating on studies in order to remedy the in great shortage deficiency of natural fabric raw material, comes back to life many textile enterprise on the verge of bankruptcy.
The purpose of the present invention's design, be to avoid above-mentioned the deficiencies in the prior art, and provide a kind of active health fibre processing technology, but large-scale industrial production, it is the improvement of producing the polypropylene fibre processing technology to existing, be by section, dry, spinning and back manufacturing procedure are finished, it is characterized in that slicing process is with polypropylene agglomerate, far-infrared powder, spinning-aid agent, after stabilizing agent mixes by a certain percentage, granulation enters drying process, the technology advantages of simple, on the technology basis of original production polypropylene fibre, suitably adjust fabrication process condition and can finish the present invention, its raw material sources are extensive, and product has the advantages that to absorb far infrared, and fiber self temperature is raise, far infrared is emitted in reflection again, have and prevent and cure diseases, strengthen blood circulation, promote the metabolism function, be fit to the sportsman, the elderly makes various clothes, improves the health, diseases prevention, health care, allaying tiredness is invigorated.
To achieve these goals, the present invention can adopt following measure to realize, described active health fibre processing technology, be to finish by section, drying, spinning and back manufacturing procedure, it is characterized in that slicing process is that polypropylene agglomerate 82～95%, the outer powder 5～10% of cylinder far away, spinning-aid agent 0.1～0.5, stabilizing agent 0.4～1% and dispersant 0.01～0.05 5 kind of a raw material are mixed, aforementioned proportion is weight percentage, carry out granulation again, produce active health polypropylene fiber master batch, enter drying process.
To achieve these goals, the present invention can also adopt following measure to realize, described active health fibre processing technology, it is characterized in that, far-infrared powder is the mixture of alundum (Al, titanium dioxide and silica gel, the fineness of the outer powder of cylinder far away is at 0.1～2 μ m, and spinning-aid agent is a methoxyl group silicon ether compound, and stabilizing agent is the light stabilizer of hindered amine type.
To achieve these goals, the present invention can also adopt following measure to implement, and the pre-crystallization temperature of described drying process is 60～90 ℃, 10～35 minutes time, baking temperature is 70～90 ℃, 3～6 hours time, dry back active health polypropylene fiber master batch Heshui amount＜100ppm.
To achieve these goals, the present invention can also adopt following measure to realize, described spinning, the technological parameter difference in each district of screw rod, temperature: minimum is 240 ℃, be up to 315 ℃, the screw rod melt pressure is: 6～9MPa, quench air velocity: 0.3～0.9m/s, ring blowing temp: 16～20 ℃, winding speed: 450～800m/min, drafting multiple: 3.5～4.5 times.
To achieve these goals, the present invention can also adopt following measure to realize, the temperature in loose HEAT SETTING three districts in the manufacturing procedure of described back is respectively: 1 district: 80～110 ℃, and 2 districts: 90～110 ℃, three districts: 80～110 ℃.
To achieve these goals, the present invention can also adopt following measure to realize, the used spinnerets diameter of described spinning process is: 160～180mm, and hole count is: 300～1000, draw ratio is: 1: 1.5～4.0, the aperture is: 0.3～0.5mm.
In order to be illustrated more clearly in the present invention, this bright doing is further illustrated below in conjunction with embodiment:
Embodiment 1:
The described active health fibre processing technology of present embodiment, will be through section, dry, spinning and back manufacturing procedure are finished, with polypropylene agglomerate 83%, far-infrared powder 6%, spinning-aid agent 0.2%, stabilizing agent 0.5%. dispersant 0.02%, produce the active health fibre master batch through slicing process, through super-dry, temperature is controlled at about 75 ℃ then, 4 hours time, dried active health polypropylene fiber master batch moisture＜100PPm, the temperature in each district of screw rod is at 240 ℃～315 ℃, and melt pressure is 6～9MPa, quench air velocity: 0.3～0.9m/s, ring blowing temperature: 16～20 ℃, winding speed; 500m/min, drafting multiple: 3.5～4.5 times, relaxation heat setting three district's temperature in the back manufacturing procedure are respectively: 1 district: 80～110 ℃, 2 districts: 90～110 ℃, 3 districts: 80～110 ℃, the used spinnerets diameter of spinning process is 162mm, hole count is 500, draw ratio is 1: 1.6, aperture, 0.35mm.
Enforcement of the present invention has following advantages;
Can carry out large-scale industrial production, the technical process advantages of simple, poly-in original production On the equipment of tacryl, adjust suitable technological parameter, can produce, the cost of material ratio More cheap, product has the advantages that to absorb far infrared, and makes self temperature rising, also can Radiate far infrared, have the function of preventing and curing diseases, also can make various cold-resistant clothes, And have the sleep state of improvement, eliminate the effects such as fatigue.
Claims (6)
1, a kind of processing technology of synthetic fiber, be to finish by section, drying, spinning and back manufacturing procedure, it is characterized in that slicing process is that polypropylene agglomerate 82～95%, far-infrared powder 5～10%, spinning-aid agent 0.1～0.5%, stabilizing agent 0.4～1% and dispersant 0.01～0.05 5 kind of a raw material are mixed, aforementioned proportion is weight percentage, carry out granulation again, produce active health polypropylene fiber master batch, enter drying process.
2, a kind of according to the described active health fibre processing technology of claim 1, it is characterized in that, far-infrared powder is alundum (Al, the titanium mixture from powder and silica gel, the fineness of the outer powder of cylinder far away is at 0.1～2 μ m, spinning-aid agent is a methoxyl group silicon ether compound, and stabilizing agent is the light stabilizer of hindered amine type.
3, a kind of according to the described active health fibre processing technology of claim 2, the pre-crystallization temperature that it is characterized in that described drying process is 60～90 ℃, 10～35 minutes time, baking temperature is 70～90 ℃, 3～6 hours time, dry back active health polypropylene fiber master batch moisture＜100ppm.
4, a kind of according to the described active health fibre processing technology of claim 3, when it is characterized in that spinning, the technological parameter difference in each district of screw rod, temperature: minimum is 240 ℃, is up to 315 ℃, and the screw rod melt pressure is: 6～9MPa, quench air velocity: 0.3～0.9m/s, the ring blowing temp: 16～20 ℃, winding speed: 450～800m/min leads the short multiple of stretching: 3.5～4.5 times.
5, a kind of according to the described active health fibre processing technology of claim 4, it is characterized in that the temperature in loose HEAT SETTING three districts in the manufacturing procedure is respectively: 1 district: 80～110 ℃, 2 districts, 90～110 ℃, three districts: 80～110 ℃.
6, a kind of according to the described active health fibre processing technology of claim 5, it is characterized in that the used spinnerets diameter of spinning process is: 160～180mm, hole count is: 300～1000, draw ratio is: 1: 1.5～4.0, the aperture is: 0.3～0.5mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN95112193A CN1046558C (en) | 1995-11-01 | 1995-11-01 | Processing tech. for active health fibre |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN95112193A CN1046558C (en) | 1995-11-01 | 1995-11-01 | Processing tech. for active health fibre |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1145420A CN1145420A (en) | 1997-03-19 |
| CN1046558C true CN1046558C (en) | 1999-11-17 |
Family
ID=5079390
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN95112193A Expired - Fee Related CN1046558C (en) | 1995-11-01 | 1995-11-01 | Processing tech. for active health fibre |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1046558C (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1306972C (en) * | 2003-11-14 | 2007-03-28 | 金纯玉 | Method for producing far infrared energy pad |
| CN101255329B (en) * | 2006-07-24 | 2013-04-17 | 刘燕平 | Master batch and fibre as well as manufacturing method thereof |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1052712A (en) * | 1989-12-20 | 1991-07-03 | 小室俊夫 | Infrared micro energy radiation is with powder and sneak into the synthetic fiber and the fiber product thereof of this powder |
-
1995
- 1995-11-01 CN CN95112193A patent/CN1046558C/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1052712A (en) * | 1989-12-20 | 1991-07-03 | 小室俊夫 | Infrared micro energy radiation is with powder and sneak into the synthetic fiber and the fiber product thereof of this powder |
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| Publication number | Publication date |
|---|---|
| CN1145420A (en) | 1997-03-19 |
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Free format text: CORRECT: PATENTEE; FROM: HUSHAN ORGANIC CHEMICAL CO., LTD. LINZI, ZIBO CITY TO: SHANDONG CENTURY KANGSHI CO., LTD. |
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Patentee after: Shandong century Kang Shi Co., Ltd. Patentee before: Hushan Organic Chemical Co., Ltd. Linzi, Zibo City |
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