KR830000407B1 - Process for preparing filled and curable polymer materials - Google Patents
Process for preparing filled and curable polymer materials Download PDFInfo
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- KR830000407B1 KR830000407B1 KR1019790001232A KR790001232A KR830000407B1 KR 830000407 B1 KR830000407 B1 KR 830000407B1 KR 1019790001232 A KR1019790001232 A KR 1019790001232A KR 790001232 A KR790001232 A KR 790001232A KR 830000407 B1 KR830000407 B1 KR 830000407B1
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- polymer
- filler
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- curable polymer
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- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 239000002861 polymer material Substances 0.000 title claims description 3
- 238000000034 method Methods 0.000 claims description 18
- 239000000945 filler Substances 0.000 claims description 15
- 239000008187 granular material Substances 0.000 claims description 12
- 229920000642 polymer Polymers 0.000 claims description 12
- 239000000463 material Substances 0.000 claims description 11
- -1 silane compound Chemical class 0.000 claims description 11
- 229910000077 silane Inorganic materials 0.000 claims description 8
- 239000003054 catalyst Substances 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 239000003963 antioxidant agent Substances 0.000 claims description 3
- 230000003078 antioxidant effect Effects 0.000 claims description 3
- 229920001577 copolymer Polymers 0.000 claims description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 2
- 239000005977 Ethylene Substances 0.000 claims description 2
- 238000001125 extrusion Methods 0.000 claims description 2
- 229920001519 homopolymer Polymers 0.000 claims description 2
- 238000002360 preparation method Methods 0.000 claims description 2
- 238000001723 curing Methods 0.000 description 10
- 239000004698 Polyethylene Substances 0.000 description 8
- 235000012204 lemonade/lime carbonate Nutrition 0.000 description 8
- 229920000573 polyethylene Polymers 0.000 description 7
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 4
- KPUWHANPEXNPJT-UHFFFAOYSA-N disiloxane Chemical class [SiH3]O[SiH3] KPUWHANPEXNPJT-UHFFFAOYSA-N 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 239000012212 insulator Substances 0.000 description 3
- 125000003545 alkoxy group Chemical group 0.000 description 2
- 229920005601 base polymer Polymers 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 239000011256 inorganic filler Substances 0.000 description 2
- 229910003475 inorganic filler Inorganic materials 0.000 description 2
- 229920002521 macromolecule Polymers 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 150000002978 peroxides Chemical class 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 229910021532 Calcite Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical group [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 150000001282 organosilanes Chemical class 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000003617 peroxidasic effect Effects 0.000 description 1
- 238000010517 secondary reaction Methods 0.000 description 1
- 150000004756 silanes Chemical class 0.000 description 1
- 125000005372 silanol group Chemical group 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/24—Crosslinking, e.g. vulcanising, of macromolecules
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
내용 없음.No content.
Description
본 발명은 중합체의 기본 분자상에 그라프트 결합된 실란화합물로 인해 수분작용에 의해 경화될 수 있는 충전재 함유중합체의 제조방법에 관한 것이다.The present invention relates to a method for preparing a filler-containing polymer that can be cured by water action due to the silane compound graft-bonded onto the base molecule of the polymer.
열안정성 및 내구성등이 높은 합성수지제품을 제조하기 위해서 오래전부터 유기과산화물에 의해 중합체 재료를 경화(網組織化)시키는 것이 알려져 있으며, 이 경화공정은 열공급화, 고압하에서 행한다.In order to manufacture a synthetic resin product having high thermal stability and durability, it has been known for a long time to harden a polymer material with an organic peroxide. This curing process is performed under heat supply and high pressure.
그러나 그 사이에 실옥산(siloxane)기법을 알게 되어 실현을 보게된 다른 경화법이 또한 등장했다.In the meantime, however, other hardening methods have also emerged, in which the siloxane technique became known and realized.
통상적인 과산화적 경화와는 반대로, 여기서는 기본중합체의 거대분자상에 저분자량 화합물이 그라프트결합(graft)되고 그 다음 이차반응의 경과로 거대분자 경화시키게 된다.Contrary to conventional peroxidative curing, here low molecular weight compounds are grafted onto the macromolecules of the base polymer and then the macromolecules are cured as a secondary reaction proceeds.
예컨대 폴리에틸렌분자상에 그라프트 결합되기에 특히 적당한 것으로는 어떤 다관능(多官能)오르가노실란이 있는데, 이것은 불포화비닐기와 쉽게 가수분해될 수 있는 알콕시기를 임의로 처리한다. 그라프트 결합된 상태에서는 폴리에틸렌은 아직 열가소적이다.Particularly suitable for graft bonding on polyethylene molecules, for example, are some polyfunctional organosilanes, which optionally process unsaturated vinyl groups and alkoxy groups that can be readily hydrolyzed. In the graft bonded state, the polyethylene is still thermoplastic.
이제, 우선 최소량의 수분을 공급하면 실란올기내의 규소원자를 알콕시기가 포Now, when the minimum amount of water is supplied, the silicon atom in the silanol group contains an alkoxy group.
이 경화방법은 경화가능제품의 특히 합리적인 제공을 허용하며, 종래의 과산화물 경화법에 비하여 열안정성이 더욱 개선되며, 또한 경화된 재료의 내노화(老化)안정성이 시판 VPE화합물보다 더 우수하다.This curing method allows particularly reasonable provision of curable products, further improves thermal stability as compared to conventional peroxide curing methods, and is superior to commercially available VPE compounds in aging stability of cured materials.
그러나, 예컨대 중합체원료를 절약하기 위해서 또는 특정 성질의 제품을 위해서 그러한 경화가능원료에 염가의 무기충전제를 혼합해야 하는 경우에는, 보통의 과산화물 경화제가 혼합된 재료의 경우에서 처럼 곤란한 문제가 발생한다.However, when it is necessary to mix inexpensive inorganic fillers with such a curable raw material, for example to save a polymer raw material or for a product of a certain property, a problem arises as in the case of a material in which a normal peroxide curing agent is mixed.
왜냐하면 충전재에 흡착결합된 수분으로 인해 지상결합과정중에 이미 사전경화가 일어나 버리기 쉽기 때문이다.This is because the moisture adsorbed on the filler is likely to cause precure during the ground bonding process.
그 결과는 불량, 불균일한 용융물질과 보기흉한 압출표면이다. 본 발명의 목적은 수분을 근거로 작용하는 경화메카니즘에 의존하는 재료에 있어서는 무기충전재 첨가시 사전경화의 위험없이 중합제품을 얻을 수 있는 가능성을 발견하는 것이다.The result is poor, uneven melt and unsightly extruded surfaces. It is an object of the present invention to find the possibility of obtaining a polymerized product without the risk of pre-curing when the inorganic filler is added in a material that depends on the curing mechanism acting on the basis of moisture.
에틸렌의 호모중합체 또는 공중합체같은 중합체를 우선 건조상태에서 충전재와 혼합, 교반 및 조립(造粒)하고, 그렇게 준비된 또는 이미 이런 준비상태에 놓인 재료내에 실온 또는 그보다 약간 높은 온도에서 실란화합물을 확산시키고 이 경화제함유 과립을 산화방지제 및 경화촉매함유 중합체뱃치와 혼합시키며, 최종적으로 이 과립을 압출공정을 받게하여 동일공정에서 성형하는, 본 발명에 의하여 상기목적은 달성된다. 이와 같은 방법은 양호한 표면형상의 제품의 생산을 보장하며, 사전경화가 방지된다.A polymer, such as a homopolymer or copolymer of ethylene, is first mixed, stirred and granulated with the filler in the dry state, and the silane compound is diffused at room temperature or slightly higher in the material so prepared or already in such preparation. The above object is achieved by the present invention, wherein the curing agent-containing granules are mixed with an antioxidant and a curing catalyst-containing polymer batch, and finally the granules are subjected to an extrusion process and molded in the same process. This method ensures the production of good surface-shaped products and prevents precure.
무충전(無充塡)중합체재료에 비하여 훨씬 높은 함량의 충전재로 인해 또한 그로Due to the much higher content of fillers compared to non-filled polymeric materials,
본 발명의 목적에 특히 적합한 충전재로서는 습기없는 방해석 충전재가 있다. 여기에는 예컨대 Durcal 2 및 Millicarb라는 상품명하에 알려져 있는 백색도가 높은 천연산이 포함된다.Particularly suitable fillers for the purposes of the present invention are moisture-free calcite fillers. This includes, for example, high whiteness natural acids known under the trade names Durcal 2 and Millicarb.
예컨대 전기케이블이나 도선의 절연체를 제조할 경우에는 바람직하기는 65부까지의 양, 특히 45-55부의 양의 충전재를 단독상태로 기본중합체에 첨가할 수 있다.For example, in the production of insulators for electric cables or conductors, fillers, preferably up to 65 parts, in particular 45-55 parts, may be added to the base polymer in a single state.
그러나 본 발명의 수행에 있어서는 그런 충전재를 고충전재농도의 중합체뱃치의 상태로 첨가할 수도 있다.However, in the practice of the present invention such fillers may be added in the state of polymer batches of high filler concentration.
이 경우에는 예컨대 90부의 충전재 예컨대 탄산석회와, (폴리에틸렌이 동시에 기본물질인 때는) 30부의 폴리에틸렌으로 되어 있는 뱃치가 적당하다.In this case, for example, a batch consisting of 90 parts of filler such as lime carbonate and 30 parts of polyethylene (when polyethylene is a base material at the same time) is suitable.
이 경우에는 0.2내지 4.0사이의 멜트인덱스 특히 약 2.0의 인덱스를 가진 기본재료를 선택하는 것이 특히 유리하다. 그렇게 하면 압출상태와 충전물의 분산성이 특히 좋다.In this case it is particularly advantageous to select a base material with a melt index between 0.2 and 4.0, in particular about 2.0. The extruded state and the dispersibility of the packing are then particularly good.
상기 방법에서 벗어나 실란화합물을 이미 함유하고 있는 폴리에틸렌과립 또는 공중합체과립을, 충전재 예컨대 탄산석회함유뱃치와 혼합하면 가끔 유리할 수 있다.It may sometimes be advantageous to deviate from the process and mix polyethylene granules or copolymer granules already containing silane compounds with fillers such as batches containing lime carbonate.
실란확산 침투공정이 끝난 뒤에는 예컨대 빠르게 또는 느리게 작동하는 교반기속에서 탄산석회의 첨가 조작이 행해지는 것이나, 이 첨가조작은 예컨대 통상적 혼합장치에 의해 압출기에서 직접 수행될 수도 있다.After completion of the silane diffusion infiltration process, for example, an addition operation of lime carbonate is performed in a stirrer which operates rapidly or slowly, but this addition operation may be performed directly in the extruder, for example, by a conventional mixing device.
본 발명의 방법에 따라 합성수지로 되어 있고 경화가능한 여러가지 제품을 만들 수 있다. 상업관례적 기계에 대한 큰 투자없이도 실천될 수 있는 생산기술적 간단한 방법으로서 인해 장척(長尺)제품을 연속제조 해야하는 경우에 본 발명을 적절히 이용할 수 있다. 예컨대 그것은 합성수지형재(形材) 또는 관재(管材)일 수 있고, 또는 높은 내열성 외피(外皮)로 심(芯)을 보호해야할 경우 그런심에 대한 단순한 외피일 수도 있다.According to the method of the present invention, various products made of synthetic resin and curable can be made. The present invention can be suitably used when continuous production of long products is required due to a simple production technique that can be practiced without a large investment in commercial customary machinery. For example, it may be a synthetic resinous shape or a tubular material, or it may be a simple skin for the seam if it is necessary to protect the seam with a high heat-resistant skin.
그러나 본 발명 방법의 특히 유리한 이용은 전기케이블의 제조 특히 저전압용 전기케이블의 제조에 있다.However, a particularly advantageous use of the method of the invention lies in the manufacture of electrical cables, in particular the manufacture of electrical cables for low voltages.
수분경화재료는 전선의 절연재 역할을 한다. 이 절연재는 두께가 2~3mm에 지나지 않으므로 경화를 위한 수분보급은 가끔 완전생략될 수 있어 케이블 제조속도는 현격하게 증가된다.Moisture hardening material acts as an insulator for wires. Since the insulation is only 2-3mm thick, the moisture supply for hardening can sometimes be completely omitted, resulting in a dramatic increase in cable manufacturing speed.
본 발명에 따라 사용되는 충전재는, 수분함량이 낮아야 하는 것 이외에도 입자형태와 입경분포도 중요한 역할을 한다. 특히 적합한 것은 다음과 같다.The filler used according to the invention, in addition to having a low water content, also plays a role in particle shape and particle size distribution. Particularly suitable are as follows.
Durcal 2 MillicarbDurcal 2 Millicarb
입자형태 결정/사방육면체 결정/사방육면체Particle Form Crystals / Rhombuses Crystals / Rhombuses
CaCO399.0% 99.75%CaCO 3 99.0% 99.75%
Fe2O30.04% 0.02%Fe 2 O 3 0.04% 0.02%
BET-표면적 4㎡/g 2.5㎡/gBET-Surface Area 4㎡ / g 2.5㎡ / g
수 분 <0.2% <0.2%Moisture <0.2% <0.2%
평균입자경-φ 3㎛ 3㎛Average particle diameter-φ 3㎛ 3㎛
2μ보다 미세한 것 40% 35%Finer than 2μ 40% 35%
표에서 보이는 것과 같이 이 두재료는 입경이 극히 미세하고 흡습성이 낮다.As shown in the table, these two materials have extremely fine particle diameters and low hygroscopicity.
예컨대 45-55부 탄산석회를 함유해야할 저전압케이블선의 절연체용 실옥산경화가능 배합제를 만들기 위해서는, 먼저 예컨대 멜트인덱스 2.0의 폴리에틸렌과립을 45-55부의 탄산석회와 적당한 혼합기속에서 건조상태에서 예비 혼합시킨다. 다음 이 예비혼합물을 혼합압출기 에컨대 소위 혼련기속에서 교반시키고 물 없이 즉 건조상태에서 조립한다.For example, to make a siloxane hardenable compound for insulators of low-voltage cable lines that must contain 45-55 parts of lime carbonate, the polyethylene granules of melt index 2.0, for example, are premixed in a dry state in a suitable mixer with 45-55 parts of lime carbonate. Let's do it. This premix is then stirred in a mixed extruder such as a so-called kneader and assembled without water, ie dry.
그렇게 처리된 탄산석회 충전과립을 저온 혼합공정에서 즉 약 18~50℃의 온도에서 실옥산 시약으로 피복한다. 탄산석회의 함량이 높기 때문에 실란액은 비교적 빨리 과립표면으로부터 속으로 침투되며 그 결과 건조한 과립이 생긴다.The lime carbonate packed granules thus treated are coated with a siloxane reagent in a low temperature mixing process, ie at a temperature of about 18-50 ° C. Due to the high content of lime carbonate, the silane solution penetrates into the granule surface relatively quickly, resulting in dry granules.
실옥산 시약함유과립을, 탄산석회외에 산화방지제와 경화촉매를 함유하는 PE뱃치와, 95 : 5의 비율로 혼합한다. 그 다음 동일 압출기에서 동일공정으로 약 200℃에서 지상결합 및 성형이 일어난다.Granules containing the siloxane reagent are mixed with a PE batch containing an antioxidant and a curing catalyst in addition to lime carbonate in a ratio of 95: 5. Then surface bonding and molding takes place at about 200 ° C. in the same process in the same extruder.
실시예로서의 배합제의 조성은 다음과 같다.The composition of the compounding agent as an example is as follows.
배합제 예 1Formulation Example 1
폴리에틸렌 100부 충 전 재 45-55부Polyethylene 100 parts Filler 45-55
실 란 2.5부 과 산 화 물 0.2부2.5 parts of silane and 0.2 parts of acid
촉 매 0.07부0.07 parts catalyst
배합제 예2Formulation Example 2
공 중 합 체 100부 충 전 제 45-55부Polymer Polymer Part 100 Refills Part 45-55
실 란 2.0부 과 산 화 물 0.2부2.0 parts of silane and 0.2 parts of acid
촉 매 0.07부0.07 parts catalyst
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Application Number | Priority Date | Filing Date | Title |
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KR1019790001232A KR830000407B1 (en) | 1979-04-18 | 1979-04-18 | Process for preparing filled and curable polymer materials |
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KR1019790001232A KR830000407B1 (en) | 1979-04-18 | 1979-04-18 | Process for preparing filled and curable polymer materials |
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KR830000407B1 true KR830000407B1 (en) | 1983-03-07 |
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KR1019790001232A KR830000407B1 (en) | 1979-04-18 | 1979-04-18 | Process for preparing filled and curable polymer materials |
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1979
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