KR920006377B1 - Manufacturing process of nylon-46 fiber - Google Patents
Manufacturing process of nylon-46 fiber Download PDFInfo
- Publication number
- KR920006377B1 KR920006377B1 KR1019890018282A KR890018282A KR920006377B1 KR 920006377 B1 KR920006377 B1 KR 920006377B1 KR 1019890018282 A KR1019890018282 A KR 1019890018282A KR 890018282 A KR890018282 A KR 890018282A KR 920006377 B1 KR920006377 B1 KR 920006377B1
- Authority
- KR
- South Korea
- Prior art keywords
- nylon
- compound
- fiber
- amount
- bisoxazionone
- Prior art date
Links
Classifications
-
- 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
- D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
- D01F6/60—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyamides
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Artificial Filaments (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Polyamides (AREA)
Abstract
Description
본 발명은 폴리테트라메틸렌아디프아미드(이하 나이론-46이라고 함)에 열안정성을 부여하기 위하여 나이론-46 수지에 나이론-46의 말단기인 카르복실기와 반응하는 비스옥사졸린계 화합물과, 말단아미노기와 반응할 수 있는 비스옥사지온계 화합물을 첨가한 다음에 망간포스페이트와 알칼리금속 할로겐화합물 존재하에서 용융방사시킴을 특징으로 하는 나이론-46 섬유의 제조방법에 관한 것이다.The present invention reacts with a bisoxazolin-based compound that reacts with a carboxyl group, which is a terminal group of nylon-46, to a nylon-46 resin to give thermostability to polytetramethyleneadipamide (hereinafter referred to as nylon-46), and a terminal amino group. The present invention relates to a method for producing a nylon-46 fiber, which is characterized by melt spinning in the presence of a manganese phosphate and an alkali metal halide after the addition of a bisoxazione-based compound.
나이론-46 수지의 제조방법은 미국특허 4,408,036와 4,446,304, 일본특개소 58-83029,56-149431등에 상세하게 기재되어 있다.Methods for preparing nylon-46 resins are described in detail in US Pat. Nos. 4,408,036 and 4,446,304, Japanese Patent Laid-Open No. 58-83029,56-149431, and the like.
나이론-46은 높은 융점과 높은 유리전이 온도를 가지고 있으므로 나이론 6이나 66에 비하여 내열성, 특히고온에서의 치수안정성이 우수하며, 또 나이론 6나 66에 비하여 분자사슬의 패킹이 용이하고 단위 탄소개수당 수소 결합이 많기 때문에 결정화속도가 빠르고 결정화도가 매우 높다.Nylon-46 has high melting point and high glass transition temperature, so it has better heat resistance, especially dimensional stability at high temperature than nylon 6 or 66, and it is easier to pack molecular chains than nylon 6 or 66 and per unit carbon number. Since there are many hydrogen bonds, the crystallization rate is fast and the crystallinity is very high.
아울러 나이론-46은 내약품성 및 기타 기계적 성질이 우수하다.Nylon-46 also has excellent chemical resistance and other mechanical properties.
반면에 나이론-46은 열변형온도와 융점등은 높지만 융점과 열분해온도가 비슷하므로 타이어코드등 산업자재용 섬유를 제조할때 열분해가 심하게 발생하며, 그 결과 생산성이 떨어지고 미연신사의 물성이 크게 저하되어 타이어코드에 적합한 물성을 갖는 섬유를 제조하기 어려웠다.On the other hand, nylon-46 has high heat deflection temperature and melting point, but similar melting point and pyrolysis temperature, so that pyrolysis occurs severely when manufacturing industrial materials such as tire cords. It was difficult to produce fibers having physical properties suitable for tire cords.
또한 나이론-46은 우수한 열적, 기계적 성질에도 불구하고 용융가공성이 나쁘기 때문에 아직 산업화가되지 못하고 있다.In addition, nylon-46 has not yet been industrialized due to its poor melt processability despite its excellent thermal and mechanical properties.
그러므로 용융상태에서의 열안정성을 향상시키는 것이 나이론-46의 해결과제이지만 아직 구체적인 방법이 제시되지 않고 있다. 다만 일본특개소 62-185745에 의하면 산화방지제로서의 힌더드 페놀계를 사용하는방법이 알려져 있다. 그러나, 산화방지제만으로는 용융가공시 상대점도의 감소나 기타 다른 물성의 저하를 충분히 막을 수가 없다.Therefore, improving thermal stability in the molten state is a challenge for nylon-46, but no specific method has yet been proposed. However, according to Japanese Patent Laid-Open No. 62-185745, a method of using a hindered phenol type as an antioxidant is known. However, antioxidants alone do not sufficiently prevent the reduction of relative viscosity or other deterioration of physical properties during melt processing.
특히, 가공시간이 사출성형의 경우에 비하여 긴 방사의 경우에 있어서는 더욱 더 열분해를 방지하기가 힘들다. 일반적으로 폴리아미드의 열분해에 의한 물성저하와 변퇴색을 방지할 목적으로 폐놀계화합물, 인계화합물, 방향족아민류, 할로겐화 구리 따위의 여러가지 열안정제를 첨가하는 것이 알려져 있다.In particular, it is more difficult to prevent pyrolysis in the case of long spinning than in the case of injection molding. In general, it is known to add various thermal stabilizers such as phenolic compounds, phosphorus compounds, aromatic amines, and copper halides in order to prevent physical degradation and discoloration due to thermal decomposition of polyamides.
그러나, 나이론-46은 나이론 6나 66에 비하여 열분해 속도가 아주 빠르기 때문에 이러한 열안정제만으로는 열분해를 방지할 수가 없다.However, since nylon-46 has a much higher thermal decomposition rate than nylon 6 or 66, these thermal stabilizers alone cannot prevent thermal decomposition.
일본특개소 50-59525,56-91009에 의하면 고분자량의 폴리머를 단시간이 얻는 방법으로서 쇄연장제를사용하는 방법이 소개되어 있으며, 특히 폴리에스테르의 쇄연장제로서 비스옥사졸린 화합물을 첨가하여 말단 카르복실기와 반응시키면 내열성이 우수한 고분자량의 폴리에스테르가 얻어진다고 보고 되어 있다. 본발명자들은 이러한 쇄연장제의 효과에 착안하여 연구실험한 결과 본 발명을 완성하게 되었다.According to Japanese Patent Application Laid-Open No. 50-59525,56-91009, a method of using a chain extender as a method of obtaining a high molecular weight polymer in a short time has been introduced. In particular, a terminal carboxyl group is added by adding a bisoxazoline compound as a chain extender of polyester. It is reported that a high molecular weight polyester having excellent heat resistance is obtained when reacted with. The present inventors completed the present invention as a result of research experiments focusing on the effect of the chain extender.
본 발명을 상세히 설명하면, 본 발명은 선상 가융성 나이론-46과 비스옥사졸린 및 비스옥사지온계의 혼합화합물을 망간포스페이트와 알칼리금속 할로겐화합물의 존재하에서 용융상태로 방사하는 것을 특징으로 하는 열안정성이 우수한 나이론-46 섬유의 제조방법에 관한 것이다.DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT OF THE INVENTION The present invention is thermally stable, characterized in that the mixture of linear fusible nylon-46, bisoxazoline, and bisoxazione-based compounds are spun in a molten state in the presence of manganese phosphate and an alkali metal halide compound. A method for producing this excellent nylon-46 fiber.
본 발명에서 사용하고 있는 비스옥사졸린 화합물은 아래의 (I)식과 같은 구조식을 가지며, 구제적인 예로는 1, 3-페닐렌-비스-2-옥사졸린, 1, 4-페닐렌-비스-2-옥사졸린등이 있다.The bisoxazoline compound used in the present invention has a structural formula such as the following formula (I), and specific examples thereof include 1, 3-phenylene-bis-2-oxazoline, 1, 4-phenylene-bis-2 -Oxazoline.
그리고, 비스옥사지온 하합물은 아래의 (Ⅱ)식과 같은 구조식을 갖는다.And the bisoxazionate mixture has a structural formula as shown in the following formula (II).
단, X는 2가의 유기기로서 예를들면, 자일렌기, 치환메틸렌기, 에틸렌기, 오르토페닐렌기, 치환기를 가지는 오르트페닐렌기등이 있다.However, X is a divalent organic group, for example, a xylene group, a substituted methylene group, an ethylene group, an orthophenylene group, an ortphenylene group which has a substituent, etc. are mentioned.
특히 본 발명에서 일반식(II)의 화합물로는 X가 오르트페닐렌기로 치환된 2,2'-비스(4H-3,1-벤족사진-4-온)을 사용하는 것이 더욱 좋다.In particular, in the present invention, it is more preferable to use 2,2'-bis (4H-3,1-benzoxazin-4-one) in which X is substituted with an ortphenylene group as the compound of formula (II).
본 발명에서 비스옥사졸린의 사용량(A)과 비스옥사지온의 사용량(B)은 아래식(Ⅲ),(IV)의 범위를 만족하도록 사용하는 것이 좋다.In the present invention, the amount of bisoxazolin used (A) and the amount of bisoxazionone used (B) are preferably used to satisfy the following formulas (III) and (IV).
아 래Below
단, M1사용한 비스옥사졸린의 분자량However, the molecular weight of bisoxazolin using M 1
CV1: 나이론-46의 카르복실 말단함량(eq/106g)CV 1 : carboxyl terminal content of nylon-46 (eq / 10 6 g)
단, M2: 비스옥사지온의 분자량M 2 : Molecular weight of bisoxazionone
CV2: 나이론-46의 아미노말단함량(eq/106g)CV 2 : amino-terminal content of nylon-46 (eq / 10 6 g)
실제로 본 발명에 사용되어진 나이론-46 수지의 분자량은 상대점도가 3.63, 아미노말단기는 35eq/106g, 카르복실기는 19eq/106g이었다.In fact, the molecular weight of the nylon resin -46 been used in the present invention is the relative viscosity of 3.63, an amino end group is 35eq / 10 6 g, a carboxyl group was 19eq / 10 6 g.
그리고, 본 발명에 사용되어진 비스옥사졸린 화합물은 1,3-페닐렌-비스-2-옥사졸린이고, 비스옥사지온 화합물은 2,2'-비스(4H-3,1-벤존사진-4-온)이며, 그 분자량은 각각 216g/mol,292g/mol이다.In addition, the bisoxazolin compound used in the present invention is 1,3-phenylene-bis-2-oxazoline, and the bisoxazionone compound is 2,2'-bis (4H-3,1-benzonazine-4- On), and its molecular weight is 216 g / mol and 292 g / mol, respectively.
그러므로 실제 사용량의 범위는 비스옥사졸린의 경우 0.15∼1.03중량%, 비스옥사지온의 경우 0.38∼2.55중량%이다.Therefore, the actual usage ranges from 0.15 to 1.03% by weight for bisoxazoline and 0.38 to 2.55% by weight for bisoxazionone.
비스옥사졸린과 비스옥사지온 공히 최저사용량보다 적게 사용할 경우는 열분해에 의한 물성저하를 충분히 막을 수 없고, 최대사용량을 초과할 경우에는 더 사용한다해도 그 효과가 상승하기 않고 오히려 나이론-46의 특성만 감소시키고 조업성이 악화되므로 좋지 않다.If bisoxazoline and bisoxazone are used less than the minimum dose, the degradation of properties due to pyrolysis cannot be prevented sufficiently. If the maximum dose is exceeded, the effect does not increase even if it is used more. It is not good because it decreases and operability worsens.
본 발명에서 망간포스페이트와 알칼리금속 할로겐화합물(KI,KBr등)은 용융가공시에 발생하는 산소에 의하여 열분해나 황변과 같은 변퇴색을 방지할 목적으로 사용하는데, 망간포스페이트의 사용량은 망간이온(Mn++)에 대하여 100∼1000ppm, 더욱 좋기로는 250∼700ppm이고, 할로겐화합물의 사용량은 망간이온(Mn++) 함량의 1∼3배 사용하는 것이 바람직하다.In the present invention, manganese phosphate and alkali metal halides (KI, KBr, etc.) are used for the purpose of preventing discoloration such as pyrolysis or yellowing by oxygen generated during melt processing, the amount of manganese phosphate is used as manganese ion (Mn ++ ) is 100 to 1000ppm, more preferably 250 to 700ppm, and the amount of the halogen compound is preferably used 1 to 3 times the content of manganese ions (Mn ++ ).
망간포스페이트 화합물중의 망간 이온함량이 100ppm 미만, 할로겐화합물의 함량이 망간이온함량의 1배미만일 경우에는 열분해에 의한 황변현상을 막을 수 없으며, 또 그 함량이 1000ppm을 초과하거나 3배를 초과하는 경우에는 더 이상의 열분해 방지효과를 기대할 수 없으며, 오히려 나이론-46 섬유의 기계적성질이 저하되고 방사성이 악화되므로 좋지 않다.When the content of manganese ions in the manganese phosphate compound is less than 100 ppm and the content of the halogen compound is less than one time of the content of manganese ions, yellowing due to thermal decomposition cannot be prevented, and the content is more than 1000 ppm or more than three times. It is not good to expect any further thermal decomposition prevention effect, but rather, the mechanical properties of the nylon-46 fiber is degraded and the radioactivity is deteriorated.
본 발명에서 망간 또는 할로겐화합물만을 각각 투입할 경우에는 아무것도 넣지 않을때에 비하여 그 물성저하는 적지만 그 효과는 아주 미미하여 본 발명의 목적을 달성할 수가 없고, 또 비스옥사졸린 또는 비스옥사지온 화합물만을 각각 사용했을 경우는 방사후 미연신사의 황변을 막을 수가 없다. 따라서, 상기 화합물을 동시에 사용하여야만 열분해에 의한 황변현상, 포리마의 특성저하를 충분히 방지할 수 있으며 고온에서도 열적, 기계적물성이 우수한 나이론-46를 제조할 수 있다.In the present invention, when only manganese or a halogen compound is added to each other, the physical properties are less than that of adding nothing, but the effect is so insignificant that the object of the present invention cannot be achieved, and only the bisoxazoline or bisoxazionone compound is used. In each case, yellowing of undrawn yarn cannot be prevented after spinning. Therefore, only when the compound is used at the same time to prevent the yellowing phenomenon due to thermal decomposition, deterioration of the characteristics of the forma and can be produced nylon-46 excellent in thermal and mechanical properties even at high temperatures.
다음은 실시예에 의하여 본 발명을 더욱 상세하게 설명한다.The following describes the present invention in more detail by examples.
실시예 및 비교예에 의하여 제조된 미연신사의 물성은 아래와 같은 실험방법으로 측정하였다.Physical properties of the non-drawn yarn prepared according to Examples and Comparative Examples were measured by the following experimental method.
1.상대점도1. Relative viscosity
시료를 96% 황산에 용해하여 농도 1%의 황산용액을 조제한 다음 25℃에서 우벨로드형 점도계로 측정하였다.The sample was dissolved in 96% sulfuric acid to prepare a sulfuric acid solution having a concentration of 1%, and then measured at 25 ° C. using a Ubelrod viscometer.
2.-COOH 말단함량2.-COOH terminal content
시료를 약 40℃에서 오르토 크레졸에 용해시킨 다음 온도를 서서히 150℃까지 올린 후에 상기 용액에 벤질알코올을 부가하여 즉시 테트라부틸 암모늄 히드록시드 용액으로 적정하였다.The sample was dissolved in ortho cresol at about 40 ° C. and then slowly raised to 150 ° C., then benzyl alcohol was added to the solution and immediately titrated with tetrabutyl ammonium hydroxide solution.
3.-NH2말단함량3.-NH 2 terminal content
시료를 페놀에 녹인 후 염산으로 적정하였다.The sample was dissolved in phenol and titrated with hydrochloric acid.
4.용융점도4.melt viscosity
캐필러리 레오메타를 사용하여 305℃에서 20mm/min로 측정하였다.It measured at 20 mm / min at 305 degreeC using the capillary rheometer.
[실시예 1∼3][Examples 1-3]
상대점도 3.63, 카르복실 말단함량 19eq/106g, 아미노말단함량 35eq/106g인 나이론 46에 표 1에 표시된 함량만큼의 망간과 KI를 첨가하여 105℃, 9시간동안 건조한 후 정해진 양의 비스옥사졸린과 비스옥사지온 화합물을 블렌딩하여 방사온도 305℃, 토출량 120g/min으로 방사하여 나이론 46 미연신사를 얻었다.Nylon 46, which has a relative viscosity of 3.63, a carboxyl terminal content of 19eq / 10 6 g, and an amino terminal content of 35eq / 10 6 g, was added with the amount of manganese and KI as indicated in Table 1, and dried at 105 ° C. for 9 hours. The bisoxazoline and bisoxazionone compound were blended and spun at a spinning temperature of 305 占 폚 and a discharge amount of 120 g / min to obtain a nylon 46 unstretched yarn.
이 미연신사에 대하여 상대점도, 카르복실 말단함량, 용융점도를 비교하였다.Relative viscosity, carboxyl end content, and melt viscosity were compared for this undrawn yarn.
[표 1]TABLE 1
표 1에서 MBO : m-페닐렌-비스-2-옥사졸린MBO in Table 1: m-phenylene-bis-2-oxazoline
BZO : 2, 2'-비스(4H-3,1-벤족사진-4-온)BZO: 2, 2'-bis (4H-3,1-benzoxazin-4-one)
[실시예 4~7]EXAMPLES 4-7
MBO와 BZO를 각각 0.75중량%, 2.50중량%를 사용하고 표 2에 나타난 함량만큼 사용하는 것 이외에는 상기 실시예 1과 동일한 방법으로 실시하였다.MBO and BZO were used in the same manner as in Example 1, except that 0.75% by weight and 2.50% by weight, respectively, were used in the amounts shown in Table 2.
[표 2]TABLE 2
[비교실시예 1~7][Comparative Examples 1-7]
상기 실시예와 동일한 화합물을 사용하고 그 첨가량을 표 3과 같이 하는 것 이외에는 상기 실시예와 동일한 방법으로 행하였다.The same compound as in Example was used, and the addition amount thereof was performed in the same manner as in Example, except that Table 3 was added.
[표 3]TABLE 3
실시예 1~7은 용융점도가 1300~1600 포아즈 이어서 방사성이 양호하지만, 비교예 1~7은 용융점도가 1300 이하이므로 방사성이 매우 불량함을 알 수 있다.Examples 1 to 7 have a melt viscosity of 1300 to 1600 poise followed by good radioactivity, but Comparative Examples 1 to 7 show a very poor radioactivity because the melt viscosity is 1300 or less.
또 비교예 1∼7은 말단 -COOH와 -NH2의 양이 증가하였기 때문에 내열성이 불량하지만 실시예 1∼7은 그 양이 적기 때문에 내열성이 우수함을 알 수 있다.In Comparative Examples 1 to 7, the heat resistance was poor because the amounts of the terminal -COOH and -NH 2 were increased, but Examples 1 to 7 were excellent in the heat resistance because the amount was small.
또 비교예 1∼7은 색상이 변색되었지만 실시예 1∼7은 백색이 그대로 유지되었다.In Comparative Examples 1 to 7, the color changed, but in Examples 1 to 7, the white color remained as it is.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019890018282A KR920006377B1 (en) | 1989-12-11 | 1989-12-11 | Manufacturing process of nylon-46 fiber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019890018282A KR920006377B1 (en) | 1989-12-11 | 1989-12-11 | Manufacturing process of nylon-46 fiber |
Publications (2)
Publication Number | Publication Date |
---|---|
KR910012379A KR910012379A (en) | 1991-08-07 |
KR920006377B1 true KR920006377B1 (en) | 1992-08-03 |
Family
ID=19292736
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019890018282A KR920006377B1 (en) | 1989-12-11 | 1989-12-11 | Manufacturing process of nylon-46 fiber |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR920006377B1 (en) |
-
1989
- 1989-12-11 KR KR1019890018282A patent/KR920006377B1/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
KR910012379A (en) | 1991-08-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0827976B1 (en) | Polyamide compositions having improved thermal stability | |
JP4716576B2 (en) | Low release polymer composition | |
CA2136177C (en) | Manufacture of terephthalic acid copolyamides | |
US20100181696A1 (en) | Halogen-free flame retardants | |
US3632666A (en) | Polyether-polyamide block copolymers containing polyamide polyester or polyamide-polyester or polyamidepolyester block copolymeric synthetic resins and ionic compounds | |
EP0979320B1 (en) | Solution-dyed nylon fibers | |
US5708065A (en) | Fire resistant resin compositions | |
US4105621A (en) | Thermoplastic polyamide composition | |
US6350802B2 (en) | Thermally stable flame retardant polyamides | |
JP3699128B2 (en) | Polyester composition | |
EP0934979A2 (en) | Partly aromatic polyamide resins compositions | |
EP0139893A1 (en) | Flame retardant polyamide compositions | |
JPH03239755A (en) | Flame-retardant nylon resin composition | |
US3980615A (en) | Flame retarding plastic materials | |
KR920006377B1 (en) | Manufacturing process of nylon-46 fiber | |
US3980614A (en) | Flame retarding plastic materials | |
JPS58134148A (en) | Flame-retardant polyester resin composition | |
US5015681A (en) | Flameproof thermoplastic molding materials based on polyamides and polyester elastomers | |
KR930004291B1 (en) | Nylon 46 composition | |
US5567797A (en) | Polyamide composition and process for its production | |
CA1329441C (en) | Molecular weight controller for polymerization of lactams to polyamides | |
US5006635A (en) | Molecular weight controller composition for aqueous polymerization of lactam to polyamide | |
US5585429A (en) | Polyphthalamide resin formulations | |
US3507833A (en) | Stabilized polyamide composition containing copper and halogenated phosphite additives | |
US3890286A (en) | Production of polycaproamide fiber |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
E902 | Notification of reason for refusal | ||
G160 | Decision to publish patent application | ||
E701 | Decision to grant or registration of patent right | ||
GRNT | Written decision to grant | ||
FPAY | Annual fee payment |
Payment date: 19970616 Year of fee payment: 6 |
|
LAPS | Lapse due to unpaid annual fee |