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Применить Всего найдено 7034. Отображено 200.
22-12-2023 дата публикации

СОПОЛИМЕР ПРОПИЛЕНА И БУТЕНА

Номер: RU2810168C2
Принадлежит: БОРЕАЛИС АГ (AT)

Настоящее изобретение относится к мультимодальному статистическому сополимеру пропилена и бутена, подходящему для образования пленки, имеющему скорость течения расплава (MFR2) от 2,5 до 16,0 г/10 мин и содержание бутена от 5,0 до 20,0 % масс., при этом модуль упругости при изгибе указанного сополимера составляет от 750 до 1600 МПа, при этом указанный сополимер получен с применением металлоценового катализатора, и при этом указанный сополимер содержит: (i) от 30 до 55 % масс. фракции сополимера (A) пропилена и бутена, имеющего MFR2от 0,5 до 10,0 г/10 мин и содержание бутена от 2,0 до 10,0 % масс., и (ii) от 70 до 45 % масс. фракции сополимера (B) пропилена и бутена, имеющего MFR2от 0,5 до 10,0 г/10 мин и содержание бутена от 6,0 до 20,0 % масс., причем фракции (A) и (B) являются разными. Также изобретение относится к способу получения указанного выше мультимодального статистического сополимера пропилена и бутена, к пленке, выполненной из него, и к его применению для изготовления пленки.

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27-11-2011 дата публикации

СОПОЛИМЕРЫ ЭТИЛЕНА И АЛЬФА-ОЛЕФИНА И СПОСОБЫ ПОЛИМЕРИЗАЦИИ ДЛЯ ИХ ПОЛУЧЕНИЯ

Номер: RU2434888C2

Настоящее изобретение относится к сополимерам этилена и альфа-олефинов. Описан способ получения сополимера этилена и альфа-олефина, где способ включает: контактирование этилена и, по меньшей мере, одного альфа-олефина с металлоценовым катализатором в, по меньшей мере, одном газофазном реакторе при давлении в реакторе от 0,7 до 70 бар и при температуре в реакторе от 20°С до 150°С с получением в ходе полимеризации сополимера этилена и альфа-олефина, где сополимер этилена и альфа-олефина удовлетворяет следующим условиям: плотность 0,927 г/см3 или более, индекс расплава (I2) от 1 дециграмм/мин до 200 дециграмм/мин, соотношение индексов расплава (I21/I2) от 15 до 40, молекулярно-массовое распределение Mw/Mn 2-4, значение ESCR 500 часов или более в том случае, когда измерение проводят в соответствии со стандартом ASTM 1693/В в 10% растворе Igepal, значение Т75-Т25 4 или более, где Т25 представляет собой температуру, при которой получают 25% элюированного полимера, и Т75 представляет собой температуру ...

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22-12-2023 дата публикации

СОПОЛИМЕР ПРОПИЛЕНА

Номер: RU2810169C2
Принадлежит: БОРЕАЛИС АГ (AT)

Настоящее изобретение относится к мультимодальному статистическому сополимеру пропилена и бутена, подходящему для образования пленки, имеющему скорость течения расплава (MFR2) от 2,5 до 16,0 г/10 мин и содержание бутена от 2,0 до 7,0 % масс., при этом модуль упругости при изгибе указанного сополимера составляет от 850 МПа до 1600 МПа, при этом указанный сополимер получен с применением металлоценового катализатора и при этом указанный сополимер содержит: (i) от 40 до 60 % масс. фракции (A) пропилена и бутена, имеющей MFR2от 0,5 до 10,0 г/10 мин и содержание бутена от 0,5 до 10,0 % масс., и (ii) от 60 до 40 % масс. фракции (B) пропилена и бутена, имеющей MFR2от 0,5 до 10,0 г/10 мин и содержание бутена от 1,0 до менее 6,0 % масс., при этом фракции (A) и (B) являются разными. Также изобретение относится к способу получения указанного выше мультимодального статистического сополимера пропилена и бутена, к пленке, выполненной из него, и к его применению для изготовления пленки. Технический результат ...

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25-10-2018 дата публикации

ПРОИЗВОДСТВО ПОЛИЭТИЛЕНОВЫХ ИЗДЕЛИЙ С УЛУЧШЕННЫМИ ЖЕСТКОСТЬЮ, УДАРНОЙ ВЯЗКОСТЬЮ И ПЕРЕРАБАТЫВАЕМОСТЬЮ

Номер: RU2670755C2

Изобретение относится к этилен/альфа-олефиновым сополимерам. Полимер содержит этилен и по меньшей мере один альфа-олефин с 4-20 атомами углерода. Полимер имеет отношение индекса расплава (ОИР) больше чем приблизительно 40. Полимер также имеет значение Mw1/Mw2 по меньшей мере приблизительно 2,0, где Mw1/Mw2 представляет собой отношение средневесовой молекулярной массы (Мw) для первой половины кривой фракционирования при элюировании с повышением температуры (TREF) из кросс-фракционной хроматографии (CFC) к Mw для второй половины кривой TREF. Полимер также имеет значение Tw1-Tw2 меньше чем приблизительно -15°С, где Tw1-Tw2 представляет собой разницу средневзвешенной температуры элюирования (Tw) для первой половины кривой TREF и Tw для второй половины кривой TREF. Технический результат – получение полимера с улучшенными физическими свойствами. 9 з.п. ф-лы, 8 ил., 10 табл., 10 пр.

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19-05-2020 дата публикации

ГАЗОФАЗНЫЙ СПОСОБ ПОЛИМЕРИЗАЦИИ ПРОПИЛЕНА

Номер: RU2721530C2

Изобретение относится к способу газофазной полимеризации пропилена, необязательно в смеси с другими олефинами. Описан способ гомополимеризации или сополимеризации пропилена с прочими олефинами, осуществляемый в присутствии каталитической системы. Каталитическая система включает (а) твердый компонент катализатора, содержащий Mg, Ti, галоген, электронный донор, выбранный из 1,3-диэфиров, и 10-85 мас.% олефинового полимера; (b) алкилалюминиевое соединение; и (c) внешнее электронодонорное соединение, выбранное из соединения кремния. Компоненты (b) и (c) берутся в таких количествах, чтобы молярное соотношение Al/(ED) составляло 2-200. Твердый компонент имеет средний размер частиц 10-100 мкм. Способ пригоден для получения полипропиленового продукта, имеющего хорошие морфологические свойства, высокую стереорегулярность и обладающего свойствами самозатухания, выборочно решая или смягчая вредные воздействия, вызванные полимеризацией мелких частиц катализатора. 11 з.п. ф-лы, 1 табл., 18 пр.

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22-10-2021 дата публикации

ПОЛИМЕРНАЯ КОМПОЗИЦИЯ ДЛЯ УКУПОРОЧНЫХ СРЕДСТВ ДЛЯ КОНТЕЙНЕРА

Номер: RU2757915C2

Изобретение относится к полимерной композиции для формования и укупорочному средству для контейнера, содержащего такую полимерную композицию. Композиция содержит гомополимер этилена и сополимер этилена, содержащий сомономер, представляющий собой 1-бутен, в количестве от 0,60 до 0,65 мол.% по отношению к общему количеству мономера в сополимере этилена. Сополимер этилена имеет более высокую средневесовую молекулярную массу, чем гомополимер этилена, причем полимерная композиция имеет плотность в диапазоне 0,9553-0,9560 г/см3, скорость течения расплава MFR2от 0,72 до 0,78 г/10 мин в условиях проведения испытания при 190°C с нагрузкой 2,16 кг, средневесовую молекулярную массу от 150000 до 200000 г/моль, вязкость при угловой частоте 0,01 [1/с], η0,01при 190°С от 22371 до 24420 Па*с. При этом массовое соотношение гомополимера этилена к сополимеру этилена в полимерной композиции находится в диапазоне от 45:55 до 55:45. Полимерная композиция имеет полупериод изотермической кристаллизации, который ...

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11-05-2021 дата публикации

КОМПОНЕНТЫ КАТАЛИЗАТОРА И ПОЛУЧЕННЫЕ ИЗ НИХ КАТАЛИЗАТОРЫ ДЛЯ ПОЛИМЕРИЗАЦИИ ОЛЕФИНОВ

Номер: RU2747650C2

Изобретение относится к компонентам катализатора для полимеризации олефинов CH2=CHR, где R представляет собой водород или углеводородный радикал с 1-12 атомами углерода, катализаторам для полимеризации олефинов и способу (со)полимеризации олефинов. Компоненты катализатора для полимеризации олефинов содержат Ti, Mg, хлор и внутренний донор, выбранный из сложных эфиров алифатических монокарбоновых кислот (EAA), и другой внутренний донор, выбранный из циклических простых эфиров (CE). При этом молярное соотношение EAA/CE составляет от 0,2 до менее чем 20, молярное соотношение Mg/Ti составляет от 10 до 40, и атомы Ti присутствуют в виде тетрахлорида титана. Катализатор содержит продукт реакции между твердым компонентом катализатора и одним или несколькими алкилалюминиевыми соединениями. Техническим результатом заявленного изобретения является повышенная морфологическая стабильность катализатора и, по меньшей мере, приемлемая активность и способность сохранять постоянство свойств полимера. 3 ...

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22-10-2021 дата публикации

МУЛЬТИМОДАЛЬНАЯ ПОЛИЭТИЛЕНОВАЯ ПЛЕНКА

Номер: RU2757914C2

Изобретение относится к мультимодальной полиэтиленовой композиции для формования, в частности для пленок или геомембран. Композиция включает: (А) от 40 до 65% по массе полиэтилена с низкой молекулярной массой, имеющего средневзвешенную молекулярную массу (Mw) от 20000 до 90000 г/моль, причем полиэтилен с низкой молекулярной массой имеет значение MI2от 500 до 1000 г/10 мин согласно стандарту ASTM D 1238, (В) от 5 до 17% по массе полиэтилена со сверхвысокой молекулярной массой, имеющего средневзвешенную молекулярную массу (Mw) от более 1000000 до 5000000 г/моль, и (С) от 30 до 50% по массе полиэтилена с высокой молекулярной массой, имеющего средневзвешенную молекулярную массу (Mw) от более 150000 до 1000000 г/моль. Причем плотность полиэтилена со сверхвысокой молекулярной массой и полиэтилена с высокой молекулярной массой составляет величину в одном и том же диапазоне, и обе плотности находятся в диапазоне от 0,910 до 0,940 г/см3. Молекулярно-массовое распределение мультимодальной полиэтиленовой ...

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10-01-2013 дата публикации

СПОСОБ ПОЛУЧЕНИЯ ПОЛИМЕРОВ ПРОПИЛЕНА С ВЫСОКОЙ ТЕКУЧЕСТЬЮ

Номер: RU2471811C2

Изобретение относится к способу получения полимеров пропилена. Полученный полимер пропилена имеет скорость течения расплава (230°С, 2,16 кг) выше 30 г/10 мин. Способ осуществляется в присутствии каталитической системы, включающей (a) твердый каталитический компонент, содержащий Mg, Ti, галоген и электронодонорное соединение, выбранное из сукцинатов; (b) алкилалюминиевый сокатализатор; и (c) соединение кремния формулы RSi(OR), в которой Rпредставляет собой разветвленный алкил и R представляет собой независимо C-Cалкил. Описан также способ получения композиции полимера пропилена и гетерофазные композиции. Технический результат - получение полимеров пропилена, обладающих одновременно широким ММР и высокой скоростью течения расплава. 3 н. и 8 з.п. ф-лы, 5 табл., 7 пр.

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20-06-2014 дата публикации

ПЛЕНКИ, ПОЛУЧЕННЫЕ ИЗ ГЕТЕРОГЕННОГО СОПОЛИМЕРА ЭТИЛЕН/АЛЬФА-ОЛЕФИН

Номер: RU2519776C2

Изобретение относится к многослойной пленке для получения готового изделия и готовому изделию, содержащему такую пленку. Многослойная пленка включает, по меньшей мере, два слоя. Первый слой включает первый сополимер этилена и, по меньшей мере, одного альфа-олефина. Первый сополимер имеет плотность менее 0,925 г/сми средневязкостную молекулярную массу Mи температурное плато между сополимером и высококристаллической фракцией Tтакие, что Mдля фракции выше Tиз ATREF, разделенная на Mвсего полимера из ATREF (M/M), составляет менее 1,95. Первый сополимер имеет индекс ширины распределения по составу (CDBI) менее 60%. Один другой второй слой включает второй сополимер этилена и, по меньшей мере, одного альфа-олефина. Второй сополимер имеет плотность от 0,925 до 0,965 г/см. Технический результат - получение пленки с улучшенными оптическими свойствами, жесткостью, сопротивлением проколам, сопротивлением раздиру и технологичностью. 2 н. и 13 з.п. ф-лы, 3 табл., 1 ил., 1 табл.

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27-07-2017 дата публикации

ПОЛИПРОПИЛЕНОВАЯ КОМПОЗИЦИЯ С УЛУЧШЕННОЙ УДАРНОЙ ПРОЧНОСТЬЮ ДЛЯ ПРИМЕНЕНИЯ В ТРУБАХ

Номер: RU2626395C2

Изобретение относится к полипропиленовой композиции, подходящей для получения труб и фитингов для труб, а также к способу ее получения. Композиция содержит статистический сополимер пропилена с по меньшей мере одним сомономером, выбранным из альфа-олефинов с 2 или от 4 до 8 атомов углерода. Статистический сополимер пропилена состоит по меньшей мере из статистического сополимера пропилена с низкой молекулярной массой (низкомолекулярная (LMW) фракция) и статистического сополимера пропилена с высокой молекулярной массой (высокомолекулярная (HMW) фракция), при этом среднемассовая молекулярная масса низкомолекулярной фракции ниже, чем среднемассовая молекулярная масса высокомолекулярной фракции. Причем полипропиленовая композиция имеет скорость течения расплава (MFR) (2,16 кг, 230°C) от 0,05 до 1,0 г/10 мин, определенную в соответствии с ISO 1133, коэффициент полидисперсности (PI) от 2,0 до 7,0 и ударную вязкость по Шарли образца с надрезом при 0°C по меньшей мере 6,5 кДж/м, определенную в соответствии ...

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05-07-2017 дата публикации

ТЕРМОФОРМОВАННОЕ ИЗДЕЛИЕ С ВЫСОКОЙ ЖЕСТКОСТЬЮ И ХОРОШИМИ ОПТИЧЕСКИМИ СВОЙСТВАМИ

Номер: RU2624703C2

Изобретение относится к термоформованным изделиям, в частности к термоформованным стаканам, включающим боковую стенку, состоящую из полимера на основе пропилена, содержащего ароматический сложный диэфир замещенного фенилена, выбранный из группы 3-метил-5-трет-бутил-1,2-фенилендибензоата и 3,5-диизопропил-1,2-фенилендибензоата и характеризующуюся значением мутности от 1 до 10% при измерении в соответствии с ASTM D 1003. Термоформованные изделия имеют высокую жесткость, хорошую прочность на сжатие, превосходную технологичность и превосходные оптические свойства. 2 н. и 10 з.п. ф-лы, 3 табл., 3 ил.

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18-11-2021 дата публикации

КОМПОЗИЦИЯ КАТАЛИЗАТОРА ДЛЯ ПОЛИМЕРИЗАЦИИ ОЛЕФИНА, СПОСОБ ПОЛУЧЕНИЯ ПОЛИОЛЕФИНА И ПОЛИОЛЕФИНОВАЯ СМОЛА

Номер: RU2759915C2
Принадлежит: ДЛ КЕМИКАЛ КО., ЛТД. (KR)

Изобретение относится к композиции катализатора полимеризации для получения полиолефина, содержащей одно первое металлоорганическое соединение, описывающееся следующей далее формулой 1, одно второе металлоорганическое соединение, описывающееся следующей далее формулой 2, и алкилалюмоксан; способу получения полиолефина и полиолефиновых смол. 5 н. и 7 з.п. ф-лы, 8 ил., 8 табл., 12 пр.

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13-01-2020 дата публикации

Номер: RU2018109999A3
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29-01-2020 дата публикации

Номер: RU2018121643A3
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09-10-2019 дата публикации

Номер: RU2018107539A3
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27-09-2019 дата публикации

Номер: RU2017144534A3
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29-01-2019 дата публикации

Номер: RU2017111499A3
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13-12-2019 дата публикации

Номер: RU2018104667A3
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12-03-2020 дата публикации

Номер: RU2018123722A3
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15-01-2020 дата публикации

Номер: RU2018117616A3
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09-12-2020 дата публикации

Номер: RU2019109042A3
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07-05-2018 дата публикации

Номер: RU2016141292A3
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28-06-2018 дата публикации

Номер: RU2016132399A3
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11-10-2018 дата публикации

Номер: RU2017107510A3
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27-01-2021 дата публикации

Номер: RU2019115582A3
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13-05-2021 дата публикации

Номер: RU2019136079A3
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17-07-2019 дата публикации

Номер: RU2017141782A3
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25-02-2019 дата публикации

Номер: RU2017126222A3
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18-12-2019 дата публикации

СПОСОБ ПОЛИМЕРИЗАЦИИ ОЛЕФИНОВ В ГАЗОФАЗНОМ РЕАКТОРЕ С ТРЕМЯ ИЛИ БОЛЕЕ ЗОНАМИ ПОЛИМЕРИЗАЦИИ

Номер: RU2709525C1

Изобретение относится к способу получения олефинового полимера в присутствии водорода в газофазном реакторе полимеризации. Реактор полимеризации имеет три или более зон полимеризации, где по меньшей мере две из зон полимеризации являются подзонами установки полимеризации, в которой растущие полимерные частицы стекают вниз в уплотненной форме. По меньшей мере одна зона полимеризации имеет соотношение водорода к суммарному объему олефинов, которое в 1,5 раза ниже, чем соотношение водорода к суммарному объему олефинов в зоне полимеризации, имеющей самое высокое соотношение водорода к суммарному объему олефинов и которое в 1,5 раза выше, чем соотношение водорода к суммарному объему олефинов в зоне полимеризации, имеющей самое низкое соотношение водорода к суммарному объему олефинов. Способ полимеризации олефинов позволяет простым образом осуществлять полимеризацию в трех или более зонах полимеризации в одном реакторе полимеризации и получать гомогенные мультимодальные олефиновые полимеры с ...

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11-09-2019 дата публикации

ВЯЗКАЯ КОМПОЗИЦИЯ ПРОПИЛЕНА С ХОРОШЕЙ СТАБИЛЬНОСТЬЮ РАЗМЕРОВ И ОТЛИЧНЫМ ВНЕШНИМ ВИДОМ ПОВЕРХНОСТИ

Номер: RU2699810C1
Принадлежит: БОРЕАЛИС АГ (AT)

Изобретение относится к композиции, предназначенной для получения литых изделий со сниженным эффектом тигровых полос, изделию, содержащему такую композицию и применению перекиси для обработки композиции полипропилена с получением композиции для литых изделий. Композиция по изобретению содержит от 35 до 80 мас.% модифицированной композиции полипропилена и от 20 до 50 мас.% неорганического наполнителя от общей массы композиции. Модифицированную композицию полипропилена получают обработкой композиции полипропилена перекисью. Композиция полипропилена содержит гетерофазную композицию из (полу)кристаллического полипропилена и сополимера этилена/пропилена, диспергированную в указанном (полу)кристаллическом полипропилене, и пластомер, представляющий собой сополимер этилена и по меньшей мере одного С-Сα-олефина. Характеристическая вязкость IV, определенная согласно DIN ISO 1628/1 (в декалине при 135°С), фракции, растворимой в холодном ксилоле, модифицированной композиции полипропилена составляет ...

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27-11-2013 дата публикации

ГЕТЕРОФАЗНЫЙ ПОЛИПРОПИЛЕН С УЛУЧШЕННЫМ СООТНОШЕНИЕМ МЕЖДУ ЖЕСТКОСТЬЮ И ПРОЗРАЧНОСТЬЮ

Номер: RU2499804C1
Принадлежит: БОРЕАЛИС АГ (AT)

Группа изобретений относится к гетерофазной полипропиленовой композиции с достаточно высоким показателем текучести расплава, высокой жесткостью, приемлемыми ударными свойствами и выгодным соотношением между жесткостью и прозрачностью, способу получения полипропиленовой композиции, изделию, изготовленному из полипропиленовой композиции и применению полипропиленовой композиции для изготовления пленок и литых изделий, таких как тонкостенные полимерные контейнеры для упаковки. Полипропиленовая гетерофазная композиция включает по меньшей мере фракцию полипропиленового гомополимера, фракцию статистического полипропиленового сополимера, две различные фракции этилен пропиленового каучука и фракцию гомо- или сополимера этилена. Технический результат, достигаемый при использовании композиции и способа ее получения для изготовления пленок и литых изделий, заключается в том, чтобы обеспечить хорошую ударную прочность при низкой температуре, а также улучшенную текучесть и прозрачность изделия. 4 н.

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22-10-2019 дата публикации

СПОСОБ ПОЛИМЕРИЗАЦИИ ОЛЕФИНОВ В ГАЗОФАЗНОМ РЕАКТОРЕ, ВКЛЮЧАЮЩЕМ РЕАКТОР ВОСХОДЯЩЕГО ПОТОКА И РЕАКТОР НИСХОДЯЩЕГО ПОТОКА

Номер: RU2703716C1

Изобретение относится к способу получения полимера этилена, включающему гомополимеризацию этилена или сополимеризацию этилена с одним или несколькими сомономерами в реакторе газофазной полимеризации. Реактор газофазной полимеризации имеет реактор восходящего потока, в котором растущие полимерные частицы движутся вверх в условиях псевдоожижения, быстрого псевдоожижения или других режимах транспортировки, и реактор нисходящего потока, в котором растущие частички полимера стекают вниз в уплотненной форме. В реакторе нисходящего потока остаточный объем полимерных частиц составляет 55- 80 мас.% от остаточного объема полимерных частиц в реакторе газофазной полимеризации. Технический результат – предотвращение и минимизация образования агломератов, комков или отложений на стенке реактора. 14 з.п. ф-лы, 1 ил., 1 табл., 3 пр.

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10-01-2019 дата публикации

КОМПОЗИЦИЯ НЕУПОРЯДОЧЕННОГО CCСОПОЛИМЕРА С УЛУЧШЕННЫМ БАЛАНСОМ МЕЖДУ ТЕМПЕРАТУРОЙ НАЧАЛА СВАРИВАНИЯ И ТЕМПЕРАТУРОЙ ПЛАВЛЕНИЯ

Номер: RU2676711C1
Принадлежит: БОРЕАЛИС АГ (AT)

Изобретение относится к композиции C-Cнеупорядоченного сополимера. Композиция C-Cнеупорядоченного сополимера содержит 3 полимерные фракции (А), (В) и (С) с различным содержанием сомономеров. Фракция (А) включает 30-65 масс.% C-Cнеупорядоченного сополимера с содержанием этилена (СА) 0,4-1,5 масс. % от общей массы сополимера (А), как измерено при использовании инфракрасной спектроскопии Фурье с преобразованием (FTIR). Фракция (В) включает 25-50 масс.% C-Cнеупорядоченного сополимера с содержанием этилена (СВ) 3,0-10,0 масс.% от общей массы сополимера (В). Фракция (С) включает 5-35 масс.% C-Cнеупорядоченного сополимера с содержанием этилена (СС) 7,0-15,0 масс.% от общей массы сополимера (С). Сумма 3 полимерных фракций (А), (В) и (С) составляет 100%, и при этом содержание сомономера в полимерных фракциях увеличивается от фракции (А) к фракции (С) согласно (СА)<(СВ)<(СС). Технический результат - улучшенный баланс между температурой начала сваривания (SIT) и температурой плавления (Тm), хорошие ...

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27-11-2011 дата публикации

СПОСОБ ПОЛУЧЕНИЯ ПОЛИМЕРОВ ПРОПИЛЕНА С ВЫСОКОЙ ТЕКУЧЕСТЬЮ

Номер: RU2010119499A
Принадлежит:

... 1. Способ получения полимеров пропилена, имеющих показатель полидисперсности выше 5 и значение индекса расплава, определенное согласно ISO 1133 (230°C, 2,16 кг), выше 30 г/10 мин, осуществляемый в присутствии каталитической системы, включающей ! (а) твердый каталитический компонент, содержащий атомы Mg, Ti и галогена и электронодонорное соединение, выбранное из сукцинатов; ! (b) алкилалюминиевый сокатализатор; и ! (с) соединение кремния формулы R1Si(OR)3, в которой R1 представляет собой разветвленный алкил и R представляет собой независимо С1-С10 алкил. ! 2. Способ по п.1, в котором электронодонорное соединение выбрано из сукцинатов формулы (I): ! ! где радикалы R1 и R2, одинаковые или отличающиеся друг от друга, представляют собой С1-С20 линейную или разветвленную алкильную, алкенильную, циклоалкильную, арильную, арилалкильную или алкиларильную группу, необязательно содержащую гетероатомы; радикалы R3-R6, одинаковые или отличающиеся друг от друга, представляют собой водород или С1-С20 ...

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27-09-2016 дата публикации

СПОСОБ ПОЛУЧЕНИЯ ПОЛИПРОПИЛЕНА, ИМЕЮЩИЙ ПОВЫШЕННУЮ ПРОИЗВОДИТЕЛЬНОСТЬ

Номер: RU2015106531A
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... 1. Способ получения полипропилена (РР) при использовании процесса последовательной полимеризации, включающий реактор предварительной полимеризации (PR) и по меньшей мере два реактора полимеризации (R1 и R2), соединенных в серию, где полимеризацию проводят по меньшей мере в двух реакторах полимеризации (R1 и R2) в присутствии катализатора Циглера-Натта (ZN-C), и указанный катализатор Циглера-Натта (ZN-C) содержит(a) прокатализатор (PC), содержащий(a1) соединение переходного металла (ТМ),(а2) соединение металла (М), где металл выбирают из групп 1-3 Периодической таблицы (IUPAC),(а3) внутренний донор электронов (ID),(b) сокатализатор (Со) и(c) внешний донор (ED),гдеуказанный катализатор Циглера-Натта (ZN-C) присутствует в реакторе предварительной полимеризации (PR) и дополнительно к пропилену (С3) в указанный реактор предварительной полимеризации (PR) подают этилен (C2)(i) при соотношении подачи C2/C3 от 0,5 до 10,0 г/кг;и/или(ii) подается, таким образом, что в реакторе предварительной полимеризации ...

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10-09-2016 дата публикации

КАТАЛИЗАТОР ДЛЯ ПОЛИМЕРИЗАЦИИ ОЛЕФИНОВ И СПОСОБ ЕГО ПОЛУЧЕНИЯ

Номер: RU2015105287A
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... 1. Способ получения твердого титанового каталитического компонента для применения в качестве прокатализатора для каталитической системы Циглера-Натта, причем указанный способ в основном включает:(a) контактирование соединения диалкилмагния, представленного R′R″Mg, с солюбилизирующим магний соединением с образованием реакционной смеси, где каждый из элементов R′ и R″ представляет собой углеводородную группу, имеющую С-Сатомов углерода, отличающийся тем, что контактирование соединения диалкилмагния с солюбилизирующим магний соединением приводит к образованию первой реакционной смеси, содержащей алкоксид магния в реакционной смеси;(b) добавление титанового соединения, представленного Ti(OR′′′)X, где X представляет собой атом галогена; R′′′ - углеводородную группу и p - целое число, меньшее или равное 4, для преобразования алкоксида магния в реакционной смеси с образованием второй реакционной смеси;(c) добавление по меньшей мере одного внутреннего донора электронов либо после этапа (a), либо ...

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20-02-2014 дата публикации

ПОЛИЭТИЛЕН С ВЫСОКОЙ ПРОЧНОСТЬЮ РАСПЛАВА ДЛЯ ИСПОЛЬЗОВАНИЯ В ПЛЕНКАХ

Номер: RU2012134431A
Принадлежит:

... 1. Способ изготовления пленки, особенно хорошо приспособленной для применений пленки, причем указанный способ включает стадии:a) выбор целевой полиэтиленовой смолы, у которой плотность, при определении согласно стандарту ASTM D792, составляет от 0,90 г/смдо 0,955 г/см, и индекс расплава, при определении согласно стандарту ASTM D1238 (2,16 кг, 190°C), составляет от 0,01 г/10 мин до 10 г/10 мин;b) реакция производного алкоксиамина в количестве, составляющем менее чем 900 частей производного на миллион частей суммарной массы полиэтиленовой смолы, с целевой полиэтиленовой смолой в количестве и в условиях, достаточных для увеличения прочности расплава полиэтиленовой смолы; иc) образование пленки, включающей прореагировавшую целевую полиэтиленовую смолу.2. Способ по п.1, в котором производное алкоксиамина соответствует формуле:(R)(R)N-O-R,где каждый из Rи R, независимо друг от друга, представляет собой атом водорода, алкил C-Cили арил C-Cили замещенные углеводородные группы, включающие O и/или ...

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17-12-2018 дата публикации

ПРОИЗВОДСТВО ПОЛИЭТИЛЕНОВЫХ ИЗДЕЛИЙ С УЛУЧШЕННЫМИ ЖЕСТКОСТЬЮ, УДАРНОЙ ВЯЗКОСТЬЮ И ПЕРЕРАБАТЫВАЕМОСТЬЮ

Номер: RU2670755C9

Изобретение относится к этилен/альфа-олефиновым сополимерам. Полимер содержит этилен и по меньшей мере один альфа-олефин с 4-20 атомами углерода. Полимер имеет отношение индекса расплава (ОИР) больше чем приблизительно 40. Полимер также имеет значение Mw1/Mw2 по меньшей мере приблизительно 2,0, где Mw1/Mw2 представляет собой отношение средневесовой молекулярной массы (Мw) для первой половины кривой фракционирования при элюировании с повышением температуры (TREF) из кросс-фракционной хроматографии (CFC) к Mw для второй половины кривой TREF. Полимер также имеет значение Tw1-Tw2 меньше чем приблизительно -15°С, где Tw1-Tw2 представляет собой разницу средневзвешенной температуры элюирования (Tw) для первой половины кривой TREF и Tw для второй половины кривой TREF. Технический результат – получение полимера с улучшенными физическими свойствами. 9 з.п. ф-лы, 8 ил., 10 табл., 10 пр.

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05-11-2019 дата публикации

ПРОПИЛЕН-ПОЛИМЕРНЫЕ КОМПОЗИЦИИ

Номер: RU2697706C9

Изобретение относится к пропиленовой композиции, предназначенной для получения формованных изделий. Композиция содержит А) от 60 до 75 мас.% гомополимера пропилена, имеющего коэффициент полидисперсности (P.I.) от 4,3 до 4,9, фракцию, нерастворимую в ксилоле при 25°C, выше чем 95%, и скорость течения расплава (MFR), составляющую от 20 до 75 г/10 мин, измеренную при 230°С и нагрузке 2,16 кг, и В) от 25 до 40 мас.% сополимера пропилена, содержащего от 46,0 до 49,0 мас.% звеньев, полученных из этилена. Кроме того, композиция имеет характеристическую вязкость фракции, растворимой в ксилоле при 25°C, от 2,2 до 2,9 дл/г и отношение 10,7+1,3xMFRa-17,7xP.I.-29,3xIV+4,9xXs (I), составляющее от 40 до 66, где MFR представляет собой скорость течения расплава компонента А), P.I. представляет собой коэффициент полидисперсности компонента A), IV представляет собой характеристическую вязкость фракции, растворимой в ксилоле при 25°C, а Xs представляет собой растворимую в ксилоле при 25°C фракцию и составляет ...

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21-10-2020 дата публикации

Полипропиленовая композиция

Номер: RU2734641C1
Принадлежит: БОРЕАЛИС АГ (AT)

Изобретение относится к пропиленовым композициям для получения упаковочных материалов и пленок. Предложена полипропиленовая композиция, включающая смесь (А) 50-90 мас.% статистического сополимера пропилена и этилена, имеющего содержание этилена 2-6 мас.%, и (Б) 10-50 мас.% статистического сополимера пропилена и гексена, имеющего содержание гексена 3-7 мас.%, где температура плавления сополимера (Б) меньше температуры плавления сополимера (А). Предложены также способ получения указанной композиции, применение предложенной композиции для получения изделий, выбранных из упаковочных материалов и пленок, и соответствующие изделия. Технический результат - получение материала, обладающего улучшенным балансом между низкой температурой начала сваривания, низкой общей миграцией, хорошими оптическими характеристиками и достаточной термической стойкостью. 4 н. и 10 з.п. ф-лы, 5 табл.

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24-04-2020 дата публикации

СПОСОБ ПОЛУЧЕНИЯ КОМПОЗИЦИИ МУЛЬТИМОДАЛЬНОГО ПОКРЫТИЯ

Номер: RU2720143C1
Принадлежит: БОРЕАЛИС АГ (AT)

Изобретение относится к способу получения металлической трубы с покрытием. Способ включает гомополимеризацию этилена или сополимеризацию этилена и α-олефинового сомономера на первой стадии полимеризации в присутствии катализатора полимеризации с получением первого гомо- или сополимера этилена с плотностью 940-980 кг/ми скоростью течения расплава MFR1-2000 г/10 мин. Затем проводят гомополимеризацию этилена или сополимеризацию этилена и α-олефинового сомономера на второй стадии полимеризации в присутствии первого гомо- или сополимера этилена с получением первой смеси полимера этилена, содержащей первый гомо- или сополимер этилена и второй гомо- или сополимер этилена. Первая смесь полимера этилена имеет плотность 940-980 кг/ми скорость течения расплава MFR10-2000 г/10 мин. На третьей стадии проводят сополимеризацию этилена и α-олефинового сомономера в присутствии первой смеси полимера этилена с получением второй смеси полимера этилена, содержащей первую смесь полимера этилена и третий сополимер ...

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01-10-2020 дата публикации

Полипропиленовая композиция

Номер: RU2733454C1
Принадлежит: БОРЕАЛИС АГ (AT)

Настоящее изобретение относится к полипропиленовой композиции, способу получения полипропиленовой композиции, применению полипропиленовой композиции, изделию и применению изделия. Полипропиленовая композиция включает смесь (А) из тройного пропиленового сополимера (а) от 80,0 до 97,0 масс. %, включающего сомономерные звенья, образованные из этилена, в количестве от 0,3 до 4,0 масс. % и сомономерные звенья, образованные из С-Сα-олефина, в количестве от 4,0 до 16,0 масс. %, и пластомера на основе этилена (б) с плотностью согласно ISO 1183 от 0,850 г/смдо 0,915 г/сми ПТРот 3,0 до 20,0 масс.; и (Б) возможно, одну или более добавок в общем количестве от 0,0 до 5,0 масс. %, исходя из композиции, выбранных из группы, включающей понижающие трение агенты, препятствующие слипанию агенты, УФ-стабилизаторы, альфа- и/или бета-нуклеирующие агенты, антистатики, антиоксиданты. Тройной сополимер имеет показатель текучести расплава (ПТР), измеренный согласно ISO1133 при 230°С, 2,16 кг, от 0,5 до 20,0 г/10 ...

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11-05-2018 дата публикации

СПОСОБ ПОЛИМЕРИЗАЦИИ В ПРИСУТСТВИИ ДОБАВКИ, СНИЖАЮЩЕЙ СТАТИСТИЧЕСКИЕ ЗАРЯДЫ

Номер: RU2653535C1

Изобретение относится к способу получения полиолефинов путем полимеризации олефинов в присутствии катализатора полимеризации. Полимеризацию осуществляют в присутствии добавки, снижающей статические заряды. Добавка, снижающая статический заряд, включает полимер, полученный из алкиленоксида, содержащего в среднем 10-200 повторяющихся звеньев -(CH-CHR-O)-. Полимер, полученный из алкиленоксида, представляет собой статистический сополимер этиленоксида и другие алкиленоксиды. Соотношение n:m повторяющихся звеньев –(CH-CH-O)–, полученных из этиленоксида, к повторяющимся звеньям–(CH-CHR'-O)–, полученным из других алкиленоксидов, составляет 6:1-1:1. Концевые группы полимера, полученного из алкиленоксида, представляют собой группы –OH. Технический результат – предотвращение электростатического заряда и уменьшение образование листового покрытия стенок или отложения полимерных агломератов в реакторе полимеризации. 14 з.п. ф-лы, 1 ил., 1 табл., 4 пр.

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21-05-2018 дата публикации

ПОЛИЭТИЛЕНОВАЯ КОМПОЗИЦИЯ, ОБЛАДАЮЩАЯ ВЫСОКОЙ СТОЙКОСТЬЮ К РАСТРЕСКИВАНИЮ ПОД НАПРЯЖЕНИЕМ

Номер: RU2654479C1

Изобретение относится к полиэтиленовой композиции для изготовления геомембран плоскощелевой экструзией, экструзией с раздувом или ламинированием и способу ее получения. Композиция характеризуется плотностью от 0,930 до 0,945 г/см, отношением MIF/MIP от 10 до менее 30 и значением MIF от 3 до 25 г/10 мин, где MIF представляет собой индекс текучести расплава при 190°С с массой груза 21,60 кг, a MIP представляет собой индекс текучести расплава при 190° С с массой груза 5 кг. При этом композиция имеет значение z-среднего молекулярного веса (Mz) не менее 1500000 г/моль и показатель длинноцепочечной разветвленности (ПДЦР), не превышающий 0,50 при молекулярном весе М, равном 1000000 г/моль. Полученная композиция обладает хорошей технологичностью при обработке и стойкостью к растрескиванию под воздействием окружающей среды. 3 н. и 7 з.п. ф-лы, 1 ил., 1 табл., 2 пр.

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27-09-2018 дата публикации

НОВАЯ СШИТАЯ ПОЛИМЕРНАЯ КОМПОЗИЦИЯ С НИЗКИМ ПТР, ИЗОЛЯЦИЯ СИЛОВОГО КАБЕЛЯ И СИЛОВОЙ КАБЕЛЬ

Номер: RU2668244C1
Принадлежит: Бореалис АГ (AT)

Изобретение относится к сшитой полимерной композиции, ее применению в изоляции силового кабеля и силовому кабелю. Сшитую полимерную композицию получают путем сшивания полимерной композиции, которая имеет показатель текучести расплава (ПТР) менее 1,7 г/10 мин и содержит полиолефин, пероксид и фенольный серосодержащий антиоксидант. Причем сшитая полимерная композиция имеет индукционный период окисления, который соответствует Z мин, и содержит количество пероксидных побочных продуктов, которое соответствует W ч./млн, где 0≤Z≤60, 0≤W≤9500, и W≤p-270⋅Z, и p = 18500. Полимерная композиция содержит менее 0,05 мас.% 2,4-дифенил-4-метил-1-пентена. Обеспечивается полимерная композиция с пониженной проводимостью, подходящая для применений в кабелях постоянного тока высокого напряжения и сверхвысокого напряжения. 5 н. и 11 з.п. ф-лы, 3 табл.

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07-10-2020 дата публикации

СПОСОБ ПОЛУЧЕНИЯ ГОМОПОЛИМЕРОВ ИЛИ СОПОЛИМЕРОВ ЭТИЛЕНА

Номер: RU2733850C1

Изобретение относится к способу получения гомополимеров или сополимеров этилена. Описан способ получения гомополимеров или сополимеров этилена в установке, содержащей трубчатый реактор высокого давления и предварительный нагреватель. Реакционная текучая среда, введенная в реактор, на входе в реактор нагревается в предварительном нагревателе, а средняя скорость реакционной текучей среды в предварительном нагревателе ниже, чем средняя скорость реакционной текучей среды в трубчатом реакторе на входе в реактор. Соотношение средней скорости реакционной текучей среды в трубчатом реакторе к средней скорости реакционной текучей среды в предварительном нагревателе составляет от 1,5:1 до 5:1. Технический результат - получение ПЭНП с более высокой глубиной превращения этилена за реакторный цикл и лучшими оптическими свойствами. 13 з.п. ф-лы, 1 табл., 3 пр., 3 ил.

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29-05-2018 дата публикации

СПОСОБ ПОЛУЧЕНИЯ ПОЛИОЛЕФИНОВ

Номер: RU2016143756A
Принадлежит:

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10-08-2010 дата публикации

СОПОЛИМЕРЫ ЭТИЛЕНА И АЛЬФА-ОЛЕФИНА И СПОСОБЫ ИХ ПОЛИМЕРИЗАЦИИ ДЛЯ ИХ ПОЛУЧЕНИЯ

Номер: RU2009102501A
Принадлежит:

... 1. Способ получения сополимера этилена и альфа-олефина, где способ включает ! контактирование этилена и, по меньшей мере, одного альфа-олефина с металлоценовым катализатором в, по меньшей мере, одном газофазном реакторе при давлении в реакторе от 0,7 до 70 бар и при температуре в реакторе от 20°С до 150°С с получением в ходе полимеризации сополимера этилена и альфа-олефина, где сополимер этилена и альфа-олефина удовлетворяет следующим условиям: ! плотность 0,927 г/см3 или более, ! индекс расплава (I2) от 1 дециграмм/мин до 200 дециграмм/мин, ! соотношение индексов расплава (I21/I2) от 15 до 40, ! молекулярно-массовое распределение Mw/Mn 2-4, ! значение ESCR 500 ч или более в том случае, когда измерение проводят в соответствии со стандартом ASTM 1693/B в 10% растворе Igepal, ! значение Т75-Т25 4 или более, где Т25 представляет собой температуру, при которой получают 25% элюированного полимера, и Т75 представляет собой температуру, при которой получают 75% элюированного полимера, в эксперименте ...

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10-05-2013 дата публикации

МНОГОСЛОЙНАЯ УСАДОЧНАЯ ПЛЕНКА, ОБЛАДАЮЩАЯ ПРЕВОСХОДНОЙ ПРОЗРАЧНОСТЬЮ И ВЕЛИКОЛЕПНОЙ ПРОЧНОСТЬЮ

Номер: RU2011143744A
Принадлежит:

... 1. Многослойная пленочная структура, включающая, по меньшей мере, три слоя, где, по меньшей мере, один слой содержит интерполимер этилена и, по меньшей мере, одного альфа-олефина, отличающаяся тем, что интерполимер имеет среднее значение Mи температуру промежуточного минимума (ложбины) между интерполимерной и высококристаллической фракцией, T, такие, что среднее значение Mдля фракции выше T, определенное по результатам ATREF, деленное на среднее значение Mвсего полимера, определенное по результатам ATREF, (M/M) менее примерно 1,95, и где интерполимер имеет значение CDBI, менее примерно 60%;где пленочная структура включает внутренний слой и два поверхностных слоя, где поверхностные слои содержат интерполимер и где внутренний слой содержит LDPE; игде LDPE имеет индекс расплава, менее 1 г/10 мин.2. Пленочная структура по п.1, где каждый поверхностный слой дополнительно содержит другой термопластичный полимер.3. Пленочная структура по п.1, где указанный интерполимер имеет значение CDBI, менее ...

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04-03-2021 дата публикации

Polymer composition for container closures

Номер: AU2017218977B2
Принадлежит:

Abstract The present invention relates to a polymer composition comprising an ethylene homopolymer and an ethylene copolymer having a comonomer content comprising a comonomer in an amount of at least 0.55 mol% with respect to the total amount of monomer in the ethylene copolymer, wherein the ethylene copolymer has a higher weight average molecular weight than the ethylene homopolymer, the polymer composition has a density in the range of 0.950-0.965 g/cm, a melt flow rate (MFR2) of at least 0.3 g/10 minutes, a weight average molecular weight of at least 100,000 g/mol, a and viscosity at an angular frequency of 0.01 [1/s], n o.o1 of at least 20,000 Pa.s wherein; the polymer composition has an Isothermal Crystallization Half-Time, ICHT which is less than 10 minute at 123 C and a Full Notch Creep Test, FNCT of at least 60 hours.

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07-03-2019 дата публикации

Multimodal polyethylene thin film

Номер: AU2017322196A1
Принадлежит: Davies Collison Cave Pty Ltd

The present invention relates to a reactor system for a multimodal polyethylene polymerization process, comprising; (a) a first reactor; (b) a hydrogen removal unit arranged between the first reactor and a second reactor comprising at least one vessel connected with a depressurization equipment, preferably selected from vacuum pump, compressor, blower, ejector or a combination, thereof, the depressurization equipment allowing to adjust an operating pressure to a pressure in a range of 100 - 200 kPa (abs); (c) the second reactor; and. (d) a third reactor and the use of a film thereof.

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28-02-2019 дата публикации

PRODUCING POLYOLEFIN PRODUCTS

Номер: AU2019200925A1
Принадлежит: Phillips Ormonde Fitzpatrick

Catalyst systems and methods for making and using the same. A method of polymerizing olefins to produce a polyolefin polymer with a multimodal composition distribution, includes 5 contacting ethylene and a comonomer with a catalyst system. The catalyst system includes a first catalyst compound and a second catalyst compound that are co-supported to form a commonly supported catalyst system. The first catalyst compound includes a compound with the general formula (C5HaRIb)(C 5HcR2 d)HfX 2 . The second catalyst compound comprises the following formula: SiR3 2 R4\ Zr X R - SiR 10 4 (A) wherein each R3 or R4 is independently H, a hydrocarbyl group, a substituted hydrocarbyl group, or a heteroatom group, wherein each R3 or R4 may be the same or different, and each X is independently a leaving group selected from a labile hydrocarbyl, a substituted hydrocarbyl, a heteroatom group, or a divalent radical that links to an R group.

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15-09-2016 дата публикации

Method of producing polyethylene and polyethylene thereof

Номер: AU2015217394A1
Принадлежит: Madderns Patent & Trade Mark Attorneys

A system and method of producing polyethylene, including: polymerizing ethylene in presence of a catalyst system in a reactor to form polyethylene, wherein the catalyst system includes a first catalyst and a second catalyst; and adjusting reactor conditions and an amount of the second catalyst fed to the reactor to control melt index (MI), density, and melt flow ratio (MFR) of the polyethylene.

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08-11-2018 дата публикации

Producing polyolefin products

Номер: AU2015217402B2
Принадлежит: Phillips Ormonde Fitzpatrick

Catalyst systems and methods for making and using the same are described. A method includes selecting a catalyst blend using a blend polydispersity index (bPDI) map. The polydispersity map is generated by generating a number of polymers for at least two catalysts. Each polymer is generated at a different hydrogen to ethylene ratio. At least one catalyst generates a higher molecular weight polymer and another catalyst generates a lower molecular weight polymer. A molecular weight for each polymer is measured. The relationship between the molecular weight of the polymers generated by each of the catalysts and the ratio of hydrogen to ethylene is determined. A family of bPDI curves for polymers that would be made using a number of ratios of a blend of the at least two catalysts for each of a number of ratios of hydrogen to ethylene. A ratio for the catalyst blend of the catalysts that generates a polymer having a bPDI that matches a polymer fabrication process is selected, and the product ...

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15-09-2016 дата публикации

Producing polyolefin products

Номер: AU2015217390A1
Принадлежит: Madderns Patent & Trade Mark Attorneys

Catalyst systems and methods for making and using the same. A method of polymerizing olefins to produce a polyolefin polymer with a multimodal composition distribution, includes contacting ethylene and a comonomer with a catalyst system. The catalyst system includes a first catalyst compound and a second catalyst compound that are co-supported to form a commonly supported catalyst system. The first catalyst compound includes a compound with the general formula (C ...

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05-02-2015 дата публикации

Process for the preparation of polypropylene with improved productivity

Номер: AU2013301727A1
Принадлежит:

The present invention relates to a process for the preparation of a polypropylene in a sequential polymerization process comprising a pre-polymerization reactor and at least two polymerization reactors connected in series, wherein the polymerization in the at least two polymerization reactors takes place in the presence of a Ziegler-Natta catalyst, and said Ziegler-Natta catalyst comprises: (a) a pro-catalyst comprising (a1) a compound of a transition metal, (a2) a compound of a metal which metal is selected from one of the groups 1 to 3 of the periodic table (IUPAC), (a3) an internal electron donor, (b) a co-catalyst, and (c) an external donor, wherein said Ziegler-Natta catalyst is present in the pre-polymerization reactor and ethylene (C2) in addition to propylene (C3) is fed to said pre-polymerization reactor in a C2/C3 feed ratio of 0.5 to 10.0 g/kg.

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21-06-2018 дата публикации

High density rotomolding resin

Номер: AU2016366721A1
Принадлежит: Griffith Hack

The present invention provides high density polyethylene resins having good low temperature impact resistance. The resins are suitable for use in rotomolding application for large parts. The resin is a bi- or trimodal resin produced using solution phase polymerization in the presence of a single site catalyst.

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24-07-2000 дата публикации

Thermoplastic polymers modified with siloxane blends

Номер: AU0001629500A
Принадлежит:

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06-06-2017 дата публикации

HETEROGENEOUS ETHYLENE/ALPHA-OLEFIN INTERPOLYMER

Номер: CA0002757282C

An interpolymer of ethylene and at least one alpha-olefin is claimed, wherein the ethylene interpolymer is charac-terized as having an average Mv and a valley temperature between the interpolymer and high crystalline fraction, Thc, such that the average Mv for a fraction above Thc from ATREF divided by average Mv of the whole polymer from ATREF (Mhc/Mp) is less then about 1.95 and wherein the interpolymer has a CDBI of less than 60%. The interpolymer of ethylene and at least one al-pha-olefin can also be characterized as having a high density (HD) fraction and an overall density such that % HD fraction < -2733.3 + 2988.7x + 144111.5 (x - 0.92325)2 where x is the density in grams/cubic centimeter. Fabricated articles comprising the novel interpolymers are also disclosed.

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24-10-2019 дата публикации

TRANSPARENT POLYPROPYLENE COPOLYMER COMPOSITION HAVING IMPACT RESISTANCE

Номер: CA0003096689A1
Принадлежит: ITIP CANADA, INC.

Polypropylene polymer compositions are disclosed that can be formulated to have excellent transparency properties in conjunction with excellent impact resistance properties. The polypropylene polymer compositions are heterophasic compositions containing a first phase polymer combined with a second phase polymer. The first phase polymer is a polypropylene and alpha-olefin copolymer while the second phase polymer is also a polypropylene and alpha-olefin random copolymer. The first phase polymer contains ethylene in an amount less than 5% by weight and is present in an amount greater than the second phase polymer. The second phase polymer has elastomeric properties.

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26-03-2020 дата публикации

POLYETHYLENE COMPOSITION FOR FILMS

Номер: CA3112357A1
Принадлежит:

A polyethylene composition particularly suited for producing blown films, having the following features: 1) density from 0.948 to 0.960 g/cm3; 2) ratio MIF/MIP from 20 to 40; 3) MIF from 6 to less than 15 g/10 min.; 4) HMWcopo index from 0.5 to 3.5; ) long-chain branching index, LCBI, equal to or lower than 0.82; 6) ?0.02 of equal to or less than 150000.

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27-08-2020 дата публикации

POLYETHYLENE HAVING HIGH PRESSURE RESISTANCE AND CROSSLINKED POLYETHYLENE PIPE COMPRISING THE SAME

Номер: CA3123238A1
Принадлежит:

The present invention relates to polyethylene with high pressure resistance and a crosslinked polyethylene pipe comprising same. Polyethylene according to the present invention has a high melt index and high density and exhibits a sufficient crosslinking degree, thereby being able to exhibit excellent strength and pressure resistant properties.

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31-05-2018 дата публикации

POLYETHYLENE COMPOSITION FOR BLOW MOLDING HAVING HIGH STRESS CRACKING RESISTANCE

Номер: CA0003044697A1
Принадлежит: ELAN IP INC.

A polyethylene composition particularly suited for producing blow-molded hollow articles, having the following features: 1) density from greater than 0.952 to 0.957 g/cm3, determined according to ISO 1183-1 at 23°C; 2) ratio MIF/MIP from 12 to 25; 3) MIF from 18 to 40 g/10 min.; 4) ?0.02 from 30,000 to 55,000 Pa.s; 5) long-chain branching index, LCBI, equal to or greater than 0.55; 6) ratio (?0.02/1000)/ LCBI from 55 to 75.

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18-01-2018 дата публикации

SOLID CATALYST FOR THE PREPARATION OF NUCLEATED POLYOLEFINS

Номер: CA0003026181A1
Принадлежит: FETHERSTONHAUGH & CO.

The present invention is directed to solid catalyst particles comprising a Ziegler-Natta catalyst and a polymeric nucleating agent. Further, the present invention is also directed to a process for the preparation of said solid catalyst particles, the use of said solid catalyst particles in a process for the manufacture of a polymer and a polyolefin obtained in the presence of said solid catalyst particles.

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17-05-2018 дата публикации

OLEFIN POLYMERIZATION PROCESS IN A GAS-PHASE REACTOR HAVING THREE OR MORE POLYMERIZATION ZONES

Номер: CA0003043149A1
Принадлежит: OSLER, HOSKIN & HARCOURT LLP

Process for preparing an olefin polymer in the presence of hydrogen in a gas-phase polymerization reactor comprising three or more polymerization zones and at least two thereof are sub-zones of a polymerization unit, in which the growing polymer particles flow downward in a densified form, wherein at least one polymerization zone has a ratio of hydrogen to the sum of olefins which is by a factor of at least 1.5 lower than the ratio of hydrogen to the sum of olefins in the polymerization zone having the highest ratio of hydrogen to the sum of olefins and which is by a factor of at least.5 higher than the ratio of hydrogen to the sum of olefins in the polymerization zone having the lowest ratio of hydrogen to the sum of olefins.

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12-04-2018 дата публикации

PROCATALYST COMPOSITION MADE WITH A COMBINATION OF INTERNAL ELECTRON DONORS

Номер: CA0003038093A1
Принадлежит: GOWLING WLG (CANADA) LLP

A phthalate-free procatalyst composition is disclosed for olefin polymerization that exhibits excellent polymerization activity and response to hydrogen, and can produce a polyolefin exhibiting high stereoregularity, high melt flow rate, and desirable molecular weight distribution. The method for producing the procatalyst composition includes reaction of a magnesium support precursor with a tetravalent titanium halide and a combination of different internal electron donors. The first internal electron donor may comprise one or more substituted phenylene aromatic diester and the second internal electron donor may comprise a polyether, preferably a 1,3-diether. In one embodiment, the support precursor comprises a spherical spray crystalized MgCI2-EtOH adduct.

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06-04-2021 дата публикации

SUPPORTED CATALYSTS COMPRISING TITANIUM AND CHROMIUM

Номер: CA3035255C

A method of preparing a catalyst comprising a) contacting (i) a silica- support, (ii) an oxotitanium compound, (iii) a chromium-containing compound, and (iv) an optional solvent to form a first aqueous mixture comprising a pre-catalyst and a reaction media having from 1 wt.% to 99 wt.% water; b) thermally treating the pre-catalyst by heating to a temperature of from 400 °C to 1000 °C for a time period of from 1 minute to 24 hours to form the catalyst. A method of preparing a catalyst comprising contacting a hydrated support material comprising silica with a chromium-containing compound to form a first aqueous mixture comprising a chrominated support; contacting the first aqueous mixture comprising a chrominated support with a solution comprising (i) a solvent and (ii) an oxotitanium compound to form a second aqueous mixture comprising a pre- catalyst; and thermally treating the pre-catalyst to form the catalyst.

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10-12-2015 дата публикации

POLYMER COMPOSITION FILLED WITH AN INORGANIC FILLER MATERIAL MIXTURE

Номер: CA0002950645A1
Принадлежит:

The present invention relates to a polymer composition comprising at least 20.0 wt.-%, based on the total weight of the polymer composition, of at least one biodegradable polymer resin, from 0.1 to 20.0 wt.-%, based on the total weight of the polymer composition, of at least one polyolefin selected from polyethylene and/or polypropylene and from 5.9 to 60.0 wt.-%, based on the total weight of the polymer composition, of an inorganic filler material dispersed in the at least one polyolefin and the at least one biodegradable polymer resin, a process for the preparation of such a polymer composition, the use of an inorganic filler material for increasing the thermal stability and/or processability of a polymer composition, the use of the polymer composition for the preparation of an article as well as in a process selected from extrusion process, co-extrusion process, blown film extrusion process, cast film extrusion or sheet extrusion process, extrusion coating process, injection molding ...

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21-04-2016 дата публикации

ETHYLENE INTERPOLYMER FILMS

Номер: CA0002909093A1
Принадлежит:

This disclosure relates to multilayer films having improved caulkability. These multilayer films have at least one layer containing an ethylene interpolymer product, or a blend containing an ethylene interpolymer product, where the ethylene interpolymer product has: a Dilution Index (Y d) greater than 0; total catalytic metal 2 3.0 ppm; >= 0.03 terminal vinyl unsaturations per 100 carbon atoms, and; optionally a Dimensionless Modulus (X d) greater than 0. The ethylene interpolymer products have a melt index from about 0.4 to about 100 dg/minute, a density from about 0.950 to about 0.970 g/cm3, a polydispersity (M w/M n) from about 2 to about 25 and a CDBI50 from about 55% to about 97%. Further, the ethylene interpolymer products are a blend of at least two ethylene interpolymers; where one ethylene interpolymer is produced with a single-site catalyst formulation and at least one ethylene interpolymer is produced with a heterogeneous catalyst formulation.

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29-12-2016 дата публикации

POLYETHYLENE COMPOSITION FOR FILMS

Номер: CA0002990500A1
Принадлежит:

A polyethylene composition particularly suited for producing pipes, having the following features: 1) density from 0.945 to 0.958 g/cm3, determined according to ISO 1183 at 23°C; 2) ratio MIF/MIP from 20 to 43; 3) MIF from 4.0 to less than 8.5 g/10 min.; 4) HMWcopo index from 3.5 to 20; 5) long-chain branching index, LCBI, equal to or lower than 0.82.

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15-09-2020 дата публикации

FIBER REINFORCED COMPOSITE

Номер: CA0002989957C
Принадлежит: BOREALIS AG

Fiber reinforced composite comprising a trimodal polypropylene composition.

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29-10-2015 дата публикации

PIPE COMPRISING A METALLOCENE-CATALYZED POLYETHYLENE RESIN

Номер: CA0002946458A1
Принадлежит:

The invention relates to a pipe comprising at least one metallocene-catalyzed polyethylene resin, wherein the polyethylene resin has a multimodal molecular weight distribution and comprises at least two metallocene-catalyzed polyethylene fractions A and B, wherein fractions A and B are prepared in different reactors of at least two reactors connected in series, wherein the polyethylene resin comprises: at least 30% by weight and at most 50% by weight of the polyethylene fraction A, based on the total weight of the polyethylene resin, wherein fraction A has a melt index Ml2 of at least 50 g/10min as determined on the fluff of fraction A according to ISO 1133:1997 condition D at a temperature of 190°C and under a load of 2.16 kg; wherein fraction B has a density of at most 0.9210 g/cm3; and wherein the polyethylene resin has a melt index Ml5 of at least 0.10 g/10min and of at most 1.0 g/10min as determined according to ISO 1 133:1997, condition T, at 190°C and under a load of 5 kg; wherein ...

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20-08-2019 дата публикации

PROCESS FOR PRODUCING HETEROPHASIC COPOLYMERS OF PROPYLENE

Номер: CA0002974878C
Принадлежит: BOREALIS AG

In a preferred embodiment, there is provided a process for producing a heterophasic copolymer, comprising: introducing a solid catalyst component, a cocatalyst, propylene monomer and hydrogen, and producing a first polymer with a first MFR 2 from 0.1 to 2.0 g/10 min.; producing a first polymer mixture of the first polymer and a second propylene polymer, and which has a second MFR 2 from 0.05 to 1.0 g/10 min.; introducing the mixture, propylene monomer and a comonomer having ethylene and/or alpha-olefins, and producing the copolymer having the mixture and a third propylene copolymer, and which has a third MFR 2 from 0.05 to 1.0 g/10 min, and a comonomer unit content from 5 to 25 mole %, wherein a xylene soluble fraction amount is from 14 to 35 weight %, and intrinsic viscosity from 1.5 to 4.4 dl/g, and wherein the catalyst component has the below internal donor: (see above formula) ...

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11-06-2015 дата публикации

POLYPROPYLENE COMPOSITION SUITABLE FOR PRIMERLESS PAINTING

Номер: CA0002931177A1
Принадлежит:

The present invention is directed to a polypropylene composition (C), an article comprising the polypropylene composition (C) as well as the use of the polypropylene composition (C) to reduce paintability failure of a molded article.

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20-08-2015 дата публикации

METHOD OF PRODUCING POLYETHYLENE AND POLYETHYLENE THEREOF

Номер: CA0002938841A1
Принадлежит:

A system and method of producing polyethylene, including: polymerizing ethylene in presence of a catalyst system in a reactor to form polyethylene, wherein the catalyst system includes a first catalyst and a second catalyst; and adjusting reactor conditions and an amount of the second catalyst fed to the reactor to control melt index (MI), density, and melt flow ratio (MFR) of the polyethylene.

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20-08-2015 дата публикации

PRODUCING POLYOLEFIN PRODUCTS

Номер: CA0002938846A1
Принадлежит:

Catalyst systems and methods for making and using the same are described. A method includes selecting a catalyst blend using a blend polydispersity index (bPDI) map. The polydispersity map is generated by generating a number of polymers for at least two catalysts. Each polymer is generated at a different hydrogen to ethylene ratio. At least one catalyst generates a higher molecular weight polymer and another catalyst generates a lower molecular weight polymer. A molecular weight for each polymer is measured. The relationship between the molecular weight of the polymers generated by each of the catalysts and the ratio of hydrogen to ethylene is determined. A family of bPDI curves for polymers that would be made using a number of ratios of a blend of the at least two catalysts for each of a number of ratios of hydrogen to ethylene. A ratio for the catalyst blend of the catalysts that generates a polymer having a bPDI that matches a polymer fabrication process is selected, and the product ...

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15-07-2010 дата публикации

PROCESS FOR PRODUCING BROADER MOLECULAR WEIGHT DISTRIBUTION POLYMERS WITH A REVERSE COMONOMER DISTRIBUTION AND LOW LEVELS OF LONG CHAIN BRANCHES

Номер: CA0002746995A1
Принадлежит:

The present invention provides a polymerization process which is conducted by contacting an olefin monomer and at least one olefin comonomer in the presence of hydrogen and a metallocene-based catalyst composition. Polymers produced from the polymerization process are also provided, and these polymers have a reverse comonomer distribution, low levels of long chain branches, and a ratio of Mw/Mn from about 3 to about 6.

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21-04-2016 дата публикации

SOLUTION POLYMERIZATION PROCESS

Номер: CA0002868640A1
Принадлежит:

This disclosure relates to a continuous solution polymerization process wherein production rate is increased. Process solvent, ethylene, optional comonomers, optional hydrogen and a single site catalyst formulation are injected into a first reactor forming a first ethylene interpolymer. Process solvent, ethylene, optional comonomers, optional hydrogen and a heterogeneous catalyst formulation are injected into a second reactor forming a second ethylene interpolymer. The first and second reactors may be configured in series or parallel modes of operation. Optionally, a third ethylene interpolymer is formed in an optional third reactor, wherein an optional heterogeneous catalyst formulation may be employed. In a solution phase, the first, second and optional third ethylene interpolymers are combined, the catalyst is deactivated, the solution is passivated and following a phase separation process an ethylene interpolymer product is recovered.

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26-10-2021 дата публикации

SOLUTION POLYMERIZATION PROCESS

Номер: CA2868640C

This disclosure relates to a continuous solution polymerization process wherein production rate is increased. Process solvent, ethylene, optional comonomers, optional hydrogen and a single site catalyst formulation are injected into a first reactor forming a first ethylene interpolymer. Process solvent, ethylene, optional comonomers, optional hydrogen and a heterogeneous catalyst formulation are injected into a second reactor forming a second ethylene interpolymer. The first and second reactors may be configured in series or parallel modes of operation. Optionally, a third ethylene interpolymer is formed in an optional third reactor, wherein an optional heterogeneous catalyst formulation may be employed. In a solution phase, the first, second and optional third ethylene interpolymers are combined, the catalyst is deactivated, the solution is passivated and following a phase separation process an ethylene interpolymer product is recovered.

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27-03-2007 дата публикации

INTERPOLYMER COMPOSITIONS AND CAST STRETCH FILM THEREFROM

Номер: CA0002274746C

This invention relates to cast films prepared from interpolymer compositions comprising: (A) a substantially linear ethylene/.alpha.-olefin interpolymer present in the composition in an amount of from 10 to 100 % by weight based on the combined weight of Components A and B; and (B) a heterogeneous interpolymer present in the composition in an amount of from 0 to 90 % by weight based on the combined weight of Components A and B; and wherein said interpolymer composition has an I10/I2 value of < 10.0 and is characterized as having a viscosity at 100 rad/s and a relaxation time (.tau.) which satisfies either of the following relationships: Log(viscosity at 100 rad/s).ltoreq.4.43-0.8 log(I2) or log(.tau.) > -1.2-1.3* log(I2). The interpolymer compositions are useful in cast stretch film manufacture with the resulting cast films having an excellent balance of strength and processability.

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30-09-2019 дата публикации

FIBER-REINFORCED POLYPROPYLENE COMPOSITE

Номер: EA0201990842A1
Автор:
Принадлежит:

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31-10-2019 дата публикации

COMPOSITION FOAMED POLYPROPYLENE

Номер: EA0201991194A1
Автор:
Принадлежит:

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31-10-2018 дата публикации

POLYPROPYLENE COMPOSITION FOR USE IN AUTOMOTIVE INDUSTRY

Номер: EA0201800233A1
Автор:
Принадлежит:

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27-04-2020 дата публикации

FIBER REINFORCED POLYPROPYLENE COMPOSITE

Номер: UA0000121283C2
Принадлежит:

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27-04-2020 дата публикации

POLYPROPYLENE COMPOSITE

Номер: UA0000121238C2
Принадлежит:

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29-11-2019 дата публикации

POLYETHYLENE COMPOSITION FOR PIPES OR BELTS DRIP IRRIGATION

Номер: EA0201990989A1
Автор:
Принадлежит:

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10-06-2020 дата публикации

HIGH FLOW TPO COMPOSITION WITH EXCELLENT BALANCE IN MECHANICAL PROPERTIES FOR AUTOMOTIVE INTERIOR

Номер: UA0000121516C2
Принадлежит:

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03-05-2012 дата публикации

Polyethylene Composition and Finished Products Made Thereof

Номер: US20120108766A1
Принадлежит: BASELL POLYOLEFINE GMBH

Novel polyethylenes having defined molecular weight distribution and LCB structure are devised, for films or mouldings.

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07-06-2012 дата публикации

Process for Producing Broader Molecular Weight Distribution Polymers with a Reverse Comonomer Distribution and Low Levels of Long Chain Branches

Номер: US20120141710A1
Принадлежит: Chevron Phillips Chemical Co LP

The present invention provides a polymerization process which is conducted by contacting an olefin monomer and at least one olefin comonomer in the presence of hydrogen and a metallocene-based catalyst composition. Polymers produced from the polymerization process are also provided, and these polymers have a reverse comonomer distribution, low levels of long chain branches, and a ratio of Mw/Mn from about 3 to about 6.

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20-09-2012 дата публикации

Process for the polymerisation of olefins

Номер: US20120238714A1
Принадлежит: Ineos Commercial Services UK Ltd

The present invention relates to a process for polymerisation of olefins, in particular gas phase polymerisation of olefins, with the aid of a supported chromium oxide based catalyst.

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08-11-2012 дата публикации

Bimodal polyethylene for injection stretch blow moulding applications

Номер: US20120282422A1
Принадлежит: Total Petrochemicals Research Feluy SA

A polyethylene resin having a multimodal molecular weight distribution comprising at least two polyethylene fractions A and B, fraction A being substantially free of comonomer and having a lower weight average molecular weight and a higher density than fraction B, each fraction prepared in different reactors of two reactors connected in series in the presence of a Ziegler-Natta catalyst system, the polyethylene resin having a density of from 0.950 to 0.965 g/cm 3 and a melt index MI2 of from 0.5 to 5 g/10 min.

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08-11-2012 дата публикации

High melt strength polyethylene compositions and methods for making the same

Номер: US20120283390A1
Принадлежит: Dow Brasil SA, Dow Global Technologies LLC

The present invention is a method for increasing the melt strength of a polyethylene resin comprising reacting the polyethylene resin with a free radical generator with a decomposition energy in between −50 kJoule/mole and −250 kJoules/mole and a peak decomposition temperature of less than 280 degree C. The resulting resin has increased melt strength with higher ratio of elongational viscosities at 0.1 to 100 rad/s when compared to substantially similar polyethylene resins which have not been reacted with a free radical generator such as an alkoxy amine derivative.

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21-03-2013 дата публикации

Propylene Polymer Compositions

Номер: US20130072634A1
Принадлежит: Basell Poliolefine Italia Srl

A propylene polymer composition comprising (percent by weight): A) 65%-85% of a propylene copolymer containing from 2.0% to 5.0% of ethylene derived units having MFR L (Melt Flow Rate according to ASTM 1238, condition L, i.e. 230° C. and 2.16 kg load) from 0.5 to 50 g/10 min and a melting temperature Tm ranging from 146° C. to 155° C.; B) 15%-35%, of a copolymer of ethylene and propylene with from 74% to 87%, of ethylene derived units; the composition having the intrinsic viscosity of the fraction soluble in xylene ranging from 0.8 to 1.2 dl/g preferably from 0.9 to 1.1 dl/g.

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27-06-2013 дата публикации

Polypropylene-based terpolymers for films

Номер: US20130165612A1
Принадлежит: Basell Poliolefine Italia Srl

A terpolymer containing propylene, ethylene and an alpha olefins of formula CH2═CHZ wherein Z is an hydrocarbon group having from 2 to 10 carbon atoms wherein: (i) the content of ethylene derived units ranges from 0.5 wt % to 5.0 wt %; (ii) the content of alpha olefin derived units ranges from 1.0 wt % to 5.0 wt %; (iii) the amount (Wt %) of alpha-olefin (C6), the amount (Wt %) of ethylene (C2) and the melting point (Tm) of the terpolymer fulfil the following relation (1) Tm>−(C2+0.8C6)*6+157 (1) (iv) the polydispersity index (P1) ranges from 3 to 8.

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06-02-2014 дата публикации

Sealing material of polypropylene with high melting temperature

Номер: US20140039124A1
Принадлежит: Borealis AG

Polypropylene composition comprising propylene homopolymer (H-PP) and a propylene copolymer (C-PP), said copolmyer comprises (a) a propylene copolymer fraction (A) having a comonomer content of equal or above 1.0 wt.-%, the comomers are C 5 to C 12 α-olefins, and (b) a propylene copolymer action (B) having a comonomer content of 4.0 to 20.0 wt-%, the comomers are C 5 to C 12 α-olefins, wherein further (i) the comonomer content in propylene copolymer fraction (A) is lower compared to the comonomer content in the propylene copolymer fraction (B), (ii) the propylene copolymer (C-PP) has a comonomer content of at least 2.0 wt.-%, the comomers are C 5 to C 12 α-olefins, (iii) the weight ratio [(A)/(B)] of the propylene copolymer fraction (A) to the propylene copolymer fraction (B) is in the range of 20/80 to 80/20, and (iv) the weight ratio [(C-PP)/(H-PP)] of the propylene copolymer (C-PP) to the propylene homopolymer (H-PP) is in the range of 95/5 to 75/25.

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27-03-2014 дата публикации

Propylene-based copolymer, propylene-based copolymer composition, molded product thereof and foamed product thereof, and production process therefor

Номер: US20140088214A1
Принадлежит: Mitsui Chemicals Inc

To provide a propylene-based copolymer and a propylene-based copolymer composition, each of which has a high melt tension because it has a long-chain branched structure, exhibits excellent molding processability during molding, such as inflation molding, extrusion molding, blow molding, injection molding or vacuum forming, and is capable of favorably providing a foamed product having an excellent expansion ratio and excellent cell uniformity in the foaming stage. The propylene-based copolymer (A) of the present invention comprises 50 to 95% by mol of constituent units [i] derived from propylene, 4.9 to 49.9% by mol of constituent units [ii] derived from an α-olefin of 2 to 10 carbon atoms other than propylene and 0.1 to 10% by mol of constituent units [iii] derived from a non-conjugated polyene (with the proviso that the total amount of the constituent units [i], [ii] and [iii] is 100% by mol), and is characterized by satisfying specific requirements (a) and (c).

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05-01-2017 дата публикации

PROCESS FOR PRODUCING ETHYLENE/UNSATURATED CARBOXYLIC ACID COPOLYMER, AND SAID COPOLYMER

Номер: US20170002120A1
Принадлежит:

Provided is a process of effectively producing an ethylene/unsaturated carboxylic acid copolymer having excellent mechanical and thermal properties. A process for producing an ethylene/unsaturated carboxylic acid copolymer comprises: producing an ethylene/unsaturated carboxylic acid ester copolymer from ethylene and unsaturated carboxylic acid ester using a late-transition-metal complex catalyst; and heating the ethylene/unsaturated carboxylic acid ester copolymer at a temperature capable of converting the ester group into a carboxylic acid group, thereby converting into the ethylene/unsaturated carboxylic acid copolymer. 1. A process for producing an ethylene/unsaturated carboxylic acid copolymer comprising a structural unit derived from ethylene and a structural unit derived from unsaturated carboxylic acid , which have been copolymerized randomly and linearly , wherein the process comprises: producing an ethylene/unsaturated carboxylic acid ester copolymer from ethylene and unsaturated carboxylic acid ester using a late-transition-metal complex catalyst; and heating the ethylene/unsaturated carboxylic acid ester copolymer at a temperature capable of converting the ester group into a carboxylic acid group , thereby converting into the ethylene/unsaturated carboxylic acid copolymer2. The process for producing an ethylene/unsaturated carboxylic acid copolymer according to claim 1 , wherein the unsaturated carboxylic acid ester is (meth)acrylic acid ester and the unsaturated carboxylic acid is (meth)acrylic acid.3. The process for producing an ethylene/unsaturated carboxylic acid copolymer according to claim 1 , wherein a temperature of the heating is 150-350° C.5. The process for producing an ethylene/unsaturated carboxylic acid copolymer according to claim 1 , wherein the late-transition-metal complex is a phosphine-phenolate complex or a phosphine-sulfonate complex.6. The process for producing an ethylene/unsaturated carboxylic acid copolymer according to claim 1 ...

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20-01-2022 дата публикации

RAPID ACTIVATION PROCESS AND ACTIVATION TREATMENTS FOR CHROMIUM CATALYSTS FOR PRODUCING HIGH MELT INDEX POLYETHYLENES

Номер: US20220017661A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

Processes for activating chromium polymerization catalysts, which can use lower maximum activation temperatures and shorter activation times than conventional activation methods, and provide polyethylenes with high melt indices, broader molecular weight distributions, and lower long chain branching content. The activation process can comprise heating a supported chromium catalyst in an inert atmosphere to a first temperature (T) for a first hold time (t), followed by allowing the chromium catalyst to attain a second temperature (T) in the inert atmosphere, then contacting the chromium catalyst with an oxidative atmosphere for a second hold time (t), in which Tcan be less than or equal to T. Additional activation treatments and conditioning steps are disclosed which can be used to enhance the melt index potential of Phillips (Cr/silica) catalysts. 1. A process for preparing a supported chromium catalyst , the process comprising:(a) calcining a silicon oxide at a first temperature to provide a calcined silicon oxide comprising siloxane moieties, wherein the first temperature is above 600° C.;(b) contacting the calcined silicon oxide with a chromium composition comprising a chromium source in an anhydrous, aprotic solvent, to form a chromium-treated silicon oxide comprising a residual solvent; and(c) heating the chromium-treated silicon oxide to a second temperature to remove the residual solvent and form the supported chromium catalyst, wherein the second temperature is less than the first temperature.2. The process of claim 1 , wherein the chromium source comprises a compound of chromium(VI).3. The process of claim 1 , wherein the chromium source comprises CrO claim 1 , bis(t-butyl) chromate claim 1 , bis(triphenylsilyl) chromate claim 1 , diarenechromium(0) claim 1 , chromium tris(acetylacetonate) claim 1 , or CrCl.4. The process of claim 3 , wherein the chromium composition comprises CrOdissolved in acetonitrile.5. The process of claim 1 , wherein the supported ...

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11-01-2018 дата публикации

ADHESIVE COMPOSITION

Номер: US20180010023A1
Принадлежит:

The present invention relates to an adhesive composition comprising a. a polyethylene resin (A) which has been grafted with an acid grafting agent and b. an epoxy resin (B) in an amount of 0.01 to 15 wt. % of the adhesive total composition, wherein the adhesive composition is having a MFRof 0.1 to 12 g/10 min. Furthermore, the invention relates to an article, in particular a multilayer pipe, comprising an adhesive layer which comprises said adhesive composition and the use of said adhesive composition for the production of an adhesive layer, in particular of an adhesive layer of a pipe. 1. An adhesive composition comprisinga. a polyethylene resin (A) which has been grafted with an acid grafting agent andb. an epoxy resin (B) in an amount of 0.01 to 15 wt. % of the adhesive total composition,wherein the adhesive composition is having a MFR5 of 0.1 to 12 g/10 min.2. The adhesive composition according to wherein the adhesive composition has a density of 910 to 990 kg/m3.3. The adhesive composition according to wherein the adhesive composition further comprises an elastomeric resin (C).4. The adhesive composition according to wherein the elastomeric resin (C) is present in an amount of 2 to 60 wt. % claim 1 , of the total composition.5. The adhesive composition according to wherein the polyethylene resin (A) has a MFR2 of 0.5 to 20 g/10 min.6. The adhesive composition according to wherein the polyethylene resin (A) has a density of 920 to 970 kg/m3.7. The adhesive composition according to wherein the acid grafting agent is selected from unsaturated carboxylic acids and derivatives thereof.8. The adhesive composition according to wherein the amount of said acid grafting agent is from 0.01 to 3.0 wt. % claim 1 , of the overall composition.9. The adhesive composition according to wherein the epoxy resin (B) is present in an amount of 0.05 to 20 wt. % of the total composition.10. The adhesive composition according to wherein the epoxy resin (B) is a Bisphenol A resin.11. An ...

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10-01-2019 дата публикации

SUPPORTED HYBRID CATALYST SYSTEM FOR ETHYLENE SLURRY POLYMERIZATION AND METHOD FOR PREPARING ETHYLENE POLYMER WITH THE CATALYST SYSTEM

Номер: US20190010256A1
Принадлежит:

The present invention relates to a supported hybrid catalyst system for ethylene slurry polymerization and a method for preparing ethylene polymer therewith. The supported hybrid catalyst system according to the present invention may exhibit high activity during ethylene slurry polymerization, and enables preparation of an ethylene polymer having a narrow molecular weight distribution but excellent processability. 5. The supported hybrid catalyst system for ethylene slurry polymerization according to claim 1 , wherein the supported hybrid catalyst system further comprises one or more cocatalysts selected from the group consisting of compounds represented by the following Chemical Formulas 7 to 9:{'br': None, 'sup': '71', 'sub': 'c', '—[Al(R)—O]—\u2003\u2003[Chemical Formula 7]'}wherein, in Chemical Formula 7,c is an integer of 2 or more; and{'sup': '71', 'claim-text': {'br': None, 'sup': '81', 'sub': '3', 'D(R)\u2003\u2003[Chemical Formula 8]'}, 'each Ris each independently a halogen, or a C1-20 hydrocarbyl or C1-20 hydrocarbyl substituted with a halogen,'}wherein, in Chemical Formula 8,D is aluminum or boron; and{'sup': '81', 'claim-text': {'br': None, 'sup': +', '−, 'sub': '4', '[L—H][Q(E)]\u2003\u2003[Chemical Formula]9'}, 'each Ris independently a halogen, or a C1-20 hydrocarbyl or C1-20 hydrocarbyl group substituted with a halogen,'}wherein, in Chemical Formula 9,L is a neutral Lewis base;[L—H]+ is a Bronsted acid;Q is boron or aluminum in an oxidation state of +3; andeach E is independently a halogen having a hydrogen valence of one or more, or a C6-20 aryl or C1-20 alkyl unsubstituted or substituted with a C1-20 hydrocarbyl, alkoxy, or phenoxy functional group.6. The supported hybrid catalyst system for ethylene slurry polymerization according to claim 5 , wherein the cocatalyst is one or more selected from the group consisting of trimethyl aluminum claim 5 , triethyl aluminum claim 5 , triisopropyl aluminum claim 5 , triisobutyl aluminum claim 5 , ...

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10-01-2019 дата публикации

Ethylene based polymer composition suitable for use in extrusion coating

Номер: US20190010262A1
Принадлежит: SABIC Global Technologies BV

The present invention relates to an ethylene based polymer composition suitable for use in extrusion coating. The present invention also relates to an extrusion coating product comprising such composition and the use of such a composition.

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19-01-2017 дата публикации

CATALYST FOR OLEFIN POLYMERIZATION AND CO-POLYMNERIZATION AND A METHOD FOR OLEFIN POLYMERIZATION AND CO-POLYMERIZATION WITH USING THE SAME

Номер: US20170015770A1
Принадлежит:

The provided is an olefin (co)polymerization catalyst with an excellent catalyst activity, wherein the catalyst component is prepared by using a metallocene compound and titanocene compound or a half-titanocene compound so as to provide polyolefins having a high molecular weight and a low melt index, and also a method for olefin (co)polymerization using said catalyst. 2. The catalyst according to claim 1 , wherein the supporting of the step (1) is conducted by adding a solution obtained by dissolving the metallocene compound together with the titanocene compound or half-titanocene compound in aluminoxane solution to a support slurry claim 1 , and stirring the mixture.3. The catalyst according to claim 1 , wherein the supporting of the step (1) is conducted by adding aluminoxane to a support slurry and stirring the mixture so as to obtain an aluminoxane supported support slurry claim 1 , and adding thereto the metallocene compound and the titanocene compound or half-titanocene compound and stirring the mixture.4. The catalyst according to claim 1 , wherein the support is silica having the average particle size of 10-250 μm; micropores of which average diameter is 50-500 Å and volume is 0.1-10 ml/g; and the surface area of 5-1000 m/g.5. The catalyst according to claim 1 , wherein the aluminoxane is selected from linear aluminoxane oligomers and cyclic aluminoxane oligomers.6. A method for polymerizing olefins or copolymerizing olefin with comonomer(s) by using a catalyst according to any one of to . The present invention relates to a catalyst for olefin (co)polymerization and a method for olefin (co)polymerization using the same. Specifically, the present invention relates to an olefin (co)polymerization catalyst with an excellent catalyst activity, wherein the catalyst component is prepared by using a metallocene compound and titanocene compound or a half-titanocene compound so as to provide a polyolefin having a high molecular weight and a low melt index, and to a ...

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19-01-2017 дата публикации

VINYLIDENE FLUORIDE COPOLYMER AND PREPARATION METHOD THEREFOR

Номер: US20170015771A1
Принадлежит:

Provided in the present invention is a vinylidene fluoride copolymer. Same is acquired via a polymerization reaction taking place at conditions of 30-100° C. and 2-7 MPa with vinylidene fluoride, tetrafluoroethylene, and perfluorinated dioxole or C1-4 alkoxy-substituted perfluorinated dioxole as raw materials, with an initiator added into an emulsion consisting of water, fluorinated emulsifier, a chain transfer agent, a pH regulator, and an antifouling agent, and then via steps of separation, purification, refinement, condensation, washing, drying, and granulation, where the molar ratio of vinylidene fluoride, tetrafluoroethylene, and perfluorinated dioxole or C1-4 alkoxy-substituted perfluorinated dioxole is 13-17:2-4:1-3. The vinylidene fluoride copolymer of the present invention provides excellent transparency, flexibility, and solubility, is widely applicable in optical apparatus such as lenses, and is for use in specialty films in the fields of solar panels and of capacitors as a fuel cell membrane, a transparent and tough coating, and a large-sized blown object. 1. A vinylidene fluoride copolymer , wherein the vinylidene fluoride copolymer is synthesized by polymerizing vinylidene fluoride , tetrafluoroethylene , and perfluorinated dioxole or C1-4 alkoxy-substituted perfluorinated dioxole in a molar ratio of 13-17:2-4:1-3.2. The vinylidene fluoride copolymer of claim 1 , wherein the C1-4 alkoxy-substituted perfluorinated dioxole is perfluorinated dimethyl dioxole.3. The vinylidene fluoride copolymer of claim 1 , wherein the vinylidene fluoride copolymer has a melt point in a range of 100-150° C. claim 1 , and has a melt flow index of 0-60 g/10 min claim 1 , preferably 2.1-10 g/10 min claim 1 , at a temperature of 230° C. and under a load of 5 kg.4. A preparation method of the vinylidene fluoride copolymer of claim 3 , wherein the vinylidene fluoride copolymer is prepared by performing a polymerization reaction by using vinylidene fluoride claim 3 , ...

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18-01-2018 дата публикации

LOW DENSITY POLYETHYLENE COPOLYMER HAVING EXCELLENT FILM PROCESSABILITY AND TRANSPARENCY

Номер: US20180016372A1
Принадлежит: LG CHEM, LTD.

The low density polyethylene copolymer according to the present invention is characterized in that as LCB (Long Chain Branch) is introduced into LLDPE, the melt strength is remarkably high even without blending with LDPE, and thus it can be advantageously applied to blown film processing and the like. 1. A low density polyethylene copolymer which satisfies the following conditions:a melt index (MI) of 0.5 to 1.5 g/10 min as measured according to ASTM D1238 (2.16 kg, 190° C.),{'sup': '3', 'a density 0.910 to 0.930 g/cmas measured according to ASTM D792,'}a weight average molecular weight of 91,000 to 150,000, anda melt strength (MS) of 40 to 100 mN.2. The low density polyethylene copolymer according to claim 1 ,{'sub': 0', '500, 'wherein the low density polyethylene copolymer has η(zero shear viscosity) of 140,000 P (poise) or more, and η(viscosity measured at 500 rad/s) of 7,000 P (Poise) or less.'}3. The low density polyethylene copolymer according to claim 1 ,wherein the low density polyethylene copolymer has Mz (Z-average molecular weight) of 220,000 to 380,000.5. The low density polyethylene copolymer according to claim 4 , which satisfying the following Mathematical Formula 2:{'br': None, 'sup': 5', '2.8', '0.25', '5', '2.8', '0.25, 'sub': M', 'M, '(1.6×(Mz/10)+26×(α)) Подробнее

17-01-2019 дата публикации

GAS PHASE POLYMERISATION OF ETHYLENE

Номер: US20190016831A1
Принадлежит:

The invention relates to a process for the production of polyethylene by gas phase polymerisation of ethylene in the presence of a supported chromium oxide based catalyst which is modified with an amino alcohol wherein the molar ratio of amino alcohol:chromium ranges between 0.5:1 and 1.5:1 wherein the support is silica having a surface area (SA) between 250 m2/g and 400 m2/g and a pore volume (PV) between 1.1 cm3/g and less than 2.0 cm3/g. 1. A process for the production of polyethylene by gas phase polymerisation of ethylene in the presence of a supported chromium oxide based catalyst composition which is modified with an amino alcohol wherein the molar ratio of amino alcohol:chromium ranges between 0.5:1 and 1.5:1 , wherein the support is silica having a surface area (SA) between ≥450 m/g and ≤550 m/g and a pore volume (PV) between ≥1.7 cm/g and ≤2.0 cm/g and wherein the catalyst comprises a titanium compound.2. The process according to characterised in that the amount of chromium in the supported catalyst is ≥0.1% by weight and ≤0.5% by weight.3. The process according to claim 1 , characterised in that the molar ratio of amino alcohol:chromium ranges between 0.7:1 and 1.5:1.4. The process according to claim 1 , characterised in that the molar ratio of amino alcohol:chromium ranges between 1:1 and 1.3:1.6. The process according to characterised in that the amino alcohol is 4-(cyclohexylamino) pentan-2-ol or 4-[(2-methylcyclohexyl) amino]pentan-2-ol.7. The process according to claim 1 , characterised in that the titanium compound a compound according to the formulas Ti (OR)Xand Ti (R)X claim 1 , wherein{'sup': 1', '2, 'sub': 1', '20', '1', '20', '1', '20, 'Rand Rrepresent an (C-C) alkyl group, (C-C) aryl group or (C-C) cycloalkyl group,'}X represents a halogen atom, andn represents a number satisfying 0≥n≤4.8. Polyethylene obtained with the process according to claim 1 , characterised in that the polyethylene hasa high-load melt index (HLMI)≥5 g/10 min and ≤10 g/ ...

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17-01-2019 дата публикации

NON-PHTHALATE CATALYST SYSTEM AND ITS USE IN THE POLYMERIZATION OF OLEFINS

Номер: US20190016832A1
Принадлежит: Braskem America, Inc.

This invention relates to a non-phthalate catalyst system for olefin polymerization. The non-phthalate catalyst system comprises (a) a solid Ziegler-Natta catalyst composition comprising a transition metal, a Group 2 metal, and one or more halogens; and one or more internal electron donor compounds; and (b) one or more external electron donor compounds. 2. The non-phthalate catalyst system of claim 1 , wherein the transition metal is titanium claim 1 , the Group 2 metal is magnesium claim 1 , and the halogen is chloride.3. The non-phthalate catalyst system of claim 1 , wherein the catalyst system further comprises an organoaluminum cocatalyst selected from the group consisting of alkylaluminum claim 1 , alkylaluminum hydride claim 1 , alkylaluminum halide claim 1 , and alkylaluminum alkoxide.5. The non-phthalate catalyst system of claim 4 , wherein the cyclic diester compound is selected from the group consisting of diisobutyl cyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , diethyl 3-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , di-n-propyl 3-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , diisopropyl 3-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , di-n-butyl 3-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , diisobutyl 3-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , dihexyl 3-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , diheptyl 3-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , dioctyl 3-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , di-2-ethylhexyl 3-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , didecyl 3-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , diethyl 4-methylcyclohexane-1 claim 4 ,3-dicarboxylate claim 4 , diisobutyl 4-methylcyclohexane-1 claim 4 ,3-dicarboxylate claim 4 , diethyl 4-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , di-n-propyl 4-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , diisopropyl 4-methylcyclohexane-1 claim 4 ,2-dicarboxylate claim 4 , ...

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16-01-2020 дата публикации

Fiber reinforced polypropylene composite

Номер: US20200017671A1
Принадлежит: Borealis AG

The present invention relates to a new composite comprising glass or carbon fibers and polymer-based fibers as well as to a process for the preparation of the composite and molded articles made from said composite.

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26-01-2017 дата публикации

Process for Forming Polyolefins

Номер: US20170022307A1
Принадлежит: Chevron Phillips Chemical Co LP

Processes of forming polyolefins are described herein. One or more specific embodiments of the processes generally include introducing olefin monomer selected from C 2 -C 3 olefins into a first reaction zone under first polymerization conditions to form a first polyolefin; withdrawing a transfer effluent from the first reaction zone, the transfer effluent including first polyolefin and unreacted olefin monomer; introducing the transfer effluent, a comonomer selected from C 4 -C 8 olefins, and additional olefin monomer to a second reaction zone under second polymerization conditions to form a second reactor product; maintaining an essentially constant comonomer:olefin monomer ratio in the second reaction zone; and withdrawing at least a portion of the second reactor product, wherein the second reactor product includes a bimodal polyolefin.

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26-01-2017 дата публикации

Propylene-Based Impact Copolymers

Номер: US20170022308A1
Принадлежит:

A propylene-based impact copolymer (ICP) and composition including the ICP, the ICP comprising a polypropylene homopolymer and within the range of from 10 wt % to 45 wt % of propylene copolymer based on the weight of the ICP, wherein the copolymer comprises from 20 wt % to 44 wt % ethylene, 1-butene, 1-hexene and/or 1-octene derived units and from 80 to 60 wt % propylene-derived units based on the weight of the propylene copolymer, the propylene-based impact copolymer having a Melt Flow Rate (230° C./2.16 kg) within the range of from 10 g/10 mm to 50 g/10 mm and an Elongation at Break of greater than 70%. 1. A propylene-based impact copolymer (ICP) comprising a polypropylene homopolymer and within the range of from 10 wt % to 45 wt % of propylene copolymer based on the weight of the ICP , wherein the propylene copolymer comprises from 20 wt % to 44 wt % ethylene , 1-butene , 1-hexene and/or 1-octene derived units and from 80 to 56 wt % propylene-derived units based on the weight of the propylene copolymer , the propylene-based impact copolymer having a Melt Flow Rate (230° C./2.16 kg) within the range of from 10 g/10 mm to 50 g/10 mm and an Elongation at Break of greater than 60%.2. The propylene-based impact copolymer of claim 1 , wherein the polypropylene homopolymer forms a continuous phase and the propylene copolymer forms rubber domains having an average size within the range of from 0.40 μm to 0.90 μm.3. The propylene-based impact copolymer of claim 1 , wherein the impact copolymer is reactor grade granules having an average particle size within the range of from 1200 μm to 2800 μm and produced at a rate greater than 30 claim 1 ,000 lbs/hr (13 claim 1 ,620 kg/hr).4. The propylene-based impact copolymer of claim 1 , having a Gloss (60°) within a range of from 40 to 90% (ASTM D523).5. The propylene-based impact copolymer of claim 1 , having a Heat Deflection Temperature within the range of from 70° C. to 125° C.6. The propylene-based impact copolymer of claim 1 ...

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26-01-2017 дата публикации

Lightweight environment-friendly polypropylene composite floor and preparation process thereof

Номер: US20170022388A1
Автор: Mingqi Zhang
Принадлежит: Xinming (lutai) Technology Co Ltd

The present invention provides is a lightweight environment-friendly polypropylene composite floor comprising, from top to bottom: 1) a scratch-resistant coating layer, 2) a super-transparent wear-resistant layer, 3) a decorative layer, 4) a first substrate layer, 5) a second substrate layer, 6) a bottom connective layer, and optionally 7) a back adhesive layer. Also provided is a preparation process of the composite floor.

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24-01-2019 дата публикации

GOLF BALL INCORPORATING AT LEAST ONE LAYER OF PLASTICIZED NEUTRALIZED ACID POLYMER COMPOSITION CONTAINING LOW MOLECULAR WEIGHT ACID WAX(ES) AS SOLE ACID POLYMER COMPONENT AND LOW MOLECULAR WEIGHT NON-ACID WAX(ES) IN THE NON-ACID POLYMER COMPONENT

Номер: US20190022470A1
Принадлежит: ACUSHNET COMPANY

Golf ball comprising layer(s) comprised of plasticized neutralized acid polymer composition consisting of mixture of: (a) low molecular weight acid-containing wax(es); (b) non-acid-polymer(s) including at least one low molecular weight non-acid wax such as high density oxidized polyethylene homopolymers; ethylene maleic anhydride copolymers; polypropylene maleic anhydride copolymers; polypropylene homopolymers; ethylene-vinyl acetate copolymers; high density oxidized homopolymers; oxidized copolymers; polyethylene micronized waxes; polytetrafluoroethylene micronized waxes; emulsifiable low molecular weight non-acid waxes; non-emulsifiable low molecular weight non-acid waxes; and/or chemically modified low molecular weight non-acid waxes; (c) organic acid(s) or salt thereof; and (d) plasticizer(s). Molecular weight of each low molecular weight acid-containing wax is about 500 to 7000, or up to 30,000. Interactions between components (a), (b), (c) and (d) advantageously produce layer of ionomeric material having heat stability, processability, and well-retained durability, adhesion, CoR, compression and softer feel without need for blending high and low molecular weight acid-containing polymer(s). 1. A golf ball comprising at least one layer comprised of a plasticized neutralized acid polymer composition consisting of a mixture of: (a) at least one low molecular weight acid-containing wax; (b) at least one non-acid-polymer , of which at least one is a low molecular weight non-acid wax; (c) at least one organic acid or salt thereof; and (d) at least one plasticizer;wherein each low molecular weight acid-containing wax has a molecular weight of from about 500 to about 30,000;wherein the mixture contains at least 70 percent of neutralized acid groups; andwherein the mixture has a melt flow index of at least 0.5 g/10 min.2. The golf ball of claim 1 , wherein the low molecular weight non-acid wax is selected from the group consisting of: high density oxidized polyethylene ...

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28-01-2021 дата публикации

Methods for Scale-Up From a Pilot Plant to a Larger Production Facility

Номер: US20210024660A1
Принадлежит:

Methods for scale-up from a pilot plant to full production of a bimodal polymer product having a density, melt index, and a melt index ratio are provided herein. The methods provide for adjusting reactor conditions and catalyst ratio of a bimodal catalyst system to optimize the transition from single catalyst to bimodal polymer compositions on a full-scale process plant consistent with pilot plant development. 1. A method for scale-up from a pilot plant to a larger production facility of a bimodal polymer product having a density and a melt index comprising the steps of:producing a bimodal polymer product in a first reactor in a pilot plant with a bimodal catalyst system under a first set of operating conditions, wherein the bimodal catalyst system comprises a first catalyst and a second catalyst and the bimodal polymer product has a bimodal polymer product density and a bimodal polymer product melt index;producing a single catalyst polymer composition in the first reactor in the pilot plant with a single catalyst system under a second set of operating conditions, wherein the single catalyst polymer composition has a single catalyst polymer composition density and a single catalyst polymer composition melt index, and the single catalyst polymer composition is produced in the first reactor before or after the step of producing the bimodal polymer product in the first reactor;producing the single catalyst polymer composition in a second reactor in a full-scale process plant with the single catalyst system, wherein the second set of operating conditions to produce the single catalyst polymer composition are adjusted to provide a third set of operating conditions;determining a fourth set of operating conditions, wherein each operating condition of the fourth set of operating conditions equals a ratio of the operating condition of the third set of operating conditions to the operating condition of the second set of operating conditions and the operating condition of the ...

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28-01-2021 дата публикации

Process for obtaining low volatile plastomers

Номер: US20210024669A1
Принадлежит: Borealis AG

Process for reducing the volatile organic compound content of plastomer having a density of equal to or lower than 883 kg/m3 and—a MFR2 of 100.0 g/l 0 min or lower (ISO 1133 at 2.16 kg load and 190° C.); to below 65 ppm(VOC, VDA277), the process comprising the steps of a) providing raw plastomer in granular form, the raw plastomer having a density of equal to or lower than 883 kg/m3; and a MFR2 of 100.0 g/10 min or lower (ISO 1133 at 2.16 kg load and 190° C.); and a volatile organic compound content (VOC, VDA277) of above 150 ppm, and the granules having an average D50 diameter of 2.5 to 4.5 mm b) subjecting said granular raw plastomer to at least one intensive hydrodynamic regime at a minimum temperature of at least 20° C. and a maximum temperature of 4° C. below the Vicat temperature (10 N, ISO 306) of the granular raw plastomer or 35° C., whatever value is lower, with the temperature measured at the gas inlet to the fast-fluidization regime, c) recovering the granular plastomer.

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02-02-2017 дата публикации

Processes for Preparing Metallocene-Based Catalyst Systems

Номер: US20170029541A1
Принадлежит:

Methods for preparing single and dual metallocene catalyst systems containing an activator-support are disclosed. These methods can include precontacting of the activator-support and an organoaluminum compound, as well as sequential contacting of two different metallocene compounds to form a dual metallocene catalyst system. 17-. (canceled)8. A process to produce a dual metallocene catalyst composition , the process comprising:(a) contacting a first metallocene compound and an organoaluminum compound with a slurry of an activator-support for a first period of time to form a first mixture; and(b) contacting the first mixture with a second metallocene compound for a second period of time to form the dual metallocene catalyst composition.9. The process of claim 8 , wherein:the first metallocene compound is less reactive with the activator-support than the second metallocene compound; anda weight ratio of the first metallocene compound to the second metallocene compound is in a range from about 1:10 to about 10:1.10. The process of claim 8 , wherein:the activator-support comprises sulfated alumina;the first metallocene compound comprises a bridged metallocene compound; andthe second metallocene compound comprises an unbridged metallocene compound.11. The process of claim 8 , wherein:the activator-support comprises a fluorided solid oxide, a sulfated solid oxide, a phosphated solid oxide, or a combination thereof;the organoaluminum compound comprises trimethylaluminum, triethylaluminum, tri-n-propylaluminum, tri-n-butylaluminum, triisobutylaluminum, or any combination thereof;the first metallocene compound comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group; andthe second metallocene compound comprises an unbridged zirconium or hafnium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group.12. The process of claim 8 , wherein an ...

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31-01-2019 дата публикации

POLYOLEFIN FILM WITH IMPROVED TOUGHNESS

Номер: US20190031841A1
Принадлежит: UNIVATION TECHNOLOGIES, LLC

A film formed from a polyethylene copolymer using a reduced chromium oxide catalyst, ethylene monomers and a co-monomer selected from butene monomers or 1-hexene, where the polyethylene copolymer has a density in the range of from about 0.935 to about 0.950 g/cmand an I/Iin a range of about 18.0 to about 30.0. The film formed from the polyethylene copolymer has a dart drop impact (g/m) that significantly greater as compared to a film of the polyethylene copolymer formed using a silyl chromate catalyst in place of the reduced chromium oxide catalyst. A method of making such films is also provided. 1. A film comprising: a polyethylene copolymer formed using a reduced chromium oxide catalyst , ethylene monomers and a co-monomer selected from 1-butene or 1-hexene , the polyethylene copolymer formed with the co-monomer to ethylene monomer mole ratio in a range of about 0.012 to about 0.04 to form the polyethylene copolymer having a density in the range of from about 0.9350 to about 0.950 g/cmand an I/Iin a range of about 18.0 to about 30.0 , wherein the polyethylene copolymer formed using the reduced chromium oxide catalyst provides an improvement in a dart drop impact (g/μm) of the film of 17 percent to 56 percent as compared to a film of the polyethylene copolymer formed using a silyl chromate catalyst in place of the reduced chromium oxide catalyst.2. The film of claim 1 , where the reduced chromium oxide catalyst is reduced with diethylaluminum ethoxide (DEAlE).3. The film of claim 1 , wherein the polyethylene copolymer has a melt index (I) of about 0.4 to about 1.0 g/10 min.4. The film of claim 1 , wherein the polyethylene copolymer has a flow index (I) of about 5.0 to about 25.0 g/10 min.5. The film of claim 1 , wherein the polyethylene copolymer has an I/Iof about 18.0 to about 28.0.6. The film of claim 1 , wherein the film has a dart drop impact of about 10.0 to about 20.0 g/μm.7. The film of claim 1 , wherein the polyethylene copolymer has a Mw≥about 100 claim 1 ...

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31-01-2019 дата публикации

THERMOPLASTIC FORMULATION WITH IMPROVED ADHESION

Номер: US20190031853A1
Принадлежит: SIKA TECHNOLOGY AG

A thermally expandable composition, including at least one polymer P, cross-linkable by peroxide, at least one peroxide, preferably at least one acrylate, at least one blowing agent B, preferably at least one activator for the blowing agent, and at least one epoxide group terminated polymer of the formula (I), 2. Thermally expandable composition according to claim 1 , wherein m has a value of 2.3. Thermally expandable composition according to claim 1 , wherein the blowing agent B comprises azodicarbonamide and/or 4 claim 1 ,4′-oxybis(benzenesulphonyl hydrazide).4. Thermally expandable composition according to claim 1 , wherein the acrylate A comprises dipentaerythritol pentaacrylate and/or trimethylolpropane trimethacrylate.5. Thermally expandable composition according to claim 1 , wherein the polyurethane polymer PU is a reaction product of a polyisocyanate and a polyether polyol and optionally a hydroxyl-functional polybutadiene polyol.6. Thermally expandable composition according to claim 1 , wherein the peroxide comprises di-(2-tert.-butyl-peroxyisopropyl)-benzene.7. Thermally expandable composition according to claim 1 , wherein the polymer P comprises ethylene vinyl acetate and/or ethylene butyl acrylate.81212. Thermally expandable composition according to claim 1 , wherein the polymer P comprises or essentially consists of at least two polymers P and P claim 1 , wherein P exhibits a melt flow index (MFI) of between 100 and 200 g/10 min claim 1 , and P exhibits a melt flow index of between 0.1 and 60 g/10 min claim 1 , wherein MFI is determined by ASTM D1238.10. Baffle and/or reinforcement element for hollow structures claim 1 , wherein the element comprises or essentially consists of a thermally expandable composition according to .11. Baffle and/or reinforcement element of claim 10 , wherein that the element comprises a carrier on which the thermally expandable composition is deposited or attached claim 10 , wherein the carrier is made of a thermoplastic ...

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31-01-2019 дата публикации

HETEROPHASIC PROPYLENE COPOLYMER WITH LOW SHRINKAGE

Номер: US20190031869A1
Принадлежит:

A heterophasic propylene copolymer (HECO) comprising a polypropylene matrix having a melt flow rate MFR(230° C.) in the range of 40 to 120 g/10 min and a comonomer content in the range of 30 to 75 mol-% for the preparation of molded articles with low CLTE. 1. Heterophasic propylene copolymer (HECO) comprising{'sub': '2', '(a) a (semi)crystalline polypropylene (PP) having a melt flow rate MFR(230° C.) measured according to ISO 1133 in the range of 40 to 120 g/10 min; and'}(b) an elastomeric propylene copolymer (ESC) dispersed in said (semi)crystalline polypropylene (PP)wherein said heterophasic propylene copolymer (HECO) has(i) a xylene cold soluble (XCS) fraction in the range of 22 to 64 wt.-%;(ii) a comonomer content in the range of 30.0 to 75.0 mol-%; and{'sub': '2', '(iii) a melt flow rate MFR(230° C.) measured according to ISO 1133 in the range of 15 to70 g/10 min and'}wherein further the intrinsic viscosity (IV) of the xylene cold soluble (XCS) fraction of said heterophasic propylene copolymer (HECO) is in the range of 1.30 to 2.20 dl/g.2. Heterophasic propylene copolymer (HECO) according to claim 1 , wherein the intrinsic viscosity (IV) of the xylene cold insoluble (XCI) fraction of the heterophasic propylene copolymer (HECO) is in the range of 1.05 to 1.45 dl/g.3. Heterophasic propylene copolymer (HECO) according to any one of the preceding claims claim 1 , wherein the xylene cold soluble (XCS) fraction of the heterophasic propylene copolymer (HECO) has a comonomer content claim 1 , preferably ethylene content claim 1 , in the range of 40.0 to 75.0 mol-%.4. Heterophasic propylene copolymer (HECO) according to any one of the preceding claims claim 1 , wherein the comonomers of the heterophasic propylene copolymer (HECO) are ethylene and/or a Cto Cα-olefin and/or the comonomers of the xylene cold soluble (XCS) fraction of the heterophasic propylene copolymer (HECO) are ethylene and/or a Cto Cα-olefin claim 1 , preferably ethylene.8. Heterophasic propylene ...

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30-01-2020 дата публикации

Process for gas-phase polymerization of olefins

Номер: US20200031957A1
Принадлежит: Basell Poliolefine Italia Srl

Process for the preparation of heterophasic propylene copolymer compositions (RAHECO) made from or containing a random propylene copolymer (RACO) and an elastomeric propylene copolymer (BIPO), the process being carried out in a reactor having two interconnected polymerization zones, a riser and a downcomer, wherein growing polymer particles: (a) flow through the first polymerization zone, the riser, under fast fluidization conditions in the presence of propylene and of ethylene or an alpha-olefin having from 4 to 10 carbon atoms, thereby obtaining the random propylene copolymer (RACO); (b) leave the riser and enter the second polymerization zone, the downcomer, through which the growing polymer particles flow downward in a densified form in the presence of propylene and of ethylene or an alpha-olefin having from 4 to 10 carbon atoms, wherein the concentration of ethylene or of the alpha-olefin in the downcomer is higher than in the riser, thereby obtaining the elastomeric propylene copolymer (BIPO); and (c) leave the downcomer and are reintroduced into the riser, thereby establishing a circulation of polymer between the riser and the downcomer.

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30-01-2020 дата публикации

Process for producing a coated pipe

Номер: US20200032095A1
Принадлежит: Borealis AG

The present invention deals with a process for producing a coated pipe. The process comprises (i) homopolymerising ethylene or copolymerising ethylene and an α-olefin comonomer in a first polymerisation step in the presence of a polymerisation catalyst to produce a first ethylene homo- or copolymer having a density of from 940 to 980 kg/m 3 and a melt flow rate MFR 2 of from 1 to 2000 g/10 min; (ii) homopolymerising ethylene or copolymerising ethylene and an α-olefin comonomer in a second polymerisation step in the presence of a first ethylene homo- or copolymer to produce a first ethylene polymer mixture comprising the first ethylene homo- or copolymer and a second ethylene homo- or copolymer, said first ethylene polymer mixture having a density of from 940 to 980 kg/m 3 and a melt flow rate MFR 2 of from 10 to 2000 g/10 min; (iii) copolymerising ethylene and an α-olefin comonomer in a third polymerisation step in the presence of the first ethylene polymer mixture to produce a second ethylene polymer mixture comprising the first ethylene polymer mixture and a third ethylene copolymer, said second ethylene polymer mixture having a density of from 915 to 965 kg/m 3 , preferably from 930 to 955 kg/m 3 and a melt flow rate MFR 5 of from 0.2 to 10 g/10 min; (iv) providing a pipe having an outer surface layer; (v) applying a coating composition onto the pipe outer surface layer to form a top coat layer, wherein the coating composition comprises the second ethylene polymer mixture.

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09-02-2017 дата публикации

PROCESS FOR MAKING A STABILIZED FABRICATED ARTICLE FROM POLYOLEFIN

Номер: US20170037160A1
Принадлежит:

A process for preparing a stabilized fabricated article from a polyolefin resin, the process includes incorporating functional groups in the polyolefin resin thereby yielding a polyolefin resin having crosslinkable functional groups. The polyolefin resin having crosslinkable functional groups is converted to a fabricated article. The fabricated article is chemically crosslinked thereby yielding a crosslinked fabricated article. The crosslinked fabricated article is stabilized in an oxidizing environment at an elevated temperature. The stabilized fabricated article thus produced can be prepared as a carbonaceous article by heating the stabilized fabricated article in an inert environment. 1. A process for producing a stabilized fabricated article , the process comprising:(a) providing a polyolefin resin having crosslinkable functional groups;(b) converting the polyolefin resin to a fabricated article;(c) crosslinking at least a portion of the crosslinkable functional groups to yield a crosslinked fabricated article; and(d) heating the crosslinked fabricated article in an oxidizing environment to yield the stabilized fabricated article.2. The process of claim 1 , wherein the polyolefin resin of step (a) has at least 0.1 mol % crosslinkable functional groups.3. The process of claim 1 , wherein a chemical agent is used in step (c) to crosslink the crosslinkable functional groups.4. The process of claim 1 , wherein step (c) further comprises heating the fabricated article to a temperature at or below 160° C.5. The process of claim 1 , wherein irradiation is not used in step (c) to crosslink the crosslinkable functional groups.6. The process of claim 1 , wherein step (d) comprises heating the crosslinked fabricated article at or above 160° C.7. The process of claim 1 , wherein the oxidizing environment of step (d) is air.8. The process of claim 1 , wherein step (b) comprises converting said polyolefin resin to a fabricated article by fiber spinning claim 1 , film ...

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09-02-2017 дата публикации

NEW CATALYST SYSTEM FOR PRODUCING POLYETHYLENE COPOLYMERS IN A HIGH TEMPERATURE SOLUTION POLYMERIZATION PROCESS

Номер: US20170037164A1
Принадлежит:

Catalyst system for producing ethylene copolymers in a high temperature solution process, the catalyst system comprising (i) a metallocene complex of formula (I) wherein M is Hf X is a sigma ligand, L is a bridge of the formula —SiR—, wherein each Ris independently a C-C-hydrocarbyl, tri(C-C-alkyl)silyl, C-C-aryl, C-C-arylalkyl or C-C-alkylaryl n is 0, 1 or 2 Rand R are the same or can be different and can be a linear or branched C-C-alkyl group, Rand R are the same or are different and are a CH—Rgroup, with Rbeing H or linear or branched C-C-alkyl group Rand R are the same or are different and can be H or a linear or branched C-C-alkyl group or a OR group, wherein R is a C-C-alkyl group Rand R are the same or are different and can be H or a C(R)group, with Rbeing the same or different and Rcan be H or a linear or branched C-C-alkyl group or Rand Rand/or R and R taken together form an unsubstituted 4-7 membered ring condensed to the benzene ring of the indenyl moiety, and Rand R can be the same or are different and can be H or a linear or branched C-C-alkyl group (ii) an aluminoxane cocatalyst and/or (iii) a boron containing cocatalyst and (iv) optionally an aluminium alkyl compound. 2. Catalyst system according to claim 1 , wherein in the formula (I)M is Hf,{'sup': 11', '11', '11', '11', '11', '11', '11', '11', '11', '11, 'sub': 2', '3', '2', '2', '1', '20', '2', '20', '2', '20', '6', '20', '7', '20', '7', '20', '3', '2', '2, 'X which may be the same or different, and is a hydrogen atom, a halogen atom, a R, OR, OSOCF, OCOR, SR, NRor PRgroup, wherein Ris a linear or branched, cyclic or acyclic, C-C-alkyl, C-C-alkenyl, C-C-alkynyl, C-C-aryl, C-C-alkylaryl or C-C-arylalkyl radical; optionally containing heteroatoms belonging to groups 14-16 or is SiR, SiHRor SiHR,'}{'sup': 8', '8, 'sub': 2', '1', '10', '6', '10, 'L is a bridge of the formula —SiR—, wherein both Rare the same C-C-hydrocarbyl or C-C-aryl group,'}{'sup': 1', '1′, 'sub': 1', '6, 'Rand R are the same and ...

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09-02-2017 дата публикации

DILUTION INDEX

Номер: US20170037230A1
Принадлежит: NOVA CHEMICALS (INTERNATIONAL) S.A.

This disclosure relates to ethylene interpolymer compositions. Specifically, ethylene interpolymer products having: a Dilution Index (Y) greater than 0; total catalytic metal ≧3.0 ppm; ≧0.03 terminal vinyl unsaturations per 100 carbon atoms, and; optionally a Dimensionless Modulus (X) greater than 0. The disclosed ethylene interpolymer products have a melt index from about 0.3 to about 500 dg/minute, a density from about 0.869 to about 0.975 g/cm, a polydispersity (M/M) from about 2 to about 25 and a CDBIfrom about 20% to about 97%. Further, the ethylene interpolymer products are a blend of at least two ethylene interpolymers; where one ethylene interpolymer is produced with a single-site catalyst formulation and at least one ethylene interpolymer is produced with a heterogeneous catalyst formulation. 1102-. (canceled)104. The ethylene interpolymer product of claim 103 , wherein said single site catalyst formulation further comprises: an alumoxane co-catalyst; a boron ionic activator claim 103 , and; optionally a hindered phenol.105. The ethylene interpolymer product of claim 104 , wherein said alumoxane co-catalyst is methylalumoxane (MAO) and said boron ionic activator is trityl tetrakis (pentafluoro-phenyl) borate.106. The ethylene interpolymer product of claim 103 , further characterized as having one or more of:a) ≧0.03 terminal vinyl unsaturations per 100 carbon atoms;b) ≧3 parts per million (ppm) of a total catalytic metal;c) a Dimensionless Modulus, Xd, greater than 0.107. The ethylene interpolymer product of having a melt index from about 0.3 to about 500 dg/minute; wherein melt index is measured according to ASTM D1238 (2.16 kg load and 190° C.)108. The ethylene interpolymer product of having a density from about 0.869 to about 0.975 g/cc; wherein density is measured according to ASTM D792.109. The ethylene interpolymer product of having a M/Mfrom about 2 to about 25.110. The ethylene interpolymer product of having a CDBIfrom about 20% to about 98%.111. ...

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24-02-2022 дата публикации

Olefin-based elastomer composite resin composition for airbag chute, comprising dendrimer

Номер: US20220056254A1
Принадлежит: Cepla Co Ltd

A polyolefin thermoplastic elastomer composition for an airbag chute, includes a polypropylene, an olefin block copolymer, and a dendrimer as a material applied to a raw material of a passenger airbag chute. An olefin elastomer composite resin composition for an airbag chute includes 30-80 parts by weight of a polypropylene resin, 30-70 parts by weight of an olefin block copolymer, and 0.1-5 parts by weight of a dendrimer based on 100 parts by weight of the olefin elastomer composite resin composition. The olefin elastomer composite resin composition for an airbag chute, improves the dispersion of the elastomer by applying a high-flow elastomer and a low-flow polypropylene, and improves flowability and meltability characteristics without deteriorating physical properties by applying the dendrimer.

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15-02-2018 дата публикации

Polymers with Improved Processability for Pipe Applications

Номер: US20180044454A1
Принадлежит: Chevron Phillips Chemical Co LP

A crosslinked metallocene-catalyzed polyethylene copolymer having a higher molecular weight (HMW) component and lower molecular weight (LMW) component wherein the HMW component is present in an amount of from about 10 wt. % to about 30 wt. % and wherein the LMW component is present in an amount of from about 70 wt. % to about 90 wt. %.

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15-02-2018 дата публикации

Compound composition for vehicle interior material using natural fiber

Номер: US20180044512A1

Disclosed herein is a compound composition for a vehicle interior material using a natural fiber, which has use for enhancing physical properties, such as shock resistance, tensile strength, flexural strength, elongation, flexural modulus of elasticity, and heat deflection temperature, while realizing a reduction in weight of a vehicle. The compound composition is composed of a base resin obtained by mixing a high-fluidity polypropylene resin and a high-impact polypropylene resin, the base resin being a thermoplastic resin, a reinforcing filler that is a lightweight, eco-friendly, and low-density natural fiber, an impact modifier that is ethylene-propylene-octene rubber, an inorganic filler that functions as a nuclear agent, and a maleic-anhydride compatibilizer.

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03-03-2022 дата публикации

Catalyst for Olefin Polymerization and Polyolefin Prepared Using the Same

Номер: US20220064344A1
Принадлежит: Hanwha Solutions Corp

The present invention relates to a catalyst for olefin polymerization. Specifically, the present invention relates to a hybrid catalyst, which is capable of preparing a polyolefin, particularly a linear low-density polyethylene, which has excellent processability and is capable of providing a film having good mechanical and optical properties.

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25-02-2016 дата публикации

Polypropylene composition with improved impact resistance for pipe applications

Номер: US20160053034A1

The present invention relates to a polypropylene composition comprising a multimodal propylene random copolymer with at least one comonomer selected from alpha-olefins with 2 or 4 to 8 carbon atoms, wherein the polypropylene composition has a melt flow rate MFR 2 (2.16 kg, 230° C.) of 0.05 to 1.0 g/10 min, determined according to ISO 1133, a polydispersity index (PI) of 2.0 to 7.0, and a Charpy Notched Impact Strength at 0° C. of more than 4.0 kJ/m 2 , determined according to ISO 179/1eA:2000 using notched injection moulded specimens, a process for producing said polypropylene composition, an article comprising said polypropylene composition and the use of said polypropylene composition for the production of an article.

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25-02-2021 дата публикации

Mixed Catalyst Systems Containing Bridged Metallocenes with a Pendant Group 13 Element, Processes for Making a Polymer Product Using Same, and Products Made from Same

Номер: US20210054111A1
Принадлежит:

A mixed metallocene catalyst system can comprise at least one metallocene catalyst compound comprising a structure represented by formula (A) below and optionally at least one other metallocene catalyst compound having a structure represented by formula (B) below: 1. A polymer product made from an alpha-olefin feed comprising ethylene (C) monomer and a Cto Calpha-olefin comonomer , wherein the polymer product exhibits:an Mn, as measured by GPC, from 7,000 g/mol to 70,000 g/mol;a PDI, as measured by GPC, from 4.1 to 11.0;a reversed-co-monomer index (RCI,m) of at least 200 kg/mol; anda comonomer distribution ratio (CDR2,m) of at least 2.0.2. The polymer product of claim 1 , further exhibiting claim 1 , as measured by GPC claim 1 , an average content of polymerized Cto Calpha-olefin comonomer claim 1 , relative to a total content of alpha-olefin monomers and comonomers polymerized in the polymer product claim 1 , that increases for each quartile of increasing MWD of the polymer product.3. The polymer product of claim 1 , further exhibiting a melt index ratio (MIR) from 35 to 100.4. The polymer product of claim 1 , further exhibiting claim 1 , according to cross-fractionation chromatography (CFC):a (Tw1-Tw2) value between −30° C. and −36° C., a Tw2 of at least 90° C., an Mw1/Mw2 value of at least 0.9, or a combination thereof; andan Mw1/Mw2 value less than or equal to [0.6*(Tw1-Tw2)]−17. This application is a divisional of U.S. Ser. No. 16/250,624, filed Jan. 17, 2019 which claims priority to and the benefit of U.S. Ser. No. 62/624,558, filed Jan. 31, 2018 and is incorporated by reference in its entirety.This application also claims priority to and the benefit of U.S. Ser. No. 62/624,549, filed Jan. 31, 2018 and is incorporated by reference in its entirety.The present disclosure relates to mixed metallocene catalyst systems comprising a first metallocene catalyst compound comprising first and second cyclopentadienyl rings connected by a bridging group (BG) and a second ...

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25-02-2021 дата публикации

Metallocene Catalyst System for Producing LLDPE Copolymers With Tear Resistance and Low Haze

Номер: US20210054178A1
Принадлежит: Chevron Phillips Chemical Co LP

Ethylene polymers having a density from 0.908 to 0.925 g/cm3, a melt index from 0.5 to 3 g/10 min, a ratio of Mw/Mn from 2 to 4, a ratio of Mz/Mw from 1.6 to 2.3, a CY-a parameter from 0.45 to 0.6, and an ATREF profile characterized by a single peak at a peak ATREF temperature from 76 to 88° C., and by less than 4.5 wt. % of the polymer eluting above a temperature of 91° C. These ethylene polymers can be used to produce various articles of manufacture, such as blown and cast films with a beneficial combination of high tear resistance and low haze.

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21-02-2019 дата публикации

HETEROPHASIC PROPYLENE COPOLYMERS

Номер: US20190055333A1
Принадлежит: BASELL POLIOLEFINE ITALIA S.R.L.

A polypropylene composition made from or containing: 1. A polypropylene composition comprising:A) from about 50 wt % to about 90 wt %; of a propylene homopolymer having a fraction insoluble in xylene at 25° C., higher than about 90%; and a MFR L (Melt Flow Rate according to ISO 1133, condition L, at 230° C. and 2.16 kg load) from about 0.5 to about 200 g/10 min;B) from about 10 wt % to about 50 wt %; of a copolymer of propylene and ethylene having from about 30.0 wt % to about 70.0 wt %, of ethylene derived units, based upon the total weight of the copolymer;the sum of the amount of component A) and B) being 100;the polypropylene composition having:i) an intrinsic viscosity of the fraction soluble in xylene at 25° C. between about 2.2 to about 4.0 dl/g;ii) a MFR L (Melt Flow Rate according to ISO 1133, condition L, at 230° C. and 2.16 kg load) from about 0.5 to about 100 g/10 min;iii) a xylene soluble fraction ranging from about 20 wt % to about 50 wt %, based upon the total weight of the polypropylene composition;wherein the polypropylene composition being obtained by a two steps polymerization process comprising the steps of:step a) polymerizing propylene to obtain component A) in the presence of a catalyst comprising the product of a reaction between:a) a solid catalyst component comprising Ti, Mg, Cl, and an internal electron donor compound containing from about 0.1 to about 50% wt of Bi with respect to the total weight of the solid catalyst component;b) an alkylaluminum compound and,c) an electron-donor compound (external donor); andstep b) polymerizing propylene and ethylene to obtain component B) in the presence of the polymerization product of step a).2. The polypropylene composition according to wherein component A) ranges from about 60 wt % to about 85 wt %; and component B) ranges from about 15 wt % to about 40 wt %.3. The polypropylene composition according to wherein component B) contains from about 35.0 wt % to about 60.0 wt % of ethylene derived units ...

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01-03-2018 дата публикации

PROCESS FOR FORMING POLYOLEFINS

Номер: US20180057623A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

Processes of forming polyolefins are described herein. One or more specific embodiments of the processes generally include introducing olefin monomer selected from C-Colefins into a first reaction zone under first polymerization conditions to form a first polyolefin; withdrawing a transfer effluent from the first reaction zone, the transfer effluent including first polyolefin and unreacted olefin monomer; introducing the transfer effluent, a comonomer selected from C-Colefins, and additional olefin monomer to a second reaction zone under second polymerization conditions to form a second reactor product; maintaining an essentially constant comonomer:olefin monomer ratio in the second reaction zone; and withdrawing at least a portion of the second reactor product, wherein the second reactor product includes a bimodal polyolefin. 131.-. (canceled).32. A process of forming polyolefins comprising:{'sub': 2', '3, 'introducing olefin monomer selected from C-Colefins into a first reaction zone under first polymerization conditions to form a first polyolefin;'}withdrawing a transfer effluent from the first reaction zone, the transfer effluent comprising first polyolefin and unreacted olefin monomer;{'sub': 4', '8, 'introducing the transfer effluent, a comonomer selected from C-Colefins, and additional olefin monomer to a second reaction zone under second polymerization conditions to form a second reactor product;'}maintaining an essentially constant comonomer:olefin monomer ratio in the second reaction zone; andwithdrawing at least a portion of the second reactor product, wherein the second reactor product comprises a bimodal polyolefin,wherein the first reaction zone and second reaction zone are connected in series, the first reaction zone comprises one or more loop slurry reaction vessels, and the second reaction zone comprises a gas phase reactor.331. The process of claim , further comprising introducing hydrogen or a first comonomer into the first reaction zone under the ...

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01-03-2018 дата публикации

Polypropylene foams and processes of making

Номер: US20180057651A1
Автор: Chiang Hsiang Lin
Принадлежит: LCY Chemical Corp

The present disclosure provides a linear polypropylene foam with, for example, low density and/or high expansion ratio, said linear polypropylene foam comprising at least one polypropylene, at least one alpha nucleating agent, and at least one beta nucleating agent. The present disclosure also provides compositions and processes for making said linear polypropylene foam.

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02-03-2017 дата публикации

PROCESS FOR THE POLYMERISATION OF OLEFINS

Номер: US20170058064A1
Принадлежит:

The present invention relates to a process for polymerisation of olefins, in particular gas phase polymerisation of olefins, with the aid of a supported chromium oxide based catalyst. 114-. (canceled)16. Process according to wherein the refractory oxide support for the chromium oxide based catalyst used in the process of the present invention is spherical and/or spheroidal.17. Process according to wherein the spherical and/or spheroidal refractory oxide support consists of silica.18. Process according to wherein the chromium oxide based catalyst contains 0.3 to 2% by weight of chromium.19. Process according to wherein the chromium oxide based catalyst contains between 0.5 and 5% by weight of titanium.20. Process according to wherein the holding time during the first thermal treatment is less than or equal to 6 hours and/or said holding time is at least 30 minutes.21. Process according to wherein the temperature described in the first thermal treatment step is at least 650° C.; and/or said temperature is less than or equal to 850° C.22. Process according to wherein the second step has a holding time of at least 3 hours; and/or said holding time is less than or equal to 9 hours.23. Process according to wherein the range of temperatures descried in the second step is comprised between 500 and 700° C.24. Process according to wherein the difference between the maximum temperature of step 1 and the maximum temperature of step 2 is comprised between 50 and 200° C.25. Process according to wherein step 1 is performed under nitrogen.26. Process according to wherein the total duration of any thermal treatment (non oxidising steps) above 300° C. of the titanium modified supported chromium oxide based catalyst is less than 24 hours.27. Process according to which is a process for the gas phase polymerisation of at least one alpha olefin.28. Process according to wherein ethylene is copolymerised with one or more C3 to C8 olefins.29. Process according to wherein the oxidising ...

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27-02-2020 дата публикации

Process for obtaining low volatile plastomers

Номер: US20200062876A1
Принадлежит: Borealis AG

A process for reducing the volatile organic compound content of granular plastomers having a density of equal to or lower than 883 kg/m3 and a MFR2 of 100.0 g/10 min or lower (ISO 1133 at 2.16 kg load and 190° C.), to below 65 ppm (VOC, VDA277), the process comprising the steps of providing a granular raw plastomer in a treatment vessel, the granular raw plastomer having a density of equal to or lower than 883 kg/m3, and a MFR2 of 100.0 g/10 min or lower (ISO 1133 at 2.16 kg load and 190° C.), and a volatile organic compound content (VOC, VDA277) of above 150 ppm, subjecting said granular raw plastomer to a gasflow within the range of 30 m3/(h t) to 150 m3/(h t) for an aeration time of less than 96 hours, whereby the gas has a minimum temperature of at least 26° C. measured at a gas inlet of the treatment vessel and a maximum temperature of 4° C. below the Vicat temperature (10 N, ISO 306) of the granular raw plastomer or 35° C. measured at the gas inlet of the treatment vessel, whatever value is lower; and recovering the granular plastomer.

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08-03-2018 дата публикации

Catalyst Component for High Activity and high Stereoselectivity in Olefin Polymerization

Номер: US20180066084A1
Автор: Demin Xu
Принадлежит: Formosa Plastics Corp USA

What is disclosed is a method for preparing a catalyst system and a catalyst system for polymerizing or copolymerizing an α-olefin. Catalyst component (A) is obtained by a process of reacting a magnesium complex (A-1) containing acid salts of group IB-VIIIB elements formed by contacting a magnesium halide with an acid salt solution of group IB-VIIIB metals or spherical particles adducts, an internal electron donor (A-2) of diester or diether or composite compounds, and a titanium compound (A-3). The catalyst compound (A) is contacted with a silicon compound (B) and an organoaluminium compound (C) to complete the catalyst system providing a good balance of catalyst performance in terms of activity and stereo-specificity.

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08-03-2018 дата публикации

PRODUCING POLYOLEFIN PRODUCTS

Номер: US20180066088A1
Принадлежит: UNIVATION TECHNOLOGIES, LLC

Catalyst systems and methods for making and using the same. A method of polymerizing olefins to produce a polyolefin polymer with a multimodal composition distribution, includes contacting ethylene and a comonomer with a catalyst system. The catalyst system includes a first catalyst compound and a second catalyst compound that are co-supported to form a commonly supported catalyst system. The first catalyst compound includes a compound with the general formula (CHR)(CHR)HfX. The second catalyst compound includes at least one of the following general formulas: 147-. (canceled)49. The method of claim 48 , comprising adding a solution comprising a catalyst to a slurry comprising another catalyst.50. The method of claim 48 , comprising forming a product from the polyolefin polymer.51. The method of claim 48 , comprising:measuring a sample of the polyolefin polymer to obtain an initial product property; andchanging a process parameter to obtain a second product property, based, at least in part, on the initial product property.52. The method of claim 51 , wherein measuring a sample of the polyolefin polymer comprises at least one of:(i) measuring comonomer incorporation as a function of a molecular weight;(ii) determining a physical property of a plastic sample;(iii) determining a flow index, a melt index, a ratio of two melt indices, a density, a molecular weight distribution, a comonomer content.53. The method of claim 51 , wherein changing a process parameter comprises at least one of:(i) adjusting the molar amount of a catalyst component that is combined with a catalyst component slurry;(ii) adjusting a reactor temperature;(iii) adjusting the ethylene partial pressure.54. The method of claim 48 , comprising adjusting a ratio of the hydrogen to ethylene within a polymerization reactor to control a composition distribution claim 48 , a molecular weight distribution claim 48 , a melt index (I) claim 48 , or a ratio of two melt indices claim 48 , or any combinations ...

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08-03-2018 дата публикации

TETRAFLUOROETHYLENE/HEXAFLUOROPROPYLENE COPOLYMERS INCLUDING PERFLUOROALKOXYALKYL PENDANT GROUPS AND METHODS OF MAKING AND USING THE SAME

Номер: US20180066090A1
Принадлежит:

A copolymer having tetrafluoroethylene units, hexafluoropropylene units, and units independently represented by formula in a range from 0.02 to 2 mole percent, based on the total amount of the copolymer. Rf is a linear or branched perfluoroalkyl group having from 1 to 8 carbon atoms and optionally interrupted by one or more —O— groups, n is from 1 to 6, and m is 0 or 1. The copolymer has a melt flow index in a range from 25 grams per 10 minutes to 35 grams per 10 minutes and has up to 50 unstable end groups per 10carbon atoms. The copolymer can be extruded to make articles, such as insulated cables. A method of making the copolymer is also disclosed. 2. The copolymer of claim 1 , wherein m is 0.3. The copolymer of claim 1 , wherein Rf is —CF claim 1 , and wherein n is 1 or 3.4. The copolymer of claim 1 , wherein the copolymer comprises at least 25 parts per million alkali-metal cations.5. The copolymer of claim 1 , wherein the copolymer comprises at least 50 parts per million alkali-metal cations.6. The copolymer of claim 1 , wherein the copolymer has a polydispersity of less than or equal to 2.7. The copolymer of claim 1 , wherein the hexafluoropropylene units are present in the copolymer at 10 percent to 17 percent by weight claim 1 , based on the total weight of the copolymer.8. The copolymer of having a melting point in a range from 235° C. to 275° C.10. A method of making an extruded article claim 1 , the method comprising extruding a melted composition comprising the copolymer of .11. An extruded article comprising the copolymer of .12. The extruded article of claim 11 , wherein the extruded article comprises at least one of a film claim 11 , tube claim 11 , pipe claim 11 , or hose.13. The extruded article of claim 11 , wherein the extruded article is a conductor having the copolymer extruded thereon.14. A method of making the copolymer of claim 1 , the method comprising copolymerizing components comprising tetrafluoroethylene claim 1 , hexafluoropropylene ...

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09-03-2017 дата публикации

COATED POLYPROPYLENE-BASED MOLDED ARTICLE

Номер: US20170066891A1
Принадлежит:

An object of the present invention is to provide a coated polypropylene-based molded article having an excellent gas barrier property. A coated polypropylene-based molded article according to the present invention includes a molded article formed of a polypropylene-based resin composition and a thin film formed on a surface of the molded article, the polypropylene-based resin composition includes a polypropylene-based resin (D) and a nucleating agent (C), the content of the nucleating agent (C) is from 0.05 to 0.5 parts by mass with respect to 100 parts by mass of the polypropylene-based resin (D). 2. The coated polypropylene-based molded article according to claim 1 , whereinthe polypropylene-based resin composition includes a polypropylene-based resin (A) satisfying requirements (A-1) and (A-2) and a polypropylene-based resin (B) satisfying requirements (B-1) and (B-2) as the polypropylene-based resin (D), anda content of the polypropylene-based resin (A) is from 1 to 99 parts by mass with respect to 100 parts by mass of the total mass of the polypropylene-based resin (A) and the polypropylene-based resin (B):(A-1) the polypropylene-based resin (A) is a copolymer of propylene, and one or more olefins selected from the group consisting of ethylene and α-olefins having 4 to 20 carbon atoms;(A-2) a crystalline melting point measured in conformity to JIS-K7121:1987 with a differential scanning calorimetry (DSC) is in a range of 130 to 150° C.;(B-1) the polypropylene-based resin (B) is a propylene homopolymer or a copolymer of propylene, and one or more olefins selected from the group consisting of ethylene and α-olefins having 4 to 20 carbon atoms; and(B-2) a crystalline melting point measured in conformity to JIS-K7121:1987 with a differential scanning calorimetry (DSC) is in a range of 151 to 165° C.3. The coated polypropylene-based molded article according to claim 1 , wherein the polypropylene-based molded article is a container.4. The coated polypropylene-based ...

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15-03-2018 дата публикации

POLYMERIZATION PROCESS IN THE PRESENCE OF ANTISTATIC AGENT

Номер: US20180072876A1
Принадлежит: BASELL POLYOLEFINE GMBH

A process for preparing a polyolefin, including polymerizing olefins in the presence of an antistatic agent made from or containing an alkylene oxide derived polymer made from or containing in average from about 10 to about 200 repeating units —(CH—CHR—O)— with R being hydrogen or an alkyl group having from 1 to 6 carbon atoms, wherein the alkylene oxide derived polymer is a random copolymer of ethylene oxide and other alkylene oxides and a ratio of n:m is in the range of from 6:1 to 1:1, wherein (n) is the average number of repeating units —(CH—CH—O)— derived from ethylene oxide and (m) is the average number of repeating units —(CH—CHR′—O)— derived from the other alkylene oxides with R′ being an alkyl group having from 1 to 6 carbon atoms, and the end groups of the alkylene oxide derived polymer are —OH groups. 1. A process for preparing a polyolefin comprising:a polymerizing olefins at temperatures of from about 20 to about 200° C. and pressures of from about 0.1 to 20 MPa in the presence of a polymerization catalyst in a polymerization reactor, {'sub': '2', 'claim-text': wherein the alkylene oxide derived polymer comprises', '(1) a random copolymer of ethylene oxide and other alkylene oxides and', '(2) a ratio of n:m in the range of from 6:1 to 1:1,', {'sub': 2', '2', '2, 'wherein n is the average number of repeating units of the formula —(CH—CH—O)— derived from ethylene oxide and m is the average number of repeating units —(CH—CHR′—O)— derived from the other alkylene oxides, wherein R′ comprises an alkyl group having from 1 to 6 carbon atoms and end groups of the alkylene oxide derived polymer are —OH groups.'}], '(A) an average of 10 to 200 repeating units of the formula —(CH—CHR—O)—, with R being hydrogen or an alkyl group having from 1 to 6 carbon atoms,'}, '(i) an alkylene oxide derived polymer comprising'}, 'wherein the polymerization is carried out in the presence of an antistatic agent comprising'}2. The process of claim 1 , wherein the ratio of n:m is in ...

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24-03-2022 дата публикации

Olefin Polymer And Preparation Method Thereof

Номер: US20220089797A1
Принадлежит: LG Chem Ltd

The present disclosure provides an olefin polymer having excellent film processability and physical properties, and a preparation method of the same.

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05-03-2020 дата публикации

Process for producing propylene copolymers with low voc content

Номер: US20200071435A1
Принадлежит: WR Grace and Co Conn

A process comprising polymerizing propylene and an olefin comonomer selected from C 2 or C 4 -C 8 with a Ziegler “ Natta catalyst system and hydrogen in a single gas-phase reactor, to form a propylene polymer, at a temperature range of from 78 to 92° C. with a H 2 /C 3 molar ratio of 0.005 to 0.25, the catalyst system comprising: a solid catalyst component comprising a transition metal compound, a Group 2 metal compound, an internal electron donor comprising a substituted phenylene aromatic di ester; an activity limiting agent; an organo-aluminum compound; and an external electron donor composition comprising at least one silane, wherein if the olefin comonomer is ethylene it is present in the propylene polymer in an amount from 1.0-7.0 wt % based on the total weight of the propylene polymer, and if the olefin comonomer is C 4 -C 8 , it is present in an amount from 1.0-15.0 mol % based on the total amount of the propylene polymer.

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18-03-2021 дата публикации

CATALYST AND PREPARATION THEREOF

Номер: US20210079128A1
Принадлежит:

The present invention relates to a process for producing of solid particulate olefin polymerisation catalyst or catalyst carrier comprising forming a solution of the catalyst or a catalyst carrier in a solvent, subjecting the solution into an atomization by spraying the solution via a capillary vibrating spray nozzle with a capillary orifice having a diameter of 5 to 100 μm generating a laminar jet of liquid, which disintegrates into liquid droplets entering into the spray-dryer, transforming the droplets with aid of a gas to solid particulate catalyst or carrier in the spray-dryer and recovering the solid particulate olefin polymerisation catalyst or carrier having particle size distribution defined by a volumetric SPAN of 0.7 or less. The invention further relates to the catalyst produced by the methods, and use thereof in olefin polymerisation process. 1. A process for producing a solid particulate olefin polymerization catalyst or catalyst carrier , the process comprising the steps:i) forming a solution of the catalyst or catalyst carrier in a solvent,ii) subjecting the solution into an atomization by spraying the solution via a capillary vibrating spray nozzle with a capillary orifice having a diameter of 5 to 100 μm thereby generating a laminar jet of liquid, which disintegrates into liquid droplets entering into a spray-dryer,iii) transforming the droplets to the solid particulate olefin polymerization catalyst or catalyst carrier in the spray-dryer with aid of a gas, andiv) recovering the solid particulate olefin polymerization catalyst or catalyst carrier having a particle size distribution defined by a volumetric SPAN of 0.7 or less.2. The process according to claim 1 , wherein the solid particulate olefin polymerization catalyst or catalyst carrier has a medium particle size in the range of 5 to 150 μm.3. The process according to claim 1 , wherein in step iii) the gas is inert and is used as a co-current gas flow claim 1 , preferably as a co-current ...

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14-03-2019 дата публикации

Polyethylene resin composition for injection-molding

Номер: US20190077892A1
Принадлежит: Lotte Chemical Corp

Disclosed herein is a resin composition for injection-molding in which an ethylene-based resin is melt-mixed to be excellent in ductile property and impact property, excellent in environmental stress crack resistance, and low in an overall migration, and thus may be widely used as a food and drug container or a stopper. The present invention provides a resin composition for injection-molding formed by melt-mixing 80-90 wt % of a linear low density polyethylene having a melt flow index of 15-30 dg/min (190° C., 2.16 kg) and 10-20 wt % of an ethylene-alpha-olefin copolymer resin having a melt flow index of 10-20 wt %.

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22-03-2018 дата публикации

CATALYSTS FOR CONTROL OF LONG CHAIN BRANCHING

Номер: US20180079838A1
Принадлежит: UNIVATION TECHNOLOGIES, LLC

Catalyst systems and methods for making and using the same are disclosed. A catalyst composition is provided that includes a catalyst compound supported to form a supported catalyst system, the catalyst compound including: where each of R, R, R, R, R, R, Rand X are as discussed herein. 4. The catalyst composition of claim 1 , comprising an activator comprising an acid derived from a weakly coordinating anion.5. The catalyst composition of claim 4 , wherein the activator comprises an aluminoxane compound claim 4 , an organoboron claim 4 , an organoaluminum compound or combinations thereof.6. The catalyst composition of claim 4 , wherein the activator comprises methyl aluminoxane or modified methylauminoxane.7. The catalyst composition of claim 1 , comprising a support comprising a mineral claim 1 , a clay claim 1 , a metal oxide claim 1 , a metalloid oxide claim 1 , a mixed metal oxide claim 1 , a mixed metalloid oxide claim 1 , a mixed metal-metalloid oxide claim 1 , a polymer claim 1 , or any combinations thereof.8. The catalyst composition of claim 7 , wherein the support is a polyolefin or a polyolefin derivative.9. The catalyst composition of claim 7 , wherein the support has been thermally treated and/or chemically treated with an acid claim 7 , an organoaluminum claim 7 , or a fluoriding agent claim 7 , or any combinations thereof.10. The catalyst composition of claim 7 , wherein the support has been thermally treated.11. The catalyst composition of claim 7 , wherein the support comprises silica claim 7 , alumina claim 7 , aluminosilicate claim 7 , titanated silica claim 7 , or titanated alumina claim 7 , or any combinations thereof.12. The catalyst composition of claim 1 , comprising a silica support and a methyl aluminoxane activator.16. (canceled)17. (canceled)18. (canceled)19. (canceled)20. (canceled)21. (canceled)22. (canceled)23. (canceled)24. (canceled)25. (canceled)26. (canceled)27. (canceled)28. (canceled) Ethylene alpha-olefin (polyethylene) ...

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22-03-2018 дата публикации

Multimodal and Broad Molecular Weight High Density Polyethylene

Номер: US20180079845A1
Принадлежит:

This invention relates to new multimodal and/or broad molecular weight high density polyethylene polymers. The polymers may be made in a single reactor, preferably a gas phase reactor using a dual catalyst system comprising a pyridyldiamido transition metal compound, a metallocene compound, a support, and optionally an activator. 1. A multimodal ethylene polymer comprising a low molecular weight fraction , LMWF , having a molecular weight of less than 100 kg/mol and a high molecular weight fraction , HMWF , having a molecular weight of more than 700 kg/mol , the polymer having:a. at least 50 mol % ethylene;{'sup': '3', 'b. a density of 0.938 to 0.965 g/cmaccording to ASTM D1505;'}{'sub': '5', 'c. a medium load melt index, I, measured according to ASTM D1238 (190° C., 5 kg weight), of 0.05 to 50 g/10 min;'}{'sub': '21', 'd. a flow index, I, measured according to ASTM D1238 (190° C., 21.6 kg weight), of 0.1 to 100 g/10 min;'}e. a ratio of Mz/Mw of greater than 5.5; andf. at least two inflection points in a GPC-4D trace;wherein the polymer is produced in situ in a single reactor.2. The polymer of comprising from 0.1 to 50 wt % of the HMWF.3. The polymer of having a molecular weight distribution claim 1 , Mw/Mn claim 1 , of from 18 to 50.4. The polymer of having a strain hardening ratio claim 1 , SHR claim 1 , via SER of greater than 10 at a Hencky strain rate of 0.1 sand/or 1 10 s.5. The polymer of having a melt strength via RHEOTENS at a 190° C. die temperature of greater than 22 cN.6. The polymer of having a melt index claim 1 , 12 measured according to ASTM D1238 (190° C. claim 1 , 2.16 kg weight) claim 1 , of 0.01 to 10 g/10 min.7. The polymer of having at least three inflection points in a GPC-4D trace.8. The polymer of produced using a supported catalyst system comprising:(i) at least one first catalyst component comprising a pyridyldiamido transition metal complex;(ii) at least one second catalyst component comprising a metallocene compound;(iii) a support ...

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22-03-2018 дата публикации

Multimodal copolymer of ethylene and at least two alpha-olefin comonomers and final articles made thereof

Номер: US20180079899A1
Принадлежит: Borealis AG

The present invention is directed to a multimodal polyethylene copolymer comprising a first and a second copolymer of ethylene and at least two alpha-olefin comonomers. Such multimodal copolymers are highly suitable for conversion processes that require a high Draw Down Ratio, like the production of thin films. Such multimodal polyethylene copolymers provide a good impact strength in the sense of a high Dart drop impact strength (DDI) and good isotropy of the films produces thereof. The invention further presents final articles such as films made therefrom.

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23-03-2017 дата публикации

ETHYLENE-BASED POLYMER COMPOSITION FOR FILMS WITH IMPROVED TOUGHNESS

Номер: US20170081444A1
Принадлежит:

The invention provides a composition comprising a first composition, comprising at least one ethylene-based polymer, and wherein the first composition comprises a MWCDI value greater than 0.9, and a melt index ratio I10/I2 that meets the following equation: I10/I2≧7.0−1.2×log (I2). The invention also provides a process to form a composition comprising at least two ethylene-based polymers, said process comprising the following: polymerizing ethylene, and optionally at least one comonomer, in solution, in the presence of a catalyst system comprising a metal-ligand complex of Structure I, as described herein, to form a first ethylene-based polymer; and polymerizing ethylene, and optionally at least one comonomer, in the presence of a catalyst system comprising a Ziegler/Natta catalyst, to form a second ethylene-based polymer. 1. A composition comprising a first composition , comprising at least one ethylene-based polymer , and wherein the first composition comprises a MWCDI value greater than 0.9 , and a melt index ratio (I10/I2) that meets the following equation: I10/I2≧7.0−1.2×log (I2).2. The composition of claim 1 , wherein the first composition has a MWCDI value less than claim 1 , or equal to claim 1 , 10.0.3. The composition of claim 1 , wherein the ethylene-based polymer is an ethylene/α-olefin interpolymer.4. The composition of claim 1 , wherein the first composition further comprises a second ethylene-based polymer.5. The composition of claim 4 , wherein the second ethylene-based polymer is an ethylene/α-olefin interpolymer.6. The composition of claim 1 , wherein the first composition has a ZSVR value from 1.2 to 3.0.7. The composition of claim 1 , wherein the first composition has a melt index ratio I10/I2 less than claim 1 , or equal to claim 1 , 9.2.8. The composition of claim 1 , wherein the first composition has a vinyl unsaturation level greater than 10 vinyls per 1 claim 1 ,000 claim 1 ,000 total carbons.9. The composition of claim 1 , wherein the ...

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19-03-2020 дата публикации

Modified Supported Chromium Catalysts and Ethylene-Based Polymers Produced Therefrom

Номер: US20200086307A1
Принадлежит: Chevron Phillips Chemical Co LP

Supported chromium catalysts with an average valence less than +6 and having a hydrocarbon-containing or halogenated hydrocarbon-containing ligand attached to at least one bonding site on the chromium are disclosed, as well as ethylene-based polymers with terminal alkane, aromatic, or halogenated hydrocarbon chain ends. Another ethylene polymer characterized by at least 2 wt. % of the polymer having a molecular weight greater than 1,000,000 g/mol and at least 1.5 wt. % of the polymer having a molecular weight less than 1000 g/mol is provided, as well as an ethylene homopolymer with at least 3.5 methyl short chain branches and less than 0.6 butyl short chain branches per 1000 total carbon atoms.

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01-04-2021 дата публикации

POLYETHYLENE COMPOSITION

Номер: US20210095109A1
Принадлежит:

A bimodal linear polyethylene composition, products made therefrom, methods of making and using same, and articles containing same. 16.-. (canceled)7. A method of making a bimodal linear low density polyethylene composition , the method comprising contacting ethylene (monomer) and at least one (C-C)alpha-olefin (comonomer) with a mixture of a bimodal catalyst system and a trim solution in the presence of molecular hydrogen gas (H) and an inert condensing agent (ICA) in one , two or more polymerization reactors under (co)polymerizing conditions , thereby making the bimodal linear low density polyethylene composition; wherein prior to being mixed together the trim solution consists essentially of a (tetramethylcyclopentadienyl)(n-propylcyclopentadienyl)zirconium complex and an inert liquid solvent and the bimodal catalyst system consists essentially of an activator species , a non-metallocene ligand-Group 4 metal complex and a metallocene ligand-Group 4 metal complex , all disposed on a solid support; and wherein the (co)polymerizing conditions comprise a reaction temperature from 80 degrees (°) to 110° Celsius (C.); a molar ratio of the molecular hydrogen gas to the ethylene (H2/C2 molar ratio) from 0.001 to 0.050; and a molar ratio of the comonomer to the ethylene (Comonomer/C2 molar ratio) from 0.005 to 0.10.8. The method of further described by any one of limitations (i) to (vi): (i) wherein the bimodal catalyst system consists essentially of a bis(2-pentamethylphenylamido)ethyl)amine zirconium complex and (tetramethylcyclopentadienyl)(n-propylcyclopentadienyl)zirconium complex claim 7 , in a molar ratio thereof from 1.0:1.0 to 5.0:1.0 claim 7 , respectively claim 7 , and a methylaluminoxane species claim 7 , all disposed by spray-drying onto the solid support; (ii) wherein the bimodal catalyst system further consists essentially of mineral oil and the solid support is a hydrophobic fumed silica; (iii) wherein the mixture is a suspension of the bimodal catalyst ...

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05-04-2018 дата публикации

Linear polypropylene specimen and foam and process of preparing the same

Номер: US20180094111A1
Автор: Chiang-Hsiang Lin
Принадлежит: LCY Chemical Corp

The present disclosure provides a process of preparing linear polypropylene foam, comprising the following steps: (a) preparing a specimen comprising at least one linear polypropylene; and at least one nucleating agent selected from the group consisting of alpha nucleating agents and beta nucleating agents; (b) deforming the specimen under a deforming pressure and at a deforming temperature for a period of time; and (c) subjecting the deformed specimen obtained in the step (b) to a foaming process to obtain the linear polypropylene foam. The present disclosure further provides a specimen after PIF treatment and a linear polypropylene foam prepared by the above process.

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05-04-2018 дата публикации

THERMOPLASTIC COMPOSITION AND ARTICLE

Номер: US20180094128A1
Принадлежит:

The invention is directed to a thermoplastic composition and to an article made from said thermoplastic composition. More in particular, the invention relates to blended polyolefinic materials, which, after moulding, provide a soft touch feel. The thermoplastic composition of the invention comprises (A) 10-40% by total weight of the composition of glass fibres; (B) 22-46% by total weight of the composition of a propylene homopolymer matrix phase; (C) 1.5-26% by total weight of the composition of an ethylene-propylene copolymer dispersed phase; and (D) 11-46% by total weight of the composition of a mixture of elastomers, said mixture comprising an ethylene/Cα-olefin copolymer and an ethylene/Cα-olefin copolymer. 1. A thermoplastic composition comprising ,A) 10-40% by total weight of the composition of glass fibres;B) 22-46% by total weight of the composition of a propylene homopolymer matrix phase;C) 1.5-26% by total weight of the composition of an ethylene-propylene copolymer dispersed phase; and{'sub': 5-8', '3-4, 'D) 11-46% by total weight of the composition of a mixture of elastomers, said mixture comprising an ethylene/Cα-olefin copolymer and an ethylene/Cα-olefin copolymer.'}2. A thermoplastic composition according to claim 1 ,{'sub': 5-8', '6-8, 'wherein said ethylene-Cα-olefin copolymer is an ethylene/Cα olefin copolymer.'}3. A thermoplastic composition according to claim 1 , wherein said ethylene/Cα-olefin is copolymer of ethylene and 1-butene.4. A thermoplastic composition according to claim 1 , wherein the ethylene/Cα-olefin copolymer and the ethylene/Cα-olefin copolymer are present in a weight ratio of 5:1 to 1:1.5. A thermoplastic composition according to claim 1 , wherein said propylene homopolymer phase (B) and said ethylene propylene copolymer dispersed phase (C) are a homopolymer-based matrix phase and a dispersed elastomeric phase of a heterophasic polypropylene copolymer.6. A thermoplastic composition according to claim 1 , wherein the elastomers ...

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12-05-2022 дата публикации

Ligand Compound, Transition Metal Compound, And Catalyst Composition Including The Same

Номер: US20220144773A1
Принадлежит: LG Chem Ltd

The present invention provides a novel ligand compound, a transition metal compound and a catalyst composition including the same.

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12-05-2022 дата публикации

Process for preparing a polypropylene composition

Номер: US20220145055A1
Принадлежит: Borealis AG

The invention relates to a process for producing a polypropylene composition by sequential polymerization the polypropylene composition having an improved balanced combination of high flowability, high stiffness and impact, and high level of optical properties.

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06-04-2017 дата публикации

Supported Catalyst Systems and Methods of Using Same

Номер: US20170096506A1
Принадлежит:

A catalyst system including the reaction product of a fluorided support (such as a fluorided silica support) that preferably has not been calcined at a temperature of 400° C. or more, an activator and at least a first transition metal catalyst compound; methods of making such catalyst systems, polymerization processes using such catalyst systems and polymers made therefrom. 2. The catalyst system of claim 1 , wherein the fluorided support comprises fluorided silica.3. The catalyst system of claim 2 , wherein the fluorided silica has not been calcined at a temperature of 400° C. or more.4. The catalyst system of claim 1 , wherein M is a group 4 claim 1 , 5 claim 1 , or 6 transition metal; each X is independently hydrogen claim 1 , halogen claim 1 , or a hydrocarbyl group; Rand Rare independently a Cto Chydrocarbon group; m is 0 claim 1 , −1 claim 1 , −2 claim 1 , or −3 and n is +3 claim 1 , +4 claim 1 , or +5; Rand Rare independently a hydrocarbon group having up to 20 carbon atoms or an aryl group or an aralkyl group.5. The catalyst system of claim 1 , wherein Ris absent claim 1 , hydrogen claim 1 , or methyl.7. The catalyst system of claim 6 , wherein Ris methyl claim 6 , ethyl claim 6 , propyl or butyl and/or Ris methyl claim 6 , ethyl claim 6 , propyl claim 6 , or butyl claim 6 , and/or Ris methyl claim 6 , ethyl claim 6 , propyl or butyl claim 6 , and/or Ris methyl claim 6 , ethyl claim 6 , propyl claim 6 , or butyl and/or Ris methyl claim 6 , ethyl claim 6 , propyl claim 6 , or butyl.8. The catalyst system of claim 6 , wherein R claim 6 , R claim 6 , and Rare methyl and Rand Rare hydrogen.9. The catalyst system of claim 1 , further comprising a second catalyst compound according to Formula 1.12. The catalyst system of claim 1 , wherein the activator comprises alkyl aluminum compounds claim 1 , alumoxanes claim 1 , modified alumoxanes claim 1 , non-coordinating anions claim 1 , boranes claim 1 , borates claim 1 , and/or ionizing compounds.13. The catalyst system ...

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14-04-2016 дата публикации

Titanium Phosphinimide and Titanium Iminoimidazolidide Catalyst Systems With Activator-Supports

Номер: US20160102161A1
Принадлежит: Chevron Phillips Chemical Co LP

Catalyst compositions containing activator-supports and half-metallocene titanium phosphinimide complexes or half-metallocene titanium iminoimidazolidide complexes are disclosed. These catalyst compositions can be used to produce olefin polymers having relatively broad molecular weight distributions and low levels of long chain branching.

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26-03-2020 дата публикации

Rapid activation process and activation treatments for chromium catalysts for producing high melt index polyethylenes

Номер: US20200095350A1
Принадлежит: Chevron Phillips Chemical Co LP

Processes for activating chromium polymerization catalysts, which can use lower maximum activation temperatures and shorter activation times than conventional activation methods, and provide polyethylenes with high melt indices, broader molecular weight distributions, and lower long chain branching content. The activation process can comprise heating a supported chromium catalyst in an inert atmosphere to a first temperature (T1) for a first hold time (tH1), followed by allowing the chromium catalyst to attain a second temperature (T2) in the inert atmosphere, then contacting the chromium catalyst with an oxidative atmosphere for a second hold time (tH2), in which T2 can be less than or equal to T1. Additional activation treatments and conditioning steps are disclosed which can be used to enhance the melt index potential of Phillips (Cr/silica) catalysts.

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13-04-2017 дата публикации

POLYPROPYLENE WITH BROAD MOLECULAR WEIGHT DISTRIBUTION

Номер: US20170101487A1
Принадлежит:

Propylene homopolymer having a melt flow rate MFR(230° C.) at least 50 g/10 min, a Mw/Mn at least 12.0 and a xylene cold soluble content (XCS) of at least 2.8 wt.-%. 118-. (canceled)19. A propylene homopolymer having:{'sub': '2', '(a) a melt flow rate MFR(230° C.) measured according to ISO 1133 of 60 to 500 g/10 min;'}(b) a ratio of weight average molecular weight (Mw) to number average molecular weight (Mn) [Mw/Mn] of at least 12.0; and(c) a xylene cold soluble content (XCS) determined according ISO 16152 (25° C.) of 2.5 to 4.5 wt. %.20. The propylene homopolymer according to claim 19 , wherein the propylene homopolymer has a ratio of the complex viscosity eta* at 0.05 rad/sec to the complex viscosity eta* at 300 rad/sec of at least 4.0.21. The propylene homopolymer according to claim 19 , wherein the propylene homopolymer has:{'sup': '13', '(a) 2,1 erythro regio-defects of equal or below 0.4 mol. % determined by C-NMR spectroscopy; and/or'}(b) a pentad isotacticity (mmmm) of more than 95.0%.22. The propylene homopolymer according to claim 19 , wherein the propylene homopolymer has:(a) a ratio of z-average molecular weight (Mz) to weight average molecular weight (Mw) [Mz/Mw] of at least 6.0; and/or(b) a ratio of z-average molecular weight (Mz) to number average molecular weight (Mn) [Mz/Mn] of at least 80.23. The propylene homopolymer according to claim 19 , wherein the propylene homopolymer is not nucleated and optionally has:(a) a weight ratio of the crystalline fractions melting in the temperature range of above 160 to 180° C. to the crystalline fractions melting in the temperature range of 90 to 160° C. of at least 1.30, wherein the fractions are determined by a stepwise isothermal segregation technique (SIST), and/or(b) a crystallization temperature of at least 112° C.; and/or(c) a tensile modulus measured according to ISO 527-2 of at least 1,950 MPa.24. The propylene homopolymer according to claim 20 , wherein the propylene homopolymer is α-nucleated and ...

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13-04-2017 дата публикации

POLYPROPYLENE WITH BROAD MOLECULAR WEIGHT DISTRIBUTION

Номер: US20170101489A1
Принадлежит:

Propylene homopolymer having a melt flow rate MFR(230° C.) at least 50 g/10 min, a Mw/Mn at least 12.0 and a xylene cold soluble content (XCS) of at least 2.8 wt.-%. 118-. (canceled)19. A propylene homopolymer having:{'sub': '2', '(a) a melt flow rate MFR(230° C.) measured according to ISO 1133 of 60 to 500 g/10 min;'}(b) a ratio of the complex viscosity eta* at 0.05 rad/sec to the complex viscosity eta* at 300 rad/sec of at least 4.0; and(c) a xylene cold soluble content (XCS) determined according ISO 16152 (25° C.) of at least 2.8 wt. %.20. The propylene homopolymer according to claim 19 , wherein the propylene homopolymer has a ratio of weight average molecular weight (Mw) to number average molecular weight (Mn) [Mw/Mn] of at least 12.0.21. The propylene homopolymer according to claim 19 , wherein the propylene homopolymer has:{'sup': '13', '(a) 2,1 erythro regio-defects of equal or below 0.4 mol. % determined by C-NMR spectroscopy; and/or'}(b) a pentad isotacticity (mmmm) of more than 95.0%.22. The propylene homopolymer according to claim 19 , wherein the propylene homopolymer has:(a) a ratio of z-average molecular weight (Mz) to weight average molecular weight (Mw) [Mz/Mw] of at least 6.0; and/or(b) a ratio of z-average molecular weight (Mz) to number average molecular weight (Mn) [Mz/Mn] of at least 80.23. The propylene homopolymer according to claim 19 , wherein the propylene homopolymer is not nucleated and optionally has:(a) a weight ratio of the crystalline fractions melting in the temperature range of above 160 to 180° C. to the crystalline fractions melting in the temperature range of 90 to 160° C. of at least 1.30, wherein the fractions are determined by a stepwise isothermal segregation technique (SIST), and/or(b) a crystallization temperature of at least 112° C.; and/or(c) a tensile modulus measured according to ISO 527-2 of at least 1,950 MPa.24. The propylene homopolymer according to claim 19 , wherein the propylene homopolymer is α-nucleated and ...

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13-04-2017 дата публикации

Ethylene-based polymers

Номер: US20170101495A1
Принадлежит: Dow Global Technologies LLC

The invention provides an ethylene-based polymer comprising the following properties: a) a ZSVR value from 1.2 to 2.6, b) a MWD from 1.5 to 2.8, and c) a tan delta (0.1 rad/s; 190 C) from 5.0 to 50.

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04-04-2019 дата публикации

BUTENE-1 POLYMER IN MASTERBATCH, CONCENTRATE, AND COMPOUNDING APPLICATIONS

Номер: US20190100609A1
Принадлежит: BASELL POLIOLEFINE ITALIA S.R.L.

One or more 1-butene polymers and uses thereof. The 1-butene polymer may be used as a viscosity modifier, flexibilizer, dispersing aid, and/or impact modifier for polymer compositions, such as those including polypropylene. The 1-butene polymer may also be used as a carrier for additives, such as fluorinated additives. Articles may be made that include the 1-butene polymer, polypropylene, and pigments. 1. A composition comprising:a 1-butene polymer;a pigment; anda polypropylene;wherein the 1-butene polymer is present in the composition at an amount of about 5% to about 20% by weight, based on the weight of the composition,wherein the pigment is present in the composition at an amount of about 10% to about 45% by weight, based on the weight of the composition; andwherein the polypropylene is present in the composition at an amount of about 25% to about 85% by weight, based on the weight of the composition.2. The composition of claim 1 , wherein the pigment is in a particulate form having an average particle size of about 5 μm to about 55 μm.3. The composition of claim 1 , wherein the pigment is in a particulate form having an average particle size of about 10 μm to about 30 μm.4. The composition of claim 1 , further comprising one or more additives claim 1 , wherein the one or more additives are present in the composition at an amount of about 0.01% to about 10% by weight claim 1 , based on the weight of the composition.5. The composition of claim 4 , wherein the one or more additives is selected from a stabilizer claim 4 , a nucleating agent claim 4 , a slip agent claim 4 , an antiblocking agent claim 4 , a lubricant claim 4 , an antistatic agent claim 4 , a modifier of molecular weight claim 4 , a modifier of one or more rheological properties claim 4 , or a combination thereof.6. The composition of claim 1 , wherein the 1-butene polymer has a melt flow rate of about 0.1 to about 3000 g/10 min at a temperature of 190° C. and a load of 2.16 kg and a density of about ...

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04-04-2019 дата публикации

Ethylene/1-hexene Copolymer Having Excellent Processability And Mechanical Properties

Номер: US20190100611A1
Принадлежит: LG Chem Ltd

The ethylene/1-hexene copolymer according to the present invention has excellent processability and mechanical properties, and thus can be applied to various fields such as food containers.

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21-04-2016 дата публикации

Dilution index

Номер: US20160108218A1
Принадлежит: Nova Chemicals International SA

This disclosure relates to ethylene interpolymer compositions. Specifically, ethylene interpolymer products having: a Dilution Index (Y d ) greater than 0; total catalytic metal≧3.0 ppm; ≧0.03 terminal vinyl unsaturations per 100 carbon atoms, and; optionally a Dimensionless Modulus (X d ) greater than 0. The disclosed ethylene interpolymer products have a melt index from about 0.3 to about 500 dg/minute, a density from about 0.869 to about 0.975 g/cm 3 , a polydispersity (M w /M n ) from about 2 to about 25 and a CDBI 50 from about 20% to about 97%. Further, the ethylene interpolymer products are a blend of at least two ethylene interpolymers; where one ethylene interpolymer is produced with a single-site catalyst formulation and at least one ethylene interpolymer is produced with a heterogeneous catalyst formulation.

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19-04-2018 дата публикации

A process for controlling particle size distribution of a ziegler-natta catalyst composition

Номер: US20180105621A1
Принадлежит: Reliance Industries Ltd

The present disclosure relates to a process for controlling particle size distribution of a Ziegler-Natta catalyst composition. In order to control the particle size distribution, magnesium metal is reacted with a mixture comprising a first alcohol and a second alcohol to obtain a slurry which includes a mixture of magnesium alkoxides and unreacted alcohol. The unreacted alcohol is separated from the slurry to obtain the mixture of magnesium alkoxides having reduced methoxy content less than 2 wt %. The mixture of magnesium alkoxides is chlorinated to obtain a Ziegler-Natta pro-catalyst. The Ziegler-Natta pro-catalyst is mixed with a co-catalyst to obtain a Ziegler-Natta catalyst composition with controlled particle size distribution in the range of 5 μm to 15 μm.

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19-04-2018 дата публикации

PRODUCING POLYOLEFIN PRODUCTS

Номер: US20180105625A1
Принадлежит: UNIVATION TECHNOLOGIES, LLC

Catalyst systems and methods for making and using the same are described. A method includes selecting a catalyst blend using a blend polydispersity index (bPDI) map. The polydispersity map is generated by generating a number of polymers for at least two catalysts. Each polymer is generated at a different hydrogen to ethylene ratio. At least one catalyst generates a higher molecular weight polymer and another catalyst generates a lower molecular weight polymer. A molecular weight for each polymer is measured. The relationship between the molecular weight of the polymers generated by each of the catalysts and the ratio of hydrogen to ethylene is determined. A family of bPDI curves for polymers that would be made using a number of ratios of a blend of the at least two catalysts for each of a number of ratios of hydrogen to ethylene. A ratio for the catalyst blend of the catalysts that generates a polymer having a bPDI that matches a polymer fabrication process is selected, and the product specific polyolefin is made using the catalyst blend. 1. A polymerization catalyst for forming a polyethylene copolymer , comprising:a catalyst support;{'sub': 2', '2', '6', '2, 'sup': −6', '−6, 'a first catalyst that is impregnated on the catalyst support, wherein the first catalyst generates polymers having a slope for a plot of H/Cversus 1/Mw of between about 1.0×10and about 1.5×10, and wherein at a C/Cratio of between about 0.008 and about 0.012, the first catalyst generates a polymer having an MI of about 1.0 dg/10 min, a density of about 0.92 g/cc, and a melt index ratio (MIR) less than about 25; and'}{'sub': 2', '2', '6', '2, 'sup': −6', '−6, 'a second catalyst that is impregnated on the catalyst support with the first catalyst, wherein the second catalyst generates polymers having a slope for a plot of H/Cversus 1/Mw of between about 3.0×10and about 4×10, and wherein at a C/Cratio of between about 0.03 and about 0.04, the second catalyst generates a polymer having an MI of ...

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26-04-2018 дата публикации

Ethylene-Based Polymers with Low Hexane Extractables

Номер: US20180112017A1
Принадлежит:

Ethylene-based polymers comprising the following properties: (A) a density from 0.9190 g/cc to 0.9240 g/cc; (B) a hexane extractable level that is less than or equal to the lower of: (1) (A+(B*density (g/cc))+(C*log(MI) dg/min)) based on total weight of the ethylene-based polymer; where A=250.5 wt %, B=−270 wt %/(g/cc), C=0.25 wt %/[log(dg/min)], or (2) 2.0 wt %; (C) a G′ (at G″=500 Pa, 170° C.) that meets the following equation: G′≥D+E[log (12)], where D=150 Pa and E=−60 Pa/[log(dg/min)]; and (D) a melt index (12) from 1.0 to 20 dg/min; are made in process comprising the step of contacting in a reaction configuration, comprising a first tubular reaction zone 1 and a last tubular reaction zone i, in which i is greater than or equal to (≥) 3, under high pressure polymerization conditions, and in which the first reaction zone 1 has a peak polymerization temperature greater than the peak temperature of the ith reaction zone, and wherein the difference in these two peak temperatures is ≥30° C. 1. An ethylene-based polymer formed from a free-radical , high pressure polymerization process that includes a reactor configuration comprising , as reactors , only one or more tubular reactors , said polymer comprising the following properties:(A) a density from 0.9190 g/cc to 0.9240 g/cc; (1) (A+(B*density (g/cc))+(C*log(MI) dg/min)) based on total weight of the ethylene-based polymer; where A=250.5 wt %, B=−270 wt %/(g/cc), C=0.25 wt %/[log(dg/min)], or', '(2) 2.0 wt %;, '(B) a hexane extractable level that is less than or equal to the lower of(C) a G′ (at G″ =500 Pa, 170° C.) that meets the following equation: G′≥D+E[log (I2)], where D=150 Pa and E=−60 Pa/[log(dg/min)]; and(D) a melt index (I2) from 1.0 to 20 dg/min.2. The ethylene-based polymer of claim 1 , wherein the polymer is polymerized in the presence of at least one branching agent.3. The ethylene-based polymer of claim 2 , wherein the branching agent is at least one of a monomeric CTA and a polyene.4. The ethylene- ...

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27-04-2017 дата публикации

Production of Polyolefins with Internal Unsaturation Structures Using a Metallocene Catalyst System

Номер: US20170114167A1
Принадлежит:

This invention relates to a process to polymerize olefins, particularly to produce ethylene polymers with internal unsaturation structures. 2. The process of claim 1 , wherein each Xand Xis claim 1 , independently claim 1 , selected from the group consisting of halides and Cto Calkyl groups.3. The process of claim 1 , wherein each Rand Ris claim 1 , independently a Cto Csubstituted or unsubstituted aryl.4. The process of or claim 1 , wherein at least one of R claim 1 , R claim 1 , R claim 1 , and Rand at least one of R claim 1 , R claim 1 , R claim 1 , R claim 1 , is a linear Cto Csubstituted or unsubstituted hydrocarbyl group.5. The process of claim 1 , wherein each R claim 1 , R claim 1 , R claim 1 , R claim 1 , R claim 1 , R claim 1 , and Ris claim 1 , independently claim 1 , a linear Cto Calkyl group.6. The process of claim 1 , wherein at least one of Rand Rand at least one of Rand R claim 1 , is independently selected from the group consisting of n-propyl claim 1 , n-butyl claim 1 , n-pentyl claim 1 , and n-hexyl groups.7. The process of claim 1 , wherein each Rand Ris claim 1 , independently selected from the group consisting of phenyl claim 1 , and substituted phenyl groups.8. The process of claim 1 , wherein the metallocene compound comprises one or more of:{'sup': 1', '2, 'diphenylsilylbis(n-propylcyclopentadienyl)hafnium XX,'}{'sup': 1', '2, 'diphenylsilylbis(n-butylcyclopentadienyl)hafniumXX,'}{'sup': 1', '2, 'diphenylsilylbis(n-pentylcyclopentadienyl)hafniumXX,'}{'sup': 1', '2, 'diphenylsilyl (n-propyl cyclopentadienyl)(n-butyl cyclopentadienyl)hafniumXX,'}{'sup': 1', '2, 'diphenylsilylbis[(2-trimethylsilylethyl)cyclopentadienyl]hafniumXX,'}{'sup': 1', '2, 'dimethylsilylbis(n-propylcyclopentadienyl)hafniumXX,'}{'sup': 1', '2, 'dimethylsilylbis(n-butylcyclopentadienyl)hafniumXX,'}{'sup': 1', '2, 'dimethylsilylbis(n-pentylcyclopentadienyl)hafniumXX,'}{'sup': 1', '2, 'dimethylsilyl (n-propyl cyclopentadienyl)(n-butyl cyclopentadienyl)hafniumXX,'}{'sup': 1', ...

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18-04-2019 дата публикации

POLYOLEFIN BLENDS INCLUDING CRYSTALLINE BLOCK COMPOSITES FOR PVC-FREE WEAR LAYERS

Номер: US20190112407A1
Принадлежит:

A composition comprising (A) from 10 wt % to 90 wt % of a polymeric ethylene ionomer; (B) from 10 wt % to 40 wt % of a propylene component including at least one propylene based polymer having a propylene content of at least 50.0 wt %, based on the total weight of the propylene based polymer, and a melt flow rate from 0.5 g/10 min to 200.0 g/10 min (according to ASTM D-1238 at 230° C/2.16 kg); and (C) from 5 wt % to 20 wt % of a crystalline block composite. 1. A composition comprising:(A) from 10 wt % to 90 wt % of a polymeric ethylene ionomer;(B) from 10 wt % to 40 wt % of a propylene component including at least one propylene based polymer having a propylene content of at least 50.0 wt %, based on the total weight of the propylene based polymer, and a melt flow rate from 0.5 g/10 min to 50 g/10 min (according to ASTM D-1238 at 230° C./2.16 kg);{'sub': '3-10', '(C) from 5 wt % to 20 wt % of a crystalline block composite comprising (i) a crystalline ethylene based polymer, (ii) a crystalline alpha-olefin based polymer derived from at least one of a Calpha-olefin, and (iii) a block copolymer comprising a crystalline ethylene block and a crystalline alpha-olefin block, the crystalline ethylene block of the block copolymer having the same composition as the crystalline ethylene based polymer of the crystalline block composite, and the crystalline alpha-olefin block of the block copolymer having the same composition as the crystalline alpha-olefin based polymer of the crystalline block composite.'}2. The composition of claim 2 , further comprising from 0.1 wt % to 5 wt % of an antioxidant.3. The composition of claim 1 , wherein the polymeric ethylene ionomer comprises an acrylic acid ethylene copolymer that is neutralized with a metal salt.4. The composition of claim 3 , wherein the metal salt is selected from the group consisting of zinc claim 3 , sodium claim 3 , and calcium.5. The composition of claim 1 , wherein the polymeric ethylene ionomer has a density from 0. ...

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13-05-2021 дата публикации

Dual Catalyst System for Producing High Density Polyethylenes With Long Chain Branching

Номер: US20210139619A1
Принадлежит:

Disclosed herein are ethylene-based polymers generally characterized by a melt index of less than 1 g/10 min, a density from 0.93 to 0.965 g/cm, a CY-a parameter at 190° C. of less than 0.2, an average number of short chain branches per 1000 total carbon atoms of the polymer in a molecular weight range of 400,000 to 600,000 g/mol that is greater than that in a molecular weight range of 40,000 to 60,000 g/mol, and an average number of long chain branches per 1000 total carbon atoms of the polymer in a molecular weight range of 400,000 to 600,000 g/mol that is greater than that in a molecular weight range of 4,000,000 to 6,000,000 g/mol. The ethylene polymers can be used to fabricate pipes, blown films, and blow molded products, and the ethylene polymers can be produced with a dual catalyst system containing a single atom bridged or two carbon atom bridged metallocene compound with two indenyl groups or an indenyl group and a cyclopentadienyl group, and a single atom bridged metallocene compound with a fluorenyl group and a cyclopentadienyl group with an alkenyl substituent. 1. An ethylene polymer having:a melt index of less than or equal to about 1 g/10 min;{'sup': '3', 'a density in a range from about 0.93 to about 0.965 g/cm;'}a CY-a parameter at 190° C. of less than or equal to about 0.2;an average number of short chain branches (SCB's) per 1000 total carbon atoms of the polymer in a molecular weight range of 400,000 to 600,000 g/mol that is greater than that in a molecular weight range of 40,000 to 60,000 g/mol; andan average number of long chain branches (LCB's) per 1000 total carbon atoms of the polymer in a molecular weight range of 400,000 to 600,000 g/mol that is greater than that in a molecular weight range of 4,000,000 to 6,000,000 g/mol.2. An article of manufacture comprising the polymer of .3. The polymer of claim 1 , wherein:the average number of SCB's per 1000 total carbon atoms of the polymer in the molecular weight range of 400,000 to 600,000 g/mol ...

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09-04-2020 дата публикации

GERMANIUM-BRIDGED BIS-BIPHENYL-PHENOXY CATALYSTS FOR OLEFIN POLYMERIZATION

Номер: US20200109220A1
Принадлежит: Dow Global Technologies LLC

Embodiments are directed to a catalyst system comprising metal ligand complexes and processes for polyolefin polymerization using the metal ligand complex having the following structure: Formula I 2. The catalyst system according to claim 1 , wherein:M is zirconium or hafnium; each Z is oxygen; and{'sup': 1', '16, 'Rand Rare identical and are selected from the group consisting of radicals having formula (II), radicals having formula (III), and radicals having formula (IV).'}3. The catalyst system according to claim 1 , wherein at least one of Rand Ris a radical having formula (III) claim 1 , where at least one of Ror Ris tert-butyl and where R claim 1 , R claim 1 , and Rare —H.4. The catalyst system according to claim 1 , wherein at least one of Rand Ris a radical having formula (III) claim 1 , where at least one of Ror Ris tert-butyl and where R claim 1 , R claim 1 , and Rare —H.5. The catalyst system according to claim 1 , wherein at least one of Rand Ris a radical having formula (II) claim 1 , where Rand Rare independently tert-butyl.6. The catalyst system according to claim 1 , wherein Rand Rare independently tert-octyl or n-octyl.7. The catalyst system according to claim 1 , wherein Rand Rare halogen.8. The catalyst system according to claim 1 , wherein Rand Rare tert-butyl.9. The catalyst system according to claim 1 , wherein Rand Rare methyl; and wherein Rand Rare halogen.10. The catalyst system according to claim 1 , wherein:{'sup': 5-7', '10-12, '(A) when Rare fluorine, not more than one of Ris fluorine;'}{'sup': 10-12', '5-7, '(B) when Rare fluorine, not more than one of Ris fluorine; or'}{'sup': 5-7', '10-12, '(C) fewer than four of Rand Rare fluorine.'}11. The catalyst system according to claim 1 , wherein R claim 1 , R claim 1 , R claim 1 , and Rare —H.12. The catalyst system according to claim 1 , wherein Rand Rare halogen.13. The catalyst system according to claim 1 , wherein Rand Rare halogen.14. The catalyst system according to claim 1 , wherein at ...

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03-05-2018 дата публикации

Polymerization Process

Номер: US20180118861A1
Принадлежит:

A process including contacting one or more monomers, at least one catalyst system, and a condensing agent including a majority of 2,2-dimethylpropane under polymerizable conditions to produce a polyolefin polymer is provided. 1. A polymerization process , the process comprising contacting one or more monomers , at least one catalyst system , and a condensing agent comprising a majority of 2 ,2-dimethylpropane under polymerizable conditions to produce a polyolefin polymer; wherein the production rate of the polyolefin polymer is at least 20% greater than the same process polymerizing with another C-Ccondensing agent.2. A polymerization process , the process comprising contacting one or more monomers , at least one catalyst system , and a condensing agent comprising a mixture of 2 ,2-dimethylpropane and at least another C-Ccondensing agent under polymerizable conditions to produce a polyolefin polymer.3. The process of claim 2 , wherein the production rate of the polyolefin polymer is at least 20% greater than the same process polymerizing substantially free of 2 claim 2 ,2-dimethylpropane.4. The process of claim 1 , wherein the production rate of the polyolefin polymer is at least 25% greater than the same process polymerizing with another C-Ccondensing agent.5. The process of claim 1 , wherein the production rate of the polyolefin polymer is at least 30% greater than the same process polymerizing with another C-Ccondensing agent.6. The process of claim 1 , wherein the C-Ccondensing agent comprises n-butane claim 1 , isobutane claim 1 , n-pentane claim 1 , isopentane claim 1 , n-hexane claim 1 , isohexane claim 1 , n-heptane claim 1 , n-octane claim 1 , or mixtures thereof.7. The process of any one of claim 1 , wherein the C-Ccondensing agent is isopentane.8. The process of claim 1 , wherein the ratio of the 2 claim 1 ,2-dimethylpropane to the C-Ccondensing agent is greater than or equal to 50:50.9. The process of claim 1 , wherein the ratio of the 2 claim 1 ,2- ...

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16-04-2020 дата публикации

Fluororesin molded article

Номер: US20200114563A1
Принадлежит: Chemours Mitsui Fluoroproducts Co Ltd

A PFA molded article of a copolymer (PFA) of tetrafluoroethylene (TFE) and perfluoro(alkylvinyl ether) (PAVE), the content of the PAVE therein being from 1 to 10% by mol, characterized in that the PFA molded article has a flex life value of not less than 2,000,000 times, a zero share viscosity of from 10,000 to 20,000 Pa·s, and a heating weight loss of not more than 0.05% by weight, and a process for the production thereof. The PFA molded article has a high flex life value, a low heating weight loss and a low zero share viscosity yet maintaining excellent mechanical properties such as tensile strength, etc., and can be produced in good yields.

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25-04-2019 дата публикации

PROCESS FOR PRODUCING LLDPE RESINS

Номер: US20190119419A1
Принадлежит:

A process for producing copolymers of ethylene and at least one alpha-olefin having from 4 to 10 carbon atoms in the presence of a solid Ziegler-Natta catalyst comprising of magnesium, titanium, halogen and an internal organic compound, the copolymer having a density of from 906 to 937 kg/mand a melt flow rate MFRmeasured at 190° C. under 21.6 kg load of from 3 to 150 g/10 min. The process includes the steps of (A) homopolymerising ethylene or copolymerising ethylene and a first alpha-olefin having from 4 to 10 carbon atoms in a first polymerisation stage in the presence of the polymerisation catalyst, hydrogen and optionally the first alpha-olefin; (B) copolymerising ethylene and a second alpha-olefin having from 4 to 10 carbon atoms in a second polymerisation stage in the presence of the first homo- or copolymer of ethylene and the Ziegler-Natta catalyst; and (C) recovering the polymer mixture. 2. The process according to comprising the additional steps of (a) providing solid carrier particles of MgCl*mROH adduct; (b) pre-treating the solid carrier particles of step (a) with a compound of Group 13 metal; (c) treating the pre-treated solid carried particles of step (b) with a transition metal compound of Group 4 to 6; (d) recovering the solid catalyst component; (e) contacting the solid carrier particles with the internal organic compound compound having the formula (I) prior to the step (c); and (f) passing the solid catalyst component into the first polymerisation stage claim 1 , wherein R in the adduct MgCl*mROH is a linear or branched alkyl group with 1 to 12 carbon atoms and m is a number from 0 to 6.3. The process according to wherein the hydrogen to ethylene ratio in the fluid reaction phase of the first polymerisation stage is from 200 to 1000 mol/kmol.4. The process according to wherein the first homo- or copolymer of ethylene is a homopolymer of ethylene and no comonomer is present in the first polymerisation stage.5. The process according to wherein the ...

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25-04-2019 дата публикации

Ethylene/alpha-olefin Copolymer Having Excellent Processibility

Номер: US20190119421A1
Принадлежит: LG Chem Ltd

The present disclosure relates to an ethylene/alpha-olefin copolymer having excellent processibility. The ethylene/alpha-olefin copolymer according to the present disclosure is excellent in both mechanical properties and processibility.

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25-04-2019 дата публикации

PROPYLENE-DIENE COPOLYMER RESIN HAVING EXCELLENT MELT TENSION

Номер: US20190119427A1
Принадлежит: LOTTE CHEMICAL CORPORATION

Disclosed is a propylene-diene copolymer resin having excellent melt tension, with improved melt strength, high molecular weight and broad molecular weight distribution by using a specific metallocene catalyst system. The present invention provides a propylene-diene copolymer resin produced by polymerizing propylene and a diene compound of C4-C20 by using a metallocene catalyst system, wherein the propylene-diene copolymer resin has the melt index (2.16 kg load at 230° C.) of 0.1-100 g/10 min and the melt tension (advanced rheometric expansion system (ARES)) of 5-100 g. 1. A propylene-diene copolymer resin produced by a method comprising the step of polymerizing propylene and a diene compound of C4-C20 by using a catalyst system ,wherein the catalyst system comprises: a metallocene compound represented by the following Chemical Formula 1; and at least one cocatalyst compound selected from the group consisting of a boron compound represented by the following Chemical Formulae 2 to 4 and an aluminum compound represented by the following Chemical Formulae 5 to 9, and [{'chemistry': {'@id': 'CHEM-US-00014', '@num': '00014', 'img': {'@id': 'EMI-C00014', '@he': '30.06mm', '@wi': '69.93mm', '@file': 'US20190119427A1-20190425-C00014.TIF', '@alt': 'embedded image', '@img-content': 'chem', '@img-format': 'tif'}}, 'br': None, 'sup': '11', 'sub': '3', 'B(R)\u2003\u2003[Chemical Formula 2]'}, {'br': None, 'sup': 12', '+', '11', '−, 'sub': '4', '[R][B(R)]\u2003\u2003[Chemical Formula 3]'}, {'br': None, 'sup': 13', '+', '11', '−, 'sub': r', '4, '[(R)ZH][B(R)]\u2003\u2003[Chemical Formula 4]'}, {'br': None, 'sup': '14', 'sub': 's', '—[Al(R)—O]—\u2003\u2003[Chemical Formula 5]'}, {'br': None, 'sup': 14', '14', '14, 'sub': 2', 't', '2, '(R)Al—[O(R)]—(R)\u2003\u2003[Chemical Formula 6]'}, {'br': None, 'sup': '15', 'sub': u', '3-u, '(R)Al(E)\u2003\u2003[Chemical Formula 7]'}, {'br': None, 'sup': 16', '17, 'sub': '2', '(R)AlOR\u2003\u2003[Chemical Formula 8]'}, {'br': None, 'sup': 16', ...

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25-04-2019 дата публикации

Abs molding composition having improved crack and chemical resistance and its use

Номер: US20190119487A1
Принадлежит: INEOS STYROLUTION GROUP GMBH

Thermoplastic molding composition scan be advantageously used in hydrofluoro olefin containing areas, comprising components A, B, C and, D: 10 to 35 wt.-% ABS graft rubber A obtained by emulsion polymerization, 50 to 75 wt.-% SAN copolymer B, 4 to 20 wt.-% copolymer C from ethylene and C1-C6-alkyl(meth)acrylate, and 4 to 20 wt.-% ABS graft rubber copolymer D obtained by mass polymerization.

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16-04-2020 дата публикации

Olefin Polymer, Preparation Method of the Same, and Film Using the Same

Номер: US20200115475A1
Принадлежит: LG Chem Ltd

An olefin polymer capable of simultaneously satisfying excellent drop impact strength and transparency, a preparation method of the same, and a film using the same, can be provided. In an embodiment, an olefin polymer comprises a plurality of polymer chains, and satisfies the following conditions: i) each polymer chain of the plurality having an average number of short chain branches (SCBs) per 1000 carbon atoms of 20/1000C or more, wherein an SCB has C2 to C7 carbon atoms, ii) a molded film of the olefin polymer having a drop impact strength of 1500 g to 2400 g as measured in accordance with ASTM D1709A, wherein the molded film having a thickness of 100 μm, and iii) a molded film of the olefin polymer having a haze is 10% to 30% as measured in accordance with ASTM D1003, wherein the molded film having a thickness of 0.05 mm.

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27-05-2021 дата публикации

USE OF HYDROGEN PEROXIDE IN SOLID FORM TO MODIFY THE RHEOLOGY OF A THERMOPLASTIC POLYMER WHEN MELTED

Номер: US20210155770A1
Принадлежит:

The invention relates to the use of at least one hydrogen peroxide in solid form to modify the rheology of a thermoplastic polymer when melted, specifically a polyolefin and particularly a polymer comprising at least one unit from propylene and, more particularly, polypropylene. The invention also relates to a method for modifying the rheology of a thermoplastic polymer when melted, specifically reducing viscosity when melted. 120-. (canceled)21. A process for modifying the melt rheology of a thermoplastic polymer comprising at least one step of mixing said polymer and hydrogen peroxide in solid form.22. The process of claim 21 , wherein modifying the melt rheology of the thermoplastic polymer comprises modifying one or more melt rheological properties of the thermoplastic polymer.23. The process of claim 22 , wherein the one or more melt rheological properties are chosen from the group consisting of the melt flow index (MFI) claim 22 , the melt viscosity claim 22 , the molecular weight claim 22 , the molecular weight distribution and the polydispersity index.24. The process of claim 21 , wherein the thermoplastic polymer is a polymer comprising at least one unit derived from propylene.25. The process of claim 21 , wherein the thermoplastic polymer is chosen from the group consisting of polypropylene and propylene copolymers comprising in their structure at least 50 mol % of units derived from propylene and at least one unit derived from an ethylenically unsaturated monomer other than propylene.26. The process of claim 21 , wherein the thermoplastic polymer is polypropylene.27. The process of claim 21 , wherein the hydrogen peroxide in solid form is chosen from the group consisting of sodium percarbonate (2NaCO.3HO) claim 21 , urea-hydrogen peroxide (HO—CO(NH)) claim 21 , hydrogen peroxide adsorbed on a solid support and mixtures thereof.28. The process of claim 21 , wherein the hydrogen peroxide in solid form is sodium percarbonate (2NaCO.3HO).29. The process of ...

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10-05-2018 дата публикации

ETHYLENE-BASED POLYMERS WITH LOW HEXANE EXTRACTABLES

Номер: US20180127523A1
Принадлежит:

The invention provides an ethylene homopolymer formed from a free-radical, high pressure polymerization process in a tubular reactor system, said homopolymer comprising the following properties: (A) a density from 0.9190 to 0.9250 g/cc; (B) a hexane extractable level that is less than, or equal to, 2.6 wt %, based on the total weight of the polymer; (C) a G′ (at G″=500 Pa, 170 C) that meets the following equation: G′≥D+E[log (I2)], where D=150 Pa and E=−60 Pa/[log(dg/min)]; and (D) a melt in dex (I2) from 1.0 to 20 dg/min. 1. An ethylene homopolymer formed from a free-radical , high pressure polymerization process in a tubular reactor system , said homopolymer comprising the following properties:(A) a density from 0.9190 to 0.9250 g/cc;(B) a hexane extractable level that is less than, or equal to, 2.6 wt %, based on the total weight of the polymer;(C) a G′ (at G″=500 Pa, 170° C.) that meets the following equation: G′≥D+E[log (I2)], where D=150 Pa and E=−60 Pa/[log(dg/min)]; and(D) a melt index (I2) from 1.0 to 20 dg/min.2. The ethylene homopolymer of claim 1 , wherein a hexane extractable level that is greater than the lower of one of the following:(1) (A+(B*density (g/cc))+(C*log (MI) dg/min)), based on total weight of the ethylene-based polymer; where A=250.5 wt %, B=−270 wt %/(g/cc), C=0.25 wt %/[log(dg/min)], or(2) 2.0 wt %, based on the total weight of the polymer.3. The ethylene homopolymer of claim 1 , wherein the polymer has a vinyl content less than claim 1 , or equal to claim 1 , 0.15 vinyl groups per 1000 total carbons.4. A process for producing the ethylene homopolymer of claim 1 , the process comprising polymerizing a reaction mixture comprising ethylene and at least one free radical claim 1 , in a reaction configuration claim 1 , comprising a first tubular reaction zone 1 and a last tubular reaction zone i claim 1 , in which i is greater than claim 1 , or equal to claim 1 , (≥) 3 claim 1 , and under high pressure polymerization conditions claim 1 , and ...

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10-05-2018 дата публикации

Dual Catalyst System for Producing LLDPE Copolymers with a Narrow Molecular Weight Distribution and Improved Processability

Номер: US20180127526A1
Принадлежит: Chevron Phillips Chemical Co LP

Disclosed herein are ethylene-based polymers generally characterized by a Mw ranging from 70,000 to 200,000 g/mol, a ratio of Mz/Mw ranging from 1.8 to 20, an IB parameter ranging from 0.92 to 1.05, and an ATREF profile characterized by one large peak. These polymers have the dart impact, tear strength, and optical properties of a metallocene-catalyzed LLDPE, but with improved processability, melt strength, and bubble stability, and can be used in blown film and other end-use applications.

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10-05-2018 дата публикации

SMOOTHNESS IMPROVING ADDITIVE FOR CALENDERING PROCESS

Номер: US20180127528A1
Принадлежит: LG MMA CORP.

Provided are a smoothness improving additive for a calendering process and a polyvinylchloride-based composition including the same. More particularly, a smoothness improving additive allowing, even in the case of using a plasticizer in a smaller amount than the conventional amount used, excellent productivity and excellent processability in a calendering process to accelerate a production speed, excellent mechanical physical properties such as glass transition temperature and tensile strength of a molded body, and manufacture of a molded body having better smoothness is provided. 1. A smoothness improving additive for a calendering process , comprising:a methylmethacrylate-based polymer having a weight average molecular weight of 16,000 to 48,000 g/mol and a melt index of 0.2 to 15 g/10 min, measured at 170° C. under 3.8 kg.2. The smoothness improving additive of claim 1 , wherein the methylmethacrylate-based polymer is any one resin or a mixed resin of two or more selected from the group consisting of a methylmethacrylate homopolymer and a methylmethacrylate copolymer.3. The smoothness improving additive of claim 1 , wherein the methylmethacrylate-based polymer has a glass transition temperature of 90° C. or more.4. The smoothness improving additive of claim 1 , wherein the smoothness improving additive is used in a calendering process of polyvinylchloride-based flooring.5. A base layer for polyvinylchloride-based flooring claim 1 , comprising the smoothness improving additive of .6. The base layer of claim 5 , wherein the base layer has a thickness of 1.0 to 5.0 mm.7. The smoothness improving additive of claim 2 , wherein the smoothness improving additive is used in a calendering process of polyvinylchloride-based flooring.8. A base layer for polyvinylchloride-based flooring claim 2 , comprising the smoothness improving additive of .9. The smoothness improving additive of claim 3 , wherein the smoothness improving additive is used in a calendering process of ...

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02-05-2019 дата публикации

POLYETHYLENE MATERIAL AND APPLICATION THEREOF

Номер: US20190127501A1
Принадлежит:

Provided is a polyethylene material and application thereof. A density distribution of the polyethylene material is in a range of 0.880 g/cm-0.960 g/cm. An amount of a fraction at a temperature of 40° C. obtained by conducting temperature rising elution fractionation on the polyethylene material is in a range of 9.0 wt %-40.0 wt %, preferably in a range of 10.0 wt %-25.0 wt %, more preferably in a range of 9.9 wt %-20.0 wt %. A melting temperature of the polyethylene material is 110° C.-135° C., preferably 116° C.-130° C. The polyethylene material provided by the present application has distinctly improved amount of medium/low-molecular-weight fractions and high-degree-branching fractions, as well as relatively high-molecular-weight fractions which are highly branched. The polyethylene material thus has a relative high melting temperature. 1. A polyethylene material , having a density distribution in a range of 0.880 g/cm3-0.960 g/cm3; an amount of a fraction at a temperature of 40° C. in a range of 9.0 wt %-40.0 wt % , preferably in a range of 10.0 wt %-25.0 wt % , more preferably in a range of 9.9 wt %-20.0 wt % , as determined by conducting temperature rising elution fractionation on the polyethylene material , a melting temperature of the polyethylene material is in a range of 110° C.-135° C. , preferably in a range of 116° C.-130° C.2. The polyethylene material according to claim 1 , wherein the polyethylene material has an amount of a fraction at a temperature of 110° C. in a range of 8.0 wt %-30.0 wt % claim 1 , preferably in a range of 9.0 wt %-18.0 wt %.3. The polyethylene material according to claim 1 , wherein as determined by temperature rising elution fractionation claim 1 , a standard deviation of amounts of two fractions of the polyethylene material at temperatures at an interval of 10° C. from 40° C. to 110° C. is in a range of 0%-6.0% claim 1 , preferably in a range of 0.5%-3.5%.4. The polyethylene material according to claim 1 , wherein a number- ...

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02-05-2019 дата публикации

Olefin-Block Copolymers and their use in Elastomeric Articles

Номер: US20190127561A1
Принадлежит:

An elastomeric article comprising an olefin-block copolymer comprising within a range from 4 to 40 mol % of C4 to C12 α-olefin derived units, the remainder being ethylene-derived units, wherein the melting point temperature (T) is within a range from 92° C. to 120° C., and having an M/Mvalue of less than 2.5. The olefin-block copolymer is desirably generated by combining ethylene, C4 to C12 α-olefins, a single site catalyst, preferably a fluxional catalyst, and an activator. The elastomeric article may be an elastic hygiene garment, especially a garment comprising a waistband, stretch ear panels and/or belly bands. 1. An elastomeric article comprising an olefin-block copolymer comprising within a range from 4 to 40 mol % of C4 to C12 α-olefin derived units , the remainder being ethylene-derived units , wherein the melting point temperature (T) is within a range from 92° C. to 120° C. , and having an M/Mvalue of less than 2.5.2. The elastomeric article of claim 1 , wherein the olefin-block copolymer is generated by combining ethylene claim 1 , C4 to C12 α-olefins claim 1 , a single-site catalyst claim 1 , and an activator.3. The elastomeric article of claim 1 , wherein the olefin-block copolymer has a Mwithin a range from 100 claim 1 ,000 g/mole to 300 claim 1 ,000 g/mole and a melt index (MI) of less than 1.4 g/10 min.4. The elastomeric article of claim 1 , wherein the olefin-block copolymer has a peak melting point temperature (T) within a range from 92° C. to 110° C. within a range of 4 mol % to 20 mol % overall comonomer content.5. The elastomeric article of claim 1 , wherein the C4 to C12 α-olefin rich blocks comprise within a range from 20 mol % to 80 mol % C4 to C12 α-olefin derived units claim 1 , and wherein the C4 to C12 α-olefin poor blocks comprise within a range from 40 mol % to 5 mol % C4 to C12 α-olefin derived units.6. The elastomeric article of claim 1 , wherein the C4 to C12 α-olefin derived units comprise 1-hexene or 1-octene claim 1 , preferably 1 ...

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03-06-2021 дата публикации

A polyethylene with a high vinyl content and beneficial rheological properties

Номер: US20210163644A1
Принадлежит: Borealis AG

The invention relates to a polyethylene which contains a total amount of vinyl groups which is B vinyl groups per 1000 carbon atoms, and B1≤B, wherein B1 is 0.30; and has a complex viscosity (η*) at 0.05 rad/sec, which is X Pas, and X1≤X≤X2, wherein X1 is 10000 and X2 is 30000; and has a complex viscosity (η*) at 300 rad/sec, which is Y Pas, and Y1≤Y≤Y2, wherein Y1 is 5 and Y2 is 350, both complex viscosities (η*) are determined according to method ISO 6721-1 on stabilised samples of the polyethylene, a polymer composition, an article being e.g. a cable, e.g. a power cable, and processes for producing a polyethylene, a polymer composition and an article, and an article; useful in different end applications, such as wire and cable (W&C) applications.

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18-05-2017 дата публикации

GOLF BALL RESIN COMPOSITION AND GOLF BALL

Номер: US20170136309A1
Принадлежит: DUNLOP SPORTS CO., LTD.

An object of the present invention is to provide a golf ball resin composition having an excellent rebound resilience. The present invention provides a golf ball resin composition containing an ionomer resin as a resin component. In a DSC measurement (a measuring atmosphere: a nitrogen atmosphere, a measuring temperature range: from −50° C. to 150° C., and a temperature rising rate: 10° C./min) of the golf ball resin composition of the first embodiment, a first endothermic peak and a second endothermic peak appear, and a peak top temperature (Ti) of the first endothermic peak is equal to or lower than a peak top temperature (Tm) of the second endothermic peak and the peak top temperature (Ti) ranges from 60° C. to 70° C. 1. A golf ball resin composition containing (A1) a metal ion-neutralized product of a binary copolymer composed of an olefin and an α ,β-unsaturated carboxylic acid having 3 to 8 carbon atoms , and/or (A2) a metal ion-neutralized product of a ternary copolymer composed of an olefin , an α ,β-unsaturated carboxylic acid having 3 to 8 carbon atoms and an α ,β-unsaturated carboxylic acid ester as a resin component , wherein in a DSC measurement (a measuring atmosphere: a nitrogen atmosphere , a measuring temperature range: from −50° C. to 150° C. , and a temperature rising rate: 10° C./min) of the golf ball resin composition , a first endothermic peak and a second endothermic peak appear , and a peak top temperature (Ti) of the first endothermic peak is equal to or lower than a peak top temperature (Tm) of the second endothermic peak and the peak top temperature (Ti) ranges from 60° C. to 70° C.2. The golf ball resin composition according to claim 1 , wherein a hyperfine coupling constant (A) of the golf ball resin composition ranges from 31.6 G to 35.0 G claim 1 , measured by a spin probe-electron spin resonance method (spin probe: 5-doxylstearic acid).3. The golf ball resin composition according to claim 2 , wherein the resin component contains a ...

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09-05-2019 дата публикации

NON-STRETCHED POLYPROPYLENE-BASED FILM

Номер: US20190135962A1
Принадлежит:

The polypropylene copolymer according to the present invention has a low melting point and also is excellent in the low temperature heat sealing effect, transparency and strength, and the film prepared therefrom can be effectively used as a sealing layer of the non-stretched polypropylene-based film. 1. A polypropylene-based film comprising a propylene-ethylene-1-butene terpolymer which has a melting point (Tm) of 125 to 135° C. , a molecular weight distribution (Mw/Mn , PDI) of 2.3 to 3.5 , and a xylene soluble (Xs) content of 2.0 wt % or less ,wherein the terpolymer has a crystallization temperature (Tc) of 75 to 87° C., andwherein, when heat-sealed at 134° C. and 0.2 MPa for 1 second, a sealing strength is 300 to 500 g/15 mm.2. The polypropylene-based film according to claim 1 , which comprises a sealing layer comprising the terpolymer.3. The polypropylene-based film according to claim 2 , which further comprises a polypropylene-based core layer and a skin layer which are sequentially formed on the sealing layer.4. (canceled)5. (canceled)7. The polypropylene-based film according to claim 6 , wherein X is chloro.8. The polypropylene-based film according to claim 6 , wherein Ris phenyl substituted by tert-butyl.9. The polypropylene-based film according to claim 6 , wherein R claim 6 , Rand Rare hydrogen.10. The polypropylene-based film according to wherein A is silicon.11. The polypropylene-based film according to claim 6 , wherein Ris 6-tert-butoxy-hexyl claim 6 , and Ris methyl.13. The polypropylene-based film according to wherein the sealing layer further comprises a propylene-based elastomer. This application claims the benefit of Korean Patent Application No. 10-2014-0173004 filed on Dec. 4, 2014 with the Korean Intellectual Property Office, the disclosure of which is herein incorporated by reference in its entirety.The present invention relates to a non-stretched polypropylene-based film, having a low xylene soluble content and capable of allowing sufficient ...

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09-05-2019 дата публикации

Crosslinked polymer composition for cable accessories

Номер: US20190136022A1
Принадлежит: Borealis AG

A crosslinked polymer composition based on a plastomer, which is suitable for producing at least one layer of cable accessories like cable joints, bushings or terminations; its use for preparing such a layer and the cable accessory comprising the composition.

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09-05-2019 дата публикации

Poly(phenylene ether) composition, lined pipe and injection molded article prepared therefrom, and method of controlling microbial growth during water transportation and storage

Номер: US20190136032A1
Принадлежит: SABIC Global Technologies BV

A lined pipe includes an outer layer and an inner layer. The outer layer contains crosslinked polyethylene, polypropylene, poly(1-butene), or poly(vinyl chloride). The inner layer contains poly(phenylene ether), polystyrene, and, optionally, a hydrogenated block copolymer. The inner layer exhibits low stimulation of bacterial growth. Also described are a composition exhibiting low stimulation of bacterial growth, an injection molded article, and a method of controlling microbial growth during transportation or storage of water.

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