JP2021120454A - 異相ポリマー組成物を作製するための方法 - Google Patents
異相ポリマー組成物を作製するための方法 Download PDFInfo
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- JP2021120454A JP2021120454A JP2021066865A JP2021066865A JP2021120454A JP 2021120454 A JP2021120454 A JP 2021120454A JP 2021066865 A JP2021066865 A JP 2021066865A JP 2021066865 A JP2021066865 A JP 2021066865A JP 2021120454 A JP2021120454 A JP 2021120454A
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- SWAXTRYEYUTSAP-UHFFFAOYSA-N tert-butyl ethaneperoxoate Chemical compound CC(=O)OOC(C)(C)C SWAXTRYEYUTSAP-UHFFFAOYSA-N 0.000 description 1
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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
- C08J3/246—Intercrosslinking of at least two polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
- C08F297/06—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type
- C08F297/08—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type polymerising mono-olefins
- C08F297/083—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type polymerising mono-olefins the monomers being ethylene or propylene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F255/00—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00
- C08F255/02—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms
- C08F255/04—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms on to ethene-propene copolymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
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Abstract
Description
(a)ラジカル付加反応においてフリーラジカルと反応できる官能基を2個以上含む相溶化剤を用意する工程;
(b)プロピレンポリマー相およびエチレンポリマー相を含み、かつエチレンランの数平均連鎖長(number-average sequence length of ethylene run)が3以上である異相ポリマー組成物を用意する工程;
(c)相溶化剤と異相ポリマー組成物を混合する工程;ならびに
(d)プロピレンポリマー相およびエチレンポリマー相中でフリーラジカルを生成する工程
を含み、それによって相溶化剤の少なくとも一部がプロピレンポリマー相とエチレンポリマー相の両方のフリーラジカルと反応して、プロピレンポリマー相中のプロピレンポリマーとの結合およびエチレンポリマー相中のエチレンポリマーとの結合を形成する、方法を提供する。
この定義では、用語「置換アレーン」は、単環式および多環芳香族炭化水素から誘導された化合物を意味し、その炭化水素の1種以上の水素原子は、非水素原子(例えば、ハロゲン原子)または非アルキル官能基(例えば、ヒドロキシ基)で置きかえられている。
この定義では、用語「ヘテロアレーン」は、単環式および多環芳香族炭化水素から誘導された化合物を意味し、その炭化水素の少なくとも1種のメチン基(−C=)は、3価のヘテロ原子と置きかえられており、ならびに/または炭化水素の少なくとも1種のビニリデン基(−CH=CH−)は、2価のヘテロ原子と置きかえられている。
の構造に一致する基からなる群から選択される。
Dmol3プログラムを使用しているとき、計算のための入力パラメーターは、分子Mについては表A、ラジカルM・およびH・については表Bに示す。H°(H・)の値は、−0.496344ハートリー(1ハートリー(Ha)=627.51kcal/mol)で計算される。
したがって、より高いモル質量を有する化合物は、一般により高い融点および沸点を有する。任意の特定の理論に拘泥するものではないが、相溶化剤の融点および沸点は、本発明の組成物中の相溶化剤の効力に影響することがあると考えられている。例えば、比較的低いモル質量および低い沸点(例えば、ポリマー組成物が押出される温度よりも著しく低い沸点)を有する相溶化剤は、押出しプロセス中にかなりの程度まで揮発し得ると考えられており、それによってポリマー組成物の特性を改変する相溶化剤が少なくなる。したがって、相溶化剤は、好ましくはポリマー組成物が押し出される温度よりも高い沸点を相溶化剤が示すのに十分高いモル質量を有する。一連の好ましい態様では、相溶化剤は、好ましくは約130g/mol以上、約140g/mol以上、約150g/mol以上、または約160g/mol以上のモル質量を有している。また、比較的高い融点(例えば、ポリマー組成物が押し出される温度よりも高い融点)を有する相溶化剤は、押出しプロセス中に溶融ポリマー中に十分に分散しないかもしれない、または少なくとも押出し温度よりも低い融点を有する相溶化剤と同様には分散しないと考えられている。そして、相溶化剤の分散が不十分だと、十分に分散した相溶化剤と比較して達成できる物理的性質の改善に負の影響を与えることになる。したがって、一連の好ましい態様では、相溶化剤は、約230℃以下、約220℃以下、約210℃以下、または200℃以下の融点を有する。
during Solid−State Shear Pulverization」−vol.46、pp.7834〜7844(2013)に記載されているように、本発明の別の態様では、相溶化剤は、固体状態の異相ポリマー組成物と合わせてもよく、フリーラジカルは、固相剪断粉砕中に生成され得る。
さらなる例として、組成物は、充填剤、例えば炭酸カルシウム、タルク、ガラス繊維、ガラス球、無機ウィスカー、例えばMilliken Chemical、USAから入手可能なHyperform(登録商標)HPR−803i、マグネシウムオキシサルフェートウィスカー、硫酸カルシウムウィスカー、炭酸カルシウムウィスカー、雲母、珪灰石、粘土、例えばモンモリロナイト、およびバイオ源または天然充填剤を含んでいてもよい。添加剤は、改変された異相ポリマー組成物中の全成分の最大75重量%までを占めていてもよい。
[0086]以下の例は、本発明の方法において改変されていない異相ポリオレフィン組成物中のエチレンの数平均連鎖長の効果を示す。
[0089]以下の例は、本発明の方法において異相ポリオレフィン組成物中のエチレントライアドの相対モル%の効果を示す
[0090]6種の異相ポリマー組成物を生成し、試料2A〜2Dを2つの異なるポリプロピレン耐衝撃性コポリマー、樹脂2−1および樹脂2−2から生成した。組成物中の過酸化物結合(O−O)対相溶化剤のモル比が0.5:1になるように、試料2Aおよび2Bは、樹脂2−1または樹脂2−2のいずれかを過酸化物、2,5−ビス(tert−ブチルペルオキシ)−2,5−ジメチルヘキサン(CAS# 78−63−7)、および相溶化剤、2−(2−フリルメチレン)マロノニトリル(CAS# 3237−22−7)と混合することによって作製された。組成物中の過酸化物結合(O−O)対相溶化剤のモル比が2:1になるように、試料2Cおよび2Dは、樹脂2−1または樹脂2−2のいずれかを過酸化物、2,5−ビス(tert−ブチルペルオキシ)−2,5−ジメチルヘキサン(CAS# 78−63−7、Luperox 101)、および相溶化剤、TEMPO−メタクリレート(CAS# 15051−46−4)と混合することによって作製された。試料2A〜2Dの組成物を表2に示す。改変されていない樹脂2−1および改変されていない樹脂2−2からなる比較例(Comp.2AおよびComp.2B)も表2に示す。
[0093]以下の例は、本発明の方法において異相ポリプロピレン組成物中のエチレントライアドの割合およびエチレンの数平均連鎖長の増加の影響を例示する。
Claims (10)
- 異相ポリマー組成物を改変するための方法であって、
(a)ラジカル付加反応においてフリーラジカルと反応できる官能基を2個以上含む相溶化剤を用意する工程;
(b)プロピレンポリマー相およびエチレンポリマー相を含み、かつエチレンランの数平均連鎖長が3以上である異相ポリマー組成物を用意する工程;
(c)前記相溶化剤と前記異相ポリマー組成物を混合する工程;ならびに
(d)前記プロピレンポリマー相および前記エチレンポリマー相中でフリーラジカルを生成する工程
を含み、それによって前記相溶化剤の少なくとも一部が前記プロピレンポリマー相と前記エチレンポリマー相の両方のフリーラジカルと反応して、前記プロピレンポリマー相中のプロピレンポリマーとの結合および前記エチレンポリマー相中のエチレンポリマーとの結合を形成する、方法。 - 前記異相ポリマー組成物が、前記異相ポリマー組成物の全重量に基づいて約6重量%以上のエチレンを含む、請求項1に記載の方法。
- 前記異相ポリマー組成物が、約10重量%以上のキシレン可溶分を含む、請求項1に記載の方法。
- 前記異相ポリマー組成物中に存在する前記エチレンの約5モル%以上が、エチレントライアドで存在する、請求項1に記載の方法。
- 前記異相ポリマー組成物の60℃昇温溶離分別法(TREF)画分中に存在する前記エチレンの約30モル%以上が、エチレントライアドで存在する、請求項1に記載の方法。
- 前記異相ポリマー組成物の80℃昇温溶離分別法(TREF)画分中に存在する前記エチレンの約30モル%以上が、エチレントライアドで存在する、請求項1に記載の方法。
- 前記異相ポリマー組成物の100℃昇温溶離分別法(TREF)画分中に存在する前記エチレンの約5モル%以上が、エチレントライアドで存在する、請求項1に記載の方法。
- 前記異相ポリマー組成物の60℃昇温溶離分別法(TREF)画分中に存在するエチレンランの数平均連鎖長が、3以上である、請求項1に記載の方法。
- 前記異相ポリマー組成物の80℃昇温溶離分別法(TREF)画分中に存在するエチレンランの数平均連鎖長が、7以上である、請求項1に記載の方法。
- 前記異相ポリマー組成物の100℃昇温溶離分別法(TREF)画分中に存在するエチレンランの数平均連鎖長が、10以上である、請求項1に記載の方法。
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ZA201801122B (en) | 2019-01-30 |
JP7334042B2 (ja) | 2023-08-28 |
BR112018003266B1 (pt) | 2021-12-28 |
PL3347389T3 (pl) | 2021-04-19 |
KR20180052680A (ko) | 2018-05-18 |
JP2018528313A (ja) | 2018-09-27 |
KR101958609B1 (ko) | 2019-07-04 |
TW201716472A (zh) | 2017-05-16 |
RU2687248C1 (ru) | 2019-05-08 |
US20170073511A1 (en) | 2017-03-16 |
WO2017044387A1 (en) | 2017-03-16 |
EP3347389B1 (en) | 2020-11-25 |
TWI622607B (zh) | 2018-05-01 |
EP3347389A1 (en) | 2018-07-18 |
US10100187B2 (en) | 2018-10-16 |
SA518391104B1 (ar) | 2022-04-13 |
CN108350130A (zh) | 2018-07-31 |
BR112018003266A2 (pt) | 2018-09-25 |
CN116925465A (zh) | 2023-10-24 |
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