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Применить Всего найдено 5792. Отображено 200.
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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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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03-02-2020 дата публикации

СИСТЕМА ОТБОРА ПРОБ ИЗ ЖИДКО-ТВЕРДОЙ СМЕСИ ДЛЯ ПЕТЛЕВОГО СУСПЕНЗИОННОГО РЕАКТОРА

Номер: RU2712952C2

Изобретение относится к способу и системе измерения характеристик жидкости в двухфазной смеси жидкой и твердой фаз. Описан способ эксплуатации системы, содержащей единственный петлевой суспензионный реактор-полимеризатор или два или более петлевых суспензионных реактора-полимеризатора с интегрированными системами отбора проб смеси жидкой и твердой фаз. Также описаны система и способ измерения характеристик смеси жидкой и твердой фаз жидкости в сосуде. Технический результат - быстрое и эффективное разделение твердой и жидкой фаз с обеспечением потока жидкости, свободного от твердых частиц, которые могут закупоривать или отрицательно влиять на аналитическое оборудование. 3 н. и 17 з.п. ф-лы, 2 ил., 1 табл.

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08-04-2019 дата публикации

ИНГИБИТОРЫ КОРРОЗИИ ДЛЯ ТОПЛИВА И СМАЗОЧНЫХ МАТЕРИАЛОВ

Номер: RU2684323C2
Принадлежит: БАСФ СЕ (DE)

Изобретение раскрывает применение полимеров, которые статистически в среднем имеют по меньшей мере 4 кислотные группы на полимерную цепь, соотношение атомов углерода на кислотную группу от 7 до 35 и кислотное число от 80 до 320 мг КОН/г, определенное при помощи потенциографического титрования с 0,5-молярной водной соляной кислотой после трехчасового нагревания в 0,5-молярном этанольном растворе едкого калия, в качестве ингибиторов коррозии в топливах, которые имеют содержание щелочных и/или щелочно-земельных металлов и/или цинка по меньшей мере 0,1 мас.ч./млн, причем топливо представляет собой дизельное или бензиновое топливо. Также раскрывается применение полимеров в наборах присадок для снижения коррозии в дизельных и бензиновых топливах, которые имеют содержание щелочных и/или щелочно-земельных металлов и/или цинка по меньшей мере 0,1 мас.ч./млн. Технический результат заключается в снижении коррозии. 3 н. и 11 з.п. ф-лы, 1 ил., 3 пр., 9 табл.

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12-12-2019 дата публикации

УПРАВЛЕНИЕ ТЕМПЕРАТУРОЙ ПРИ ПОЛИМЕРИЗАЦИИ ЧАСТИЦ ПОЛИОЛЕФИНОВ

Номер: RU2708889C2

Изобретение относится к передаче тепла в системе реактора полимеризации. Описан способ, включающий контактирование олефина с катализатором в реакторе полимеризации. Проводят полимеризацию по меньшей мере части олефина с образованием альфа-олефинового продукта реакции, затем проводят обнаружение условия в реакторе полимеризации, определяют среднюю температуру по меньшей мере одной частицы олефинового продукта на основании условия, определяют порог рабочей температуры частиц с использованием кривой обрастания, сравнивают среднюю температуру полимерной частицы с порогом рабочей температуры частиц, изменяют один или более рабочих параметров в ответ на сравнение и поддерживают среднюю температуру по меньшей мере одной частицы олефинового полимера не выше порога рабочей температуры частиц в ответ на изменение одного или более рабочих параметров. Альфа-олефиновый продукт реакции содержит множество частиц олефинового полимера, и реактор полимеризации содержит реакционную смесь, которая содержит ...

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21-01-2022 дата публикации

СПОСОБ ПРОИЗВОДСТВА ПОЛИМЕРОВ ИЗОБУТЕНА С УЛУЧШЕННЫМ РЕГУЛИРОВАНИЕМ ТЕМПЕРАТУРЫ

Номер: RU2764774C2

Настоящее изобретение относится к способу получения изоолефиновых полимеров. Данный способ включает стадии: а) приготовления реакционной среды, содержащей органический разбавитель и по меньшей мере один мономер, являющийся изоолефином, и этан или диоксид углерода, который по существу растворен в реакционной среде, причём этан или диоксид углерода присутствует в реакционной среде в количестве от 5,0 до 11,0 мас.%, и b) полимеризации по меньшей мере одного мономера в реакционной среде в присутствии инициирующей системы с получением конечной среды, содержащей сополимер, органический разбавитель и необязательно остаточные мономеры, при этом этан или диоксид углерода реакционной среды по меньшей мере частично испаряют. Технический результат – разработка способа получения высококачественных изоолефиновых полимеров с превосходным регулированием температуры в крупномасштабном промышленном производстве. 20 з.п. ф-лы, 5 пр.

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18-08-2020 дата публикации

Номер: RU2018143975A3
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29-01-2020 дата публикации

Номер: RU2018121643A3
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31-10-2018 дата публикации

Номер: RU2016146802A3
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29-04-2019 дата публикации

Номер: RU2017127030A3
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25-06-2020 дата публикации

Номер: RU2018145528A3
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07-11-2018 дата публикации

Номер: RU2017114392A3
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02-02-2021 дата публикации

Номер: RU2019112843A3
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17-07-2019 дата публикации

Номер: RU2017141782A3
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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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09-07-2024 дата публикации

ОГНЕСТОЙКИЙ АНТИБАКТЕРИАЛЬНЫЙ АГЕНТ, СПОСОБ ЕГО ПОЛУЧЕНИЯ И ПРИМЕНЕНИЯ И КОМПОЗИЦИЯ ИЗ ОГНЕСТОЙКОЙ АНТИБАКТЕРИАЛЬНОЙ ТЕРМОПЛАСТИЧНОЙ СМОЛЫ

Номер: RU2822574C1

Группа изобретений относится к огнестойкому антибактериальному агенту, способу его получения и его применению, а также к огнестойкой антибактериальной термопластичной смоляной композиции. Огнестойкий антибактериальный агент представляет собой полимерную микросферу с привитой на ее поверхность гуанидиновой солью, при этом полимерная микросфера содержит сшитую структуру, состоящую из структурного звена А, полученного из малеинового ангидрида, структурного звена В, полученного из мономера М, и структурного звена С, полученного из сшивающего агента. Мономер M выбирают из C4-C9 алифатического олефина или его смеси, гуанидиновая соль содержит по меньшей мере одну гуанидиновую соль, обладающую свойством огнестойкости. Технический результат – обеспечение огнестойкого антибактериального агента, обладающего как антибактериальной эффективностью, так и свойствами огнестойкости и также обладающего дисперсностью, текучестью, низким влагопоглощением. Огнестойкая антибактериальная термопластичная смоляная ...

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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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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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10-07-2012 дата публикации

ПРОИЗВОЛЬНЫЙ СОПОЛИМЕР ПРОПИЛЕН-ГЕКСЕНА, ПОЛУЧЕННЫЙ ПРИ ПОМОЩИ КАТАЛИЗАТОРА ЦИГЛЕРА-НАТТА

Номер: RU2010148526A
Принадлежит:

... 1. Сополимер пропилена (А), ! (a) в состав которого в качестве сомономера входит, по крайней мере, 1-гексен, л ! (b) с массовым содержанием сополимера в диапазоне от 1,0 до 3,0%, ! (c) с массовым содержанием растворимой в ксилоле фракции, равным или меньше 2,5%, и ! (d) с частичной кристаллизацией в β-модификации. ! 2. Сополимер пропилена по п.1, отличающийся тем, что в состав полимера (А) входит β-зародышеобразующий агент (В). !3. Сополимер пропилена (А) ! (a) в состав которого в качестве сомономера входит, по крайней мере, 1-гексен, ! (b) с массовым содержанием сополимера в диапазоне от 1,0 до 3,0%, ! (c) с массовым содержанием растворимой в ксилоле фракции, равным или меньше 2,5%, и ! (d) с частичной кристаллизацией в β-модификации. ! 4. Сополимер пропилена по п.3, отличающийся тем, что сополимер (А) частично кристаллизован в β-модификации. ! 5. Сополимер пропилена (А) по одному из предыдущих пунктов, отличающийся тем, что скорость течения расплава MFR2 (230°C) сополимера пропилена ( ...

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20-07-1996 дата публикации

ПОЛИМЕРЫ И АДДИТИВНЫЕ КОМПОЗИЦИИ

Номер: RU94045929A
Принадлежит:

Гомополимеры или сополимеры, полученные из одного или большего числа альфа-олефинов, имеющих среднечисленную мол. м. до 15000 и изотактичность 75% или выше, и их применение в качестве присадок, улучшающих холодное течение в сырой нефти, нефтяных топливах или смазочных маслах.

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20-03-2012 дата публикации

РЕГУЛИРОВАНИЕ УРОВНЯ РАЗВЕТВЛЕНИЯ И ВЯЗКОСТИ ПОЛИ-АЛЬФА-ОЛЕФИНОВ ПОСРЕДСТВОМ ВВЕДЕНИЯ ПРОПЕНА

Номер: RU2010136927A
Принадлежит:

... 1. Поли-альфа-олефин, полученный из децена и пропена, и имеющий уровень разветвления более чем 19%. ! 2. Поли-альфа-олефин по п.1, имеющий кинематическую вязкость от 20 до 1000 Ст при 100°С. ! 3. Поли-альфа-олефин по п.1, где поли-альфа-олефин имеет вязкость по Брукфилду при -40°С, в случае приготовленного состава в виде смеси SAE 90, менее чем 45000 сП. ! 4. Поли-альфа-олефин по п.1, где поли-альфа-олефин имеет температуру потери текучести, которая составляет менее чем -30°С. ! 5. Поли-альфа-олефин по п.1, где децен включает 1-децен. ! 6. Способ получения поли-альфа-олефина, где способ включает стадию полимеризации, по меньшей мере, двух мономеров в реакционной смеси с образованием поли-альфа-олефина, где два мономера включают децен, предпочтительно 1-децен, и пропен в присутствии металлоценового катализатора такого как Ph2C(Cp-9-Flu)ZrCl, и алюмоксанового со-катализатора, предпочтительно алкилалюмоксанового со-катализатора, предпочтительно метилалюмоксана, где поли-альфа-олефин имеет ...

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10-10-2013 дата публикации

ДВУХСТАДИЙНЫЙ СПОСОБ И УСТРОЙСТВО ДЛЯ ПРОИЗВОДСТВА ВЫСОКОВЯЗКИХ ПОЛИ-α-ОЛЕФИНОВ

Номер: RU2012111831A
Принадлежит:

... 1. Способ получения конечного полимерного продукта, включающий:(a) полимеризацию первого олефинового мономера в первой реакционной зоне в присутствии каталитической системы, включающей катализатор, для получения вытекающего потока, который содержит первый полимер, имеющий первую вязкость, и активированный катализатор; и(b) подачу первого вытекающего потока или его части из первой реакционной зоны во вторую реакционную зону и полимеризацию второго олефинового мономера во второй реакционной зоне в присутствии первого полимера и катализатора, для получения конечного полимерного продукта, имеющего вторую вязкость,где первый олефиновый мономер и второй олефиновый мономер включают α-олефиновые мономеры, содержащие от 2 до 20 атомов углерода, предпочтительно от 8 до 12 атомов углерода, наиболее предпочтительно 1-децен.2. Способ по п.1, в котором первый олефиновый мономер и второй олефиновый мономер имеют одинаковые составы.3. Способ по п.1, в который дополнительно включена стадия:(c) загрузки ...

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27-08-2014 дата публикации

СИСТЕМЫ И СПОСОБЫ ИЗМЕРЕНИЯ НАКОПЛЕНИЯ ЧАСТИЦ НА ПОВЕРХНОСТЯХ РЕАКТОРА

Номер: RU2013106690A
Принадлежит:

... 1. Способ мониторинга смеси частиц и текучей среды, в котором: пропускают смесь, содержащую заряженные частицы и текучую среду, обтекая детектор накопления частиц;измеряют электрические сигналы, зарегистрированные детектором в то время, как некоторые заряженные частицы проходят мимо детектора без контакта с ним, а другие заряженные частицы контактируют с детектором;обрабатывают измеренный электрический сигнал, обеспечивая выходные данные; иопределяют по выходным данным, имеют ли заряженные частицы, контактирующие с детектором, в среднем заряд, отличный от заряженных частиц, проходящих мимо детектора без контакта с ним.2. Способ по п.1, в котором обработка измеренного электрического сигнала включает применение метода абсолютной автокорреляции к измеренному электрическому сигналу и определение вектора абсолютной автокорреляции электрического сигнала.3. Способ по п.2, в котором абсолютная автокорреляция электрического сигнала включает кривую приближения, кривую удаления и кривую у нулевого ...

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01-07-1976 дата публикации

HARZMASSE

Номер: DE0002553955A1
Автор: MUSE JOEL, MUSE,JOEL
Принадлежит:

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12-11-1975 дата публикации

HYDROCARBON-DERIVED RESIN

Номер: GB0001413489A
Автор:
Принадлежит:

... 1413489 Adhesive coatings GOODYEAR TIRE & RUBBER CO 12 Dec 1972 [20 Jan 1972] 57266/72 Heading B2E [Also in Division C3] Tetrapolymer resins derived from piperylene, -methylstyrene, 2-methyl-2-butene and dicyclopentadiene are used in combination with (a) a natural or synthetic rubber to produce a pressure-sensitive adhesive or (b) a thermoplastic polymer (certain alphamonoolefin polymers) to produce a hot-melt adhesive. In the latter case part of the polymer may be replaced by paraffin wax and/or micro-crystalline wax. Examples refer to blends of the tetrapolymer with butadiene-styrene or natural rubber coated from solution on to a polyethylene terephthalate film and to blends with ethylene-vinyl acetate copolymer and paraffin wax coated from the melt on to corrugated cardboard.

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25-08-1965 дата публикации

Copolymers

Номер: GB0001002366A
Автор:
Принадлежит:

Copolymers are produced by contacting a mono-olefinically unsaturated hydrocarbon having a slower polymerization rate than isobutene, and one or more conjugated dienes, with a Friedel-Crafts catalyst in the presence of a minor proportion of isobutene. In the examples 4-methyl pentene-1 is copolymerized with isoprene in ethyl chloride solution in the presence of aluminium chloride and isobutene, and the reaction is terminated with methanol. Other dienes specified are butadiene- 4-methyl-1,3-pentadiene and 2-methyl-1,3-pentadiene.

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29-04-1992 дата публикации

POLYMERS AND ADDITIVE COMPOSITIONS

Номер: GB0009205996D0
Автор:
Принадлежит:

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18-03-2020 дата публикации

Chemical reactions

Номер: GB0202001371D0
Автор:
Принадлежит:

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12-01-1980 дата публикации

PROCEDURE FOR THE PRODUCTION OF PAPER GLUING MEANS

Номер: AT0000360335B
Автор:
Принадлежит:

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15-09-1981 дата публикации

PROCEDURE FOR THE PRODUCTION OF COPOLYMERS FROM MALEIC ACID ANHYDRIDE AND ALKENES.

Номер: AT0000000186T
Принадлежит:

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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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25-05-1995 дата публикации

Wax-containing release agent for thermally transferable inscription and decoration systems

Номер: AU0007599094A
Автор: NAME NOT GIVEN
Принадлежит:

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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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26-04-2018 дата публикации

Non-extrusion process for functionalization of low viscosity polyolefins

Номер: AU2016327574A1
Принадлежит: Phillips Ormonde Fitzpatrick

A process to form a first composition comprising a functionalized olefin-based polymer comprises: a) polymerizing a composition comprising an olefin to form a reaction product comprising an olefin-based polymer; b) subjecting at least a portion of the reaction product to at least one devolatilization to form a polymer-rich melt, wherein step b) occurs downstream from and in-line with step a); and c) reacting at least a portion of the polymer-rich melt with at least one functionalization agent and, optionally, at least one free-radical initiator to form the first composition, wherein step c) occurs downstream from and in-line with step b), wherein "the viscosity of the functionalized olefin-based polymer (177°C/350°F)" to "the viscosity of the olefin-based polymer (177°C/350°F)" is from 0.1 to 5.0.

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25-01-2007 дата публикации

POLYALPHA-OLEFIN COMPOSITIONS AND PROCESSES TO PRODUCE THE SAME

Номер: CA0002615982A1
Принадлежит:

This invention relates to a polyalpha-olefin (and hydrogenated analogs thereof) comprising more than 50 mole % of one or more C5 to C24 alpha-olefin monomers where the polyalpha-olefin has: a) 40 mole % or more of mm triads, b) a Bromine number of Y or greater, where Y is equal to 89.92 * (V)' ~5863, whre V is the Kinematic Viscosity of the polyalpha-olefin measured at 100~C in cSt, and c) 1,2 disubstituted olefins present at 7 mole % or more, preferably having Z mole % or more of units represented by the formula: where j, k and m are each, independently, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, or 22, n is an integer from 1 to 350, and where Z = 8.420*Log(V)-4.048, where V is the kinematic viscosity of the polyalpha-olefin measured at 1000C in cSt This invention also relates to process to produce such polyalpha-olefins.

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25-05-2010 дата публикации

PROCESS FOR PRODUCING LIQUID POLYALPHAOLEFIN POLYMER, METALLOCENE CATALYST THEREFORE AND LUBRICANTS CONTAINING SAME

Номер: CA0002416894C
Принадлежит: UNIROYAL CHEMICAL COMPANY, INC.

A liquid polyalphaolefin homo- or copolymer, preferably 1-decene, which is substantially amorphous is obtained by a polymerization process employing hydrogen and a particular type of metallocene catalyst. Additionally, liquid polyalphaolefin homo- or copolymer containing from 2 to about 12 carbon carbon atoms possess a unique combination of properties, i.e., low molecular weight (Mw), low polydispersity index (Mx/Mn), controllable kinematic viscosity (Kv100), low Iodine Number (I2) and low glass transition temperature (Tg) and are substantially amorphous. The liquid polyalphaolefin homo- or copolymers provided herein are useful for manufacturing a variety of products including lubricating oils in which the polyalphaolefin functions as a viscosity modifier.

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22-01-1980 дата публикации

HYDROCARBON-DERIVED RESINS OF PIPERYLENE AND METHYL BRANCHED TERTIARY IN HYDROCARBONS

Номер: CA1070335A

A hydrocarbon-derived resin having a softening point in the range of about 0.degree.C to about 25.degree.C derived from polymerizing piperylene and selected methyl branched tertiary olefins in the presence of boron trifluoride or boron trifluoride etherate. Such resins are particularly useful for the preparation of pressure sensitive adhesives, especially when such resins are mixed with other hydrocarbon-derived resins having high softening points in the range of about 80.degree.C to about 110.degree.C.

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01-11-1988 дата публикации

COPOLYMERS OF .alpha.-OLEFIN AND ALKYLENE CARBOXYLIC ACIDS

Номер: CA1244194A

A method for viscosifying control of an organic liquid which comprises adding a sufficient of a copolymer to such organic liquid to increase the viscosifying of such organic liquid, said copolymer having the formula: wherein R1 is an alkyl group having 1 to 25 carbon atoms, R2 is an alkylene group having 3 to 17 carbon atoms, z is a hydrogen a mixture of hydrogen and an alkyl group having 1 to 25 carbon atoms, x is 95.0 to 99.95 mole % and y is .05 to 5.0 mole %, and additionally this copolymer can be complexed with an amine containing polymer, wherein the complex functions as viscosification agent.

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12-01-1993 дата публикации

CYCLO-OLEFINIC RANDOM COPOLYMER, OLEFINIC RANDOM COPOLYMER, AND PROCESS FOR PRODUCING CYCLO-OLEFINIC RANDOM COPOLYMERS

Номер: CA0001312695C

A cyclo-olefinic random copolymer composed of an alpha-olefin component having 3 to 20 carbon atoms and a cyclo-olefin component, (i) said copolymer containing 5 to 99 mole% of recurring units derived from said alpha-olefin component having 3 to 20 carbon atoms and 1 to 95 mole% of recurring units derived from said cyclo-olefin component, and (ii) said copolymer having an intrinsic viscosity ¢?!, measured in decalin at 135 .degree.C, of from 0.01 to 10 dl/g; and an olefinic random copolymer composed o component having 3 to 20 carbon atoms and (B) a cyclic polyene component and as required, (C) a cyclo-olefin component, (i) said copolymer containing S to 99 mole% of recurring units derived from said alpha-olefin component (A) having 3 to 20 carbon atoms and 1 to 95 mole% of recurring units derived from said cyclic polyene component SB) and 0 to 90 mole% of recurring units derived from said cyclo-olefin component (C), and (ii) said copolymer having an intrinsic viscosity ¢?!, measured in ...

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14-05-2020 дата публикации

METHOD OF OLEFIN POLYMERIZATION USING ALKANE-SOLUBLE NON-METALLOCENE PRECATALYST

Номер: CA3118441A1
Принадлежит:

A method of polymerizing an olefin monomer to make a polyolefin composition comprising a polyolefin polymer, the method comprising contacting a solution of an alkane-soluble non-metallocene precatalyst dissolved in an alkane solvent with an activator so as to make a trim catalyst comprising an alkane-soluble non-metallocene catalyst, feeding the trim catalyst, as a solution in an alkane solvent or supported on a support material as a dry powder or a slurry thereof in an alkane solvent, into a polymerization reactor, and polymerizing the olefin monomer with the trim catalyst in the polymerization reactor, thereby making the polyolefin composition.

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11-10-2018 дата публикации

CATALYST SYSTEMS CONTAINING LOW VALENT TITANIUM-ALUMINUM COMPLEXES AND POLYMERS PRODUCED THEREFROM

Номер: CA0003056440A1
Принадлежит: FINLAYSON & SINGLEHURST

Disclosed herein are methods for synthesizing low valence, titanium-aluminum complexes from half-metallocene titanium compounds and alkylaluminum compounds. The titanium-aluminum complexes can be used as components in catalyst systems for the polymerization of olefins.

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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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29-10-2019 дата публикации

METHODS FOR CONTROLLING DIE SWELL IN DUAL CATALYST OLEFIN POLYMERIZATION SYSTEMS

Номер: CA0002997123C

Methods for controlling the die swell of an olefin polymer produced using a dual catalyst system are disclosed. The die swell of the olefin polymer can be increased or decreased as a function of the catalyst weight ratio and the reactant molar ratio used during the olefin polymerization process.

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29-06-2017 дата публикации

IN-LINE BLENDING PROCESS

Номер: CA0003005940A1
Принадлежит:

An in-line blending process for polymers comprising: (a) providing two or more reactor-low pressure separator units (1,7) in parallel configuration, each reactor-low pressure separator unit comprising one reactor (2,8) fluidly connected to one low pressure separator (3,9) downstream and further a recycling line (5,11) connecting the low pressure separator (3,9) back to the corresponding reactor (2,8); (b) polymerizing olefin monomers having two or more carbon atoms in each of the reactors (2,8) in solution polymerisation; (c) forming an unreduced reactor effluents stream including a homogenous fluid phase polymer-monomer-solvent mixture in each of the reactors (2,8), (d) passing the unreduced reactor effluents streams from each of the reactors (2,8) through the corresponding low pressure separators (3,9), whereby the temperature and pressure of the low pressure separators (3,9) is adjusted such that a liquid phase and a vapour phase are obtained, whereby yielding a polymer-enriched liquid ...

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11-01-2020 дата публикации

POLYETHYLENE COMPOSITION AND FILM HAVING OUTSTANDING PROPERTIES

Номер: CA0003011031A1
Принадлежит: BAAR, CLIFF

A polyethylene composition comprises a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution M w/M n of < 2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 50,000 to 200,000 and a molecular weight distribution M w/M n of < 2.3, and a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 70,000 to 200,000 and a molecular weight distribution M w/M n of < 2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene. The polyethylene composition has a composition distribution breadth index, CDBI50 obtained from a crystallization elution fractionation (CEF) analysis of < 45 weight %. Film made from the polyethylene composition may have a machine direction 1% secant modulus of >=200 MPa (at a film thickness ...

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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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22-01-1980 дата публикации

HYDROCARBON-DERIVED RESINS OF PIPERYLENE AND METHYL BRANCHED TERTIARY IN HYDROCARBONS

Номер: CA0001070335A1
Принадлежит:

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13-12-2008 дата публикации

HIGH VISCOSITY LUBRICANT COPOLYMERS

Номер: CA0002634565A1
Принадлежит:

The invention pertains to a copolymer suitable for the use in or as a lubricant, which copolymer is consisting of an .alpha.-olefin and a di-ester of an .alpha.,.beta. ethylenically unsaturated dicarboxylic acid. More particularly, the inventio n pertains to a high molecular weight lubricating oil base fluid or additive comprising a copolymer of .alpha.-olefins with chain lengths for example fro m 12 to 18 carbon atoms and a di-ester of an .alpha.,.beta. ethylenically unsaturated dicarboxylic acid, with a C3-C7 alkylic alcohol, for example n-butanol, as esterifying component which is compatible with other low polar lubricating o il base fluids.

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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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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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20-08-2015 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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05-11-2015 дата публикации

COPOLYMER HAVING HIGH MULTIOLEFIN CONTENT

Номер: CA0002947046A1
Принадлежит:

A copolymer has high levels of multolefin incorporation. A process for producing the copolymer having high levels of multiolefin incorporation involves contacting at least one isoolefin monomer with at least one multiolefin and/or ß-pinene monomer in the presence of at least one Lewis acid and at least one initiator in a diluent. The diluent contains a hydrofluorinated olefin (HFO) comprising at least three carbon atoms and at least three fluorine atoms. Hydrofluorinated olefins used in the present invention are better diluents for butyl slurry cationic polymerization than saturated hydrofluorocarbons.

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07-09-2021 дата публикации

HIGH PERFORMANCE MOISTURE BARRIER FILMS AT LOWER DENSITIES

Номер: CA2947868C

A metallocene-catalyzed polyethylene copolymer having a zero shear viscosity (? ° ) of from about 1X102 Pa-s to about 5X103 Pa-s and a ratio of a z-average molecular weight to a number average molecular weight (Mz/Mn) of from about 4 to about 15, and when tested in accordance with ASTM F1249 displays a moisture vapor transmission rate of less than or equal to about 0.9 g-mil/100 in2/day. A metallocene-catalyzed polyethylene copolymer which when tested in accordance with ASTM F1249 has a moisture vapor transmission rate (MVTR) that is decreased by at least 5% when compared to an MVTR determined in accordance with ASTM F1249 of an otherwise similar metallocene-catalyzed polyethylene homopolymer.

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26-09-2009 дата публикации

PROCESS FOR SYNTHETIC LUBRICANT PRODUCTION

Номер: CA0002718879A1
Принадлежит:

A process for the preparation of oligomeric poly alpha-olefins includes oligomerizing low molecular weight PAO oligomer in the presence of a Lewis acid catalyst such as promoted aluminum trichloride or boron trifluoride under oligomerization conditions. The low molecular weight PAO oligomers used as a feed or feed component of the present process are the light olefinic by-product fractions including the dimers and light fractions from the metallocene-catalyzed PAO oligomerization process which are characterized by a molecular weight of 150 to 600 and a terminal olefin (vinylidene) content of at least 25%.

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05-05-2015 дата публикации

SHEAR-STABLE HIGH VISCOSITY POLYALPHAOLEFINS

Номер: CA0002806176C

A polyalphaolefin polymer, having a kinematic viscosity at 100° C of 135 cSt or greater, is shear stable. The polymer either has not more than 0.5 wt% of the polymer having a molecular weight of greater than 60,000 Daltons, or after being subjected to twenty hours of taper roller bearing testing, the polymer has a kinematic viscosity loss of less than 9%. Such a shear stable polyalphaolefin is obtained by either mechanical breakdown of a high viscosity polyalphaolefin or by a selective catalyst system used in oligomerization or polymerization of the feedstock.

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26-12-1978 дата публикации

RESINS AND POLYMER MIXTURES THEREOF

Номер: CA0001045294A1
Автор: MUSE JOEL
Принадлежит:

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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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25-11-1997 дата публикации

HIGHER -OLEFIN COPOLYMER, PROCESS FOR PREPARING SAME, VULCANIZATION PRODUCT THEREFOR AND VULCANIZABLE RUBBER COMPOSITION

Номер: CA0002028149C
Принадлежит: MITSUI PETROCHEMICAL IND

The higher .alpha.-olefin copolymers obtained in accordance with the present invention are copolymers derived from higher .alpha.-olefin and non-conjugated diene represented by the following general formula ¢I!, and (a) the non-conjugated diene content thereof is from 0.01 to 30 mol%, and (b) the intrinsic viscosity ¢~!, as measured in decaline at 135.degree.C, of said copolymer is from 1.0 to 10.0 dl/g. ... ¢I! The invention also provides a process for preparing such higher .alpha.-olefin copolymers as illustrated above, and vulcanization products obtained from said copolymers. Furthermore, the invention provides vulcanizable compositions containing rubber comprising of the above-mentioned higher .alpha.-olefin copolymers and a specific diene rubber or a specific ethylene/.alpha.-olefin copolymer rubber.

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11-11-1995 дата публикации

COPOLYMERS BASED ON ETHYLENICALLY UNSATURATED DICARBOXYLIC ANHYDRIDES, LONG-CHAIN OLEFINS AND FLUOROOLEFINS

Номер: CA0002148998A1
Принадлежит:

Copoltmers based on ethylenically unsaturated dicarboxylic anhydrides, long-chain olefins and fluoroolefins Copolymers containing 10 to 60% by weight of bivalent structural units of the formula A (A) wherein R1 and R2, independently of one another, are hydrogen or C1-C6-alkyl, a and b are zero or one and a + b is one, X and Y are identical or different and are the group -N-HR3, where R3 is C1-C40-alkyl, C3-C40-alkenyl, C5-C20-cyclo-alkyl or C6-C18-aryl, the group -N-(R3)2, where R3 are identical or different and have the abovementioned meaning, and/or the group -O-R4, where R4 is hydrogen, an alkali metal cation, one equivalent of an alkaline earth metal ion, a cation of the formula H2N?(R3)2 or H3N?R3, C1-C40-alkyl, C5-C20-cycloalkyl or C6-C18-aryl, 30 to 89% by weight of bivalent structural units of the formula B (B) wherein R5 is hydrogen or C1-C4-alkyl and R6 is C6-C40-alkyl or C6-C18-aryl, and 1 to 20% by weight of bivalent structural units of the formula C (C) wherein ...

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13-07-1995 дата публикации

NOVEL HYDROCARBON LUBE AND DISTILLATE FUEL ADDITIVE

Номер: CA0002179390A1
Принадлежит:

A hydrocarbon oligomer and a process for its production is disclosed that is useful as a pour point depressant and as a combination pour point depressant and viscosity index improver for mineral oil or synthetic oil. The oligomer is also useful in modifying wax crystal formation at low temperature when added to distillate fuels. The oligomer is a near linear copolymer of a mixture of ethylene and C3-C28 1-alkenes, or only 1-alkenes, wherein a large proportion of the pendant alkyl groups of the recurring 1-alkene monomer units contain between 14 and 22 carbon atoms. The oligomer is produced by polymerization of mixed 1-alkenes with reduced chromium oxide catalyst on silica support.

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01-02-2000 дата публикации

ETHYLENE POLYMERS HAVING SUPERIOR CLARITY, ENHANCED TOUGHNESS, LOW EXTRACTABLES AND PROCESSING EASE

Номер: CA0002173005C

Ethylene polymers having a Polydispersity Index of about 2 to about 4; a melt index, MI, and Relaxation Spectrum Index, RSI, such that (RSI)(MI0.6) is about 2.5 to about 6.5; c) a Crystallizable Chain Length Distribution Index, Lw/Ln, of about 1.0 to about 9; and d) a density, ?, and a percent haze when fabricated into films such that the percent haze is less than 370? - 330, are provided. These ethylene polymers advantageously combine superior clarity and toughness with low extractables and enhanced processing ease.

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16-10-1997 дата публикации

OLEFIN POLYMERIZATION CATALYSTS, OLEFIN POLYMERIZATION METHODS, AND OLEFIN POLYMER COMPOSITIONS AND HEAT MOLDED PRODUCTS

Номер: CA0002251057A1
Принадлежит:

A catalyst having a high polymerization activity and capable of providing olefin polymers having a wide molecular weight distribution, which comprises (a) a metallocene compound (a-1) or a titanium catalyst component (a-2) comprising magnesium, titanium, and a halogen as indispensable components, (b) a group 8-10 transition metal compound represented by general formula (I'), and a cocatalyst, wherein M represents Pd, Ni, or Pt; X1 and X2 represent N or P; R1 and R2 represent H or a hydrocarbon radical; R4 and R5 represent a halogen or a hydrocarbon radical; and R6 and R7 represent H or a hydrocarbon radical. An olefin polymer composition which has excellent rigidity and impact resistance is prepared by using a catalyst containing the above transition metal compound (b), and comprises a noncrystalline olefin polymer having an intrinsic viscosity, a glass transition temperature, and a density in respective particular ranges and a conventional olefin polymer other than the above olefin polymer ...

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20-03-2007 дата публикации

NOVEL DISPERSANT TERPOLYMERS

Номер: CA0002192006C
Принадлежит: CHEVRON CHEMICAL COMPANY, CHEVRON CHEM CO

A terpolymer having an average Mn of from 600 to 100,000 is obtained by t he terpolymerization of a 1-olefin having from 10 to 30 carbon atoms, maleic anhydride, and a 1,1-disubstituted polyisobutylene having an average Mn of from 500 to 5,000.

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31-07-2007 дата публикации

OLEFIN COPOLYMERS FROM BRIDGED BIS(ARYLAMIDO) GROUP 4 CATALYST COMPOUNDS

Номер: CA0002278282C

A process for preparing substantially random olefin copolymers containing geminally disubstituted olefin monomers is described. The geminally disubstituted olefin monomers can be represented by the generic formula R1 - R2(R3)(R4), where R1 is CH2, R2 is C, and R3 and R4 are, independently, essentially linear hydrocarbyl groups having from 1 to 30 carbon atoms, or more, and containing one carbon atom bound directly to R2. The copolymers can be prepared by contacting at least one geminally disubstituted olefin monomer and one or more comonomers selected from the group consisting of ethylene and C3-C20 .alpha.-olefins, optionally with one or more other coordination polymerizable monomers, with an active coordination catalyst system comprisi ng a bridged bis(arylamido) Group 4 catalyst component.

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15-12-1982 дата публикации

PROCEDURE FOR THE PRODUCTION OF A PAPER SIZING AGENT.

Номер: CH0000633597A5
Принадлежит: BAYER AG

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28-04-1978 дата публикации

Номер: CH0000598345A5

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01-05-2020 дата публикации

Polyolefin dispersants and methods of making and using the same

Номер: CN0111094394A
Автор:
Принадлежит:

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05-10-2011 дата публикации

Novel copolymer and method for producing same

Номер: CN102206296A
Принадлежит:

A novel copolymer and a method for producing it are provided. The copolymer includes a monomer unit represented by the following formula (1) and an olefin unit: wherein: each of A1, A2, A3, and A4 independently represents a hydrogen atom, a halogen atom, an alkyl group, an aralkyl group, an aryl group, a silyl group, a siloxy group, an alkoxy group, an aralkyloxy group, an aryloxy group, an amino group, an amide group, an imide group, or a hydrocarbon thio group; where all groups may have a substituent; and each of m, n, and k is independently an integer in a range of 2 to 20.

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25-05-1979 дата публикации

COPOLYMERISATS OLEFINE-ANHYDRIDE MALEIQUE

Номер: FR0002407224A
Автор:
Принадлежит:

L'INVENTION CONCERNE DES DERIVES DE COPOLYMERES OLEFINE-ACIDE MALEIQUE, CONSTITUES D'OLEFINES AYANT EN MOYENNE 8 A 24ATOMES DE CARBONE ET D'ANHYDRIDE MALEIQUE. LES COPOLYMERES OLEFINE-ANHYDRIDE MALEIQUE SELON L'INVENTION SONT UTILISES COMME LUBRIFIANTS DANS LE MOULAGE DES MATIERES PLASTIQUES.

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01-03-2012 дата публикации

Functionalizable Synthetic Hydrocarbon Fluids and Integrated Method for Production Thereof

Номер: US20120053309A1
Принадлежит: ExxonMobil Chemical Patents Inc

This invention relates to a process to produce a poly(alpha-olefin)(alpha, internally unsaturated, nonconjugated olefin) comprising: contacting at least one renewable feedstream with at least one lower olefin in the presence of a metathesis catalyst, wherein a mixture of at least one C 4 to C 40 linear alpha-olefin and at least one alpha, internally unsaturated, nonconjugated olefin is produced; and contacting the mixture with a metallocene catalyst system, wherein a poly(alpha-olefin)(alpha, internally unsaturated, nonconjugated olefin) is produced.

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05-07-2012 дата публикации

Polyolefin and preparation method thereof

Номер: US20120172548A1
Принадлежит: LG Chem Ltd

A polyolefin has 1) a density in the range of 0.93 to 0.97 g/cm 3 , 2) a BOCD (Broad Orthogonal Co-monomer Distribution) index defined by a given equation in the range of 1 to 5, and 3) a molecular weight distribution (weight average molecular weight/number average molecular weight) in the range of 4 to 10. A supported hybrid metallocene catalyst comprises a first metallocene compound represented by a first given formulae, a second metallocene compound represented by one of three given formulae, and a support.

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30-08-2012 дата публикации

4-METHYL-1-PENTENE/a-OLEFIN COPOLYMER, COMPOSITION COMPRISING THE COPOLYMER AND 4-METHYL-1-PENTENE COPOLYMER COMPOSITION

Номер: US20120220728A1
Принадлежит: Mitsui Chemicals Inc

The present invention provides a 4-methyl-1-pentene/α-olefin copolymer being excellent in lightness, stress absorption, stress relaxation, vibration damping properties, scratch resistance, abrasion resistance, toughness, mechanical properties and flexibility, having no stickiness during molding operation and being excellent in the balance among these properties; a composition comprising the polymer; and uses thereof. The 4-methyl-1-pentene/α-olefin copolymer (A) of the present invention satisfies specific requirements, and comprises 5 to 95 mol % of a structural unit (i) derived from 4-methyl-1-pentene, 5 to 95 mol % of a structural unit (ii) derived from at least one kind of α-olefin selected from α-olefins having 2 to 20 carbon atoms excluding 4-methyl-1-pentene and 0 to 10 mol % of a structural unit (iii) derived from a non-conjugated polyene, provided that the total of the structural units (i), (ii), and (iii) is 100 mol %.

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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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14-03-2013 дата публикации

Epoxy resin composition for semiconductor encapsulant and semiconductor device using the same

Номер: US20130062748A1
Автор: Jun-Ichi Tabei
Принадлежит: Sumitomo Bakelite Co Ltd

According to the present invention, an epoxy resin composition for semiconductor encapsulant including (A) an epoxy resin, (B) a curing agent, (C) an inorganic filler, and (D) a compound in which a copolymer of a 1-alkene having 5 to 80 carbon atoms and maleic anhydride is esterified with an alcohol having 5 to 25 carbon atoms in the presence of a compound represented by General Formula (1), wherein R 1 in General Formula (1) is selected from the group consisting of an alkyl group having 1 to 5 carbon atoms, a halogenated alkyl group having 1 to 5 carbon atoms, and an aromatic group having 6 to 10 carbon atoms is provided.

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21-03-2013 дата публикации

NOVEL CATALYST COMPOSITION AND PROCESS FOR PREPARING OLEFIN POLYMER USING THE SAME

Номер: US20130072646A1
Принадлежит: LG CHEM, LTD.

The present invention relates to a catalyst composition and a process for preparing an olefin polymer using the same. More specifically, the present invention relates to a novel catalyst composition comprising at least two types of catalysts and a process for preparing an olefin polymer having excellent heat resistance using the same. The present invention can provide an olefin polymer having excellent activity and high heat resistance, and also can control the values of density, heat resistance and melt index (MI) of the olefin polymer. 2. The catalyst composition for olefin polymerization according to claim 1 , wherein the catalyst composition further comprises one or more promoter compounds selected from the group consisting of the compounds of the following formulas (3) to (5):{'br': None, 'sup': '4', 'sub': '3', 'J(R)\u2003\u2003[Formula 3]'}in the formula (3),J represents aluminum or boron;{'sup': '4', 'claim-text': {'br': None, 'sup': +', '−', '+', '−, 'sub': 4', '4, '[L-H][ZA] or [L][ZA]\u2003\u2003[Formula 4]'}, 'Rindependently of one another represents halogen, or a hydrocarbyl radical which is unsubstituted or substituted by halogen and has 1 to 20 carbon atoms;'}in the formula (4),L represents a neutral or cationic Lewis acid;H represents hydrogen;Z represents a group XIII atom; {'br': None, 'sup': '5', 'sub': 'a', '—[Al(R)—O]—\u2003\u2003[Formula 5]'}, 'A independently of one another represents alkyl having 1 to 20 carbon atoms or aryl having 6 to 20 carbon atoms wherein one or more hydrogen atoms are replaced by halogen, hydrocarbyl having 1 to 20 carbon atoms, alkoxy having 1 to 20 carbon atoms or phenoxy;'}in the formula (5),{'sup': '5', 'Rrepresents halogen, or hydrocarbyl which is unsubstituted or substituted by halogen and has 1 to 20 carbon atoms; and'}a denotes an integer of 2 or more.3. The catalyst composition for olefin polymerization according to claim 2 , wherein the promoter compound is contained with respect to the compound having a ...

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28-03-2013 дата публикации

CATALYST COMPONENT FOR THE POLYMERIZATION OF OLEFINS HAVING A GUANIDINATE LIGAND

Номер: US20130079478A1
Принадлежит:

The invention relates to a new catalyst component for the polymerization of olefins comprising a compound of formula CyLMZ, wherein M is a Group 4-6 metal, Z is an anionic ligand, p is the number of anionic ligands, Cy is a mono- or poly-substituted cyclopentadienyl-type ligand and L is a guanidinate ligand of the formula wherein: each A is independently selected from nitrogen or phosphorus and R, R, Rand Rare independently selected from the group consisting of hydrogen, hydrocarbyl, silyl and germyl residues, substituted or not with one or more halogen, amido, phosphido, alkoxy, or aryloxy radicals. The invention also relates to a catalyst system for the polymerization of olefins and a process for the polymerization of at least one olefin having 2 to 20 carbon atoms. 2. Catalyst component according to claim 1 , wherein M is selected from the group consisting of Ti claim 1 , Zr and Hf.3. Catalyst component according to or claim 1 , wherein the one or more substituents of Cy are selected from the group consisting of halogen claim 1 , hydrocarbyl claim 1 , silyl and germyl residues claim 1 , optionally substituted with one or more halogen claim 1 , amido claim 1 , phosphido claim 1 , alkoxy claim 1 , or aryloxy radicals.4. Catalyst component according to any one of the to claim 1 , wherein A is nitrogen and R claim 1 , R claim 1 , Rand Rare independently selected from the group consisting of hydrogen and hydrocarbyl residue.5. Catalyst component according to any one of the to claim 1 , wherein the anionic ligand Z is selected from the group consisting of Chydrocarbyl radicals.6. A catalyst system for the polymerization of olefins comprising a catalyst component in the presence of one or more ingredients selected from the group consisting of activator claim 1 , scavenger and carrier characterized in that the catalyst component is according to any of the to .7. Catalyst system according to claims 6 , wherein the activator is selected from the group consisting of borate ...

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13-06-2013 дата публикации

Vinyl Terminated Higher Olefin Copolymers and Methods to Produce Thereof

Номер: US20130150541A1
Принадлежит: ExxonMobil Chemical Patents Inc.

This invention relates to a vinyl terminated higher olefin copolymer having an Mn of 300 g/mol or more (measured by H NMR) comprising: (i) from about 20 to about 99.9 mol % of at least one Cto Chigher olefin monomer; and (ii) from about 0.1 to about 80 mol % of propylene; wherein the higher olefin copolymer has at least 40% allyl chain ends. The copolymer may also have an isobutyl chain end to allyl chain end ratio of less than 0.7:1 and/or an allyl chain end to vinylidene chain end ratio of greater than 2:1. 2. The process of claim 1 , wherein the copolymer has an isobutyl chain end to allyl chain end ratio of less than 0.7:1.3. The process of claim 1 , wherein the copolymer has an allyl chain end to vinylidene chain end ratio of more than 2:1.4. The process of claim 1 , wherein the Cto Chigher olefin is selected from pentene claim 1 , hexene claim 1 , heptene claim 1 , octene claim 1 , nonene claim 1 , decene claim 1 , undecene claim 1 , dodecene claim 1 , norbornene claim 1 , norbornadiene claim 1 , dicyclopentadiene claim 1 , cyclopentene claim 1 , cycloheptene claim 1 , cyclooctene claim 1 , cyclooctadiene claim 1 , cyclododecene claim 1 , 7-oxanorbornene claim 1 , 7-oxanorbornadiene claim 1 , substituted derivatives thereof claim 1 , and isomers thereof.5. The process of claim 1 , wherein the higher olefin copolymer has a viscosity at 60° C. of greater than 1000 cP.6. (canceled)8. The process of claim 7 , wherein the copolymer has an isobutyl chain end to allyl chain end ratio of less than 0.7:1.9. The process of claim 7 , wherein the copolymer has an allyl chain end to vinylidene chain end ratio of more than 2:1.10. The process of claim 7 , wherein the higher olefin copolymer comprises at least 50 wt % claim 7 , based upon the weight of the copolymer composition claim 7 , of olefins having at least 36 carbon atoms claim 7 , as measured by H NMR claim 7 , assuming one unsaturation per chain.11. (canceled)13. The process of claim 12 , wherein the Cto Chigher ...

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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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27-06-2013 дата публикации

PROPYLENE-BASED TERPOLYMERS FOR FILM

Номер: US20130165613A1
Принадлежит:

A propylene/ethylene/1-hexene terpolymer containing from 1.0 wt % to 2.5 wt %, of ethylene derived units and from 2.0 wt % to 3.5 wt % of 1-hexene derived units, the sum of the amounts of propylene, ethylene and 1-.hexene derived units being 100, having the following features: a)the amount (Wt %) of 1-hexene (C6) and the amount (Wt %) of ethylene (C2) fulfil the following relation (i): 0.5 Подробнее

29-08-2013 дата публикации

Cyclopenta[b]Fluorenyl Transition Metal Compound, Catalyst Composition Containing the Same, and Method of Preparing Ethylene Homopolymer or Copolymer of Ethylene and alpha-Olefin Using the Same

Номер: US20130225834A1

The present invention relates to a new transition metal compound based on cyclopenta[b]fluorenyl group, a transition metal catalyst composition containing the same and having high catalytic activity for preparing an ethylene homopolymer or a copolymer of ethylene and one α-olefin, a method of preparing an ethylene homopolymer or a copolymer of ethylene and α-olefin using the same, and the prepared ethylene homopolymer or the copolymer of ethylene and α-olefin.

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03-10-2013 дата публикации

Polymerization process and raman analysis for olefin-based polymers

Номер: US20130261224A1
Принадлежит: Dow Global Technologies LLC

The invention provides a process for monitoring and/or adjusting a dispersion polymerization of an olefin-based polymer, the process comprising monitoring the concentration of the carbon-carbon unsaturations in the dispersion using Raman Spectroscopy. The invention also provides a process for polymerizing an olefin-based polymer, the process comprising polymerizing one or more monomer types, in the presence of at least one catalyst and at least one solvent, to form the polymer as a dispersed phase in the solvent; and monitoring the concentration of the carbon-carbon unsaturations in the dispersion using Raman Spectroscopy.

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10-10-2013 дата публикации

Additive for Polyolefin Polymerization Processes

Номер: US20130267666A1
Принадлежит: Univation Technologies Llc

A polymerization process is disclosed comprising polymerizing an olefin to form an olefin-based polymer in a polymerization reactor; and introducing a polyetheramine additive to the polymerization reactor. The process may further comprise monitoring static in the polymerization reactor; maintaining the static at a desired level by use of a polyetheramine additive, where the polyetheramine additive is present in the reactor in the range from about 0.1 to about 500 ppmw, based on the weight of polymer produced by the process.

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31-10-2013 дата публикации

Polyethylene and Process for Production Thereof

Номер: US20130289213A1
Принадлежит: ExxonMobil Chemical Patents Inc

This invention relates to a process for polymerizing olefins in which the amount of trimethylaluminum in a methylalumoxane solution is adjusted to be from 1 to 25 mol %, prior to use as an activator, where the mol % trimethylaluminum is determined by 1 H NMR of the solution prior to combination with any support. This invention also relates to a process for polymerizing olefins in which the amount of an unknown species present in a methylalumoxane solution is adjusted to be from 0.10 to 0.65 integration units prior to use as an activator, where the amount of the unknown species is determined by the 1 H NMR spectra of the solution performed prior to combination with any support. Preferably, the methylalumoxane solution is present in a catalyst system also comprising a metallocene transition metal compound.

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07-11-2013 дата публикации

REACTOR OPERABILITY IN A GAS PHASE POLYMERIZATION PROCESS

Номер: US20130296507A1
Принадлежит: NOVA CHEMICALS (INTERNATIONAL) S.A.,

Olefin polymerization is carried out with a single site polymerization catalyst in the presence of a continuity additive. The continuity additive is a cocktail containing one or more dialkanolamide derived from a fatty acid, an oil soluble sulfonic acid and a dialkanolamine. 1. A process for polymerizing ethylene and optionally an alpha olefin in a reactor with at least one single site polymerization catalyst in the presence of a continuity additive , said continuity additive comprising:i) a fatty acid dialkanolamide,ii) an oil soluble sulfonic acid, andiii) a dialkanolamine.2. The process of wherein the continuity additive comprises:{'sup': 1', '1, 'sub': 2', '2', '2, 'i) at least one fatty acid diethanolamide having the formula RC(═O)N(CHCHOH)where Ris a hydrocarbyl group having from 5 to 30 carbon atoms,'}{'sup': 3', '3, 'sub': 6', '4', '3, 'ii) a benzene sulfonic acid having the formula RCHSOH, where Ris a hydrocarbyl group having from 6 to 30 carbon atoms, and'}{'sub': 2', 'x', '2, 'iii) a dialkanolamine having the formula HN((CH)OH)where x is independently an integer from 1 to 8.'}3. The process of wherein the continuity additive comprises:{'sup': 1', '1, 'sub': 2', '2', '2, 'i) a mixture of two or more different fatty acid diethanolamides having the formula RC(═O)N(CHCHOH), where Ris a hydrocarbyl group having anywhere from 5 to 30 carbon atoms,'}{'sup': 3', '3, 'sub': 6', '4', '3, 'ii) a benzene sulfonic acid having the formula RCHSOH, where Ris a hydrocarbyl group having 6 to 22 carbon atoms, and'}{'sub': 2', 'x', '2, 'iii) a dialkanolamine having the formula HN((CH)OH), where x is 2 or 3.'}4. The process of wherein the mixture of two or more different fatty acid diethanolamides comprises compounds having the formula R(C═O)N(CHCHOH)where Ris a hydrocarbyl group with 5 claim 3 , 7 claim 3 , 9 claim 3 , 11 claim 3 , 13 claim 3 , 15 claim 3 , or 17 carbon atoms and wherein diethanolamide compounds having hydrocarbyl groups with 5 claim 3 , 7 claim 3 , 9 claim ...

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19-12-2013 дата публикации

Control of Resin Molecular Weight Distribution Using Mixed Catalyst Systems

Номер: US20130338320A1
Автор: Jorgensen Robert J.

A polymerization process including the use of a first Ziegler-Natta type procatalyst having no internal electron donor and a second Ziegler-Natta type procatalyst including an internal electron donor is provided. 2. (canceled)3. The process according to claim 1 , wherein the first and second Ziegler-Natta type procatalysts are mixed to form a mixed procatalyst feed prior to being fed into the reactor.4. The process according to claim 1 , wherein the first and second Ziegler-Natta type procatalysts are separately fed into the reactor.5. The process according to claim 1 , wherein a feed of the first Ziegler-Natta type procatalyst is decreased as a feed of the second Ziegler-Natta type procatalyst is increased.6. The process of wherein the mixed procatalyst feed comprises between 0.8 and 2.1 wt % of the second Ziegler-Natta type procatalyst and between 99.2 and 97.9 wt % of the first Ziegler-Natta type procatalyst based on the total weight of the first and second Zielger-Natta procatalysts.7. The process according to claim 1 , wherein no electron donor is added to the reactor.8. The process according to claim 1 , further comprising adding a continuity additive to the reactor.9. The process of wherein the relative weight percentages of the first and second Ziegler-Natta type procatalysts produce a variation in the molecular weight of the polyolefin polymer.10. The process of wherein the relative weight percentages of the first and second Ziegler-Natta type procatalysts produce a variation in the molecular weight distribution of the polyolefin polymer.11. The process of wherein the one or more olefins comprises ethylene and further wherein a partial pressure of the ethylene is varied to maintain a constant rate of production of polyolefin.12. The process according to claim 1 , the second Ziegler-Natta type procatalyst has a second order productivity response to ethylene concentration.13. The process according to claim 1 , wherein the polymerization is a slurry reactor or ...

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30-01-2014 дата публикации

ETHYLENE-BASED POLYMER, MANUFACTURING METHOD OF ETHYLENE-BASED POLYMER AND MANUFACTURING METHOD OF CATALYST FOR POLYMERIZATION, AND MOLDED ARTICLE OF HOLLOW PLASTICS CONTAINING ETHYLENE-BASED POLYMER AND USE THEREOF

Номер: US20140030460A1
Принадлежит: JAPAN POLYETHYLENE CORPORATION

An object of the invention is to provide an ethylene-based polymer excellent in moldability and durability, and also excellent in the balance of stiffness and durability, and to provide a molded product of hollow plastic using the ethylene-based polymer. The ethylene-based polymer according to the invention is an ethylene-based polymer having specific characteristics and manufactured by a homopolymerization of ethylene or a copolymerization of ethylene and α-olefin using a chromium catalyst. 1. An ethylene-based polymer which is manufactured by a homopolymerization of ethylene or a copolymerization of ethylene and α-olefin by using a chromium catalyst , and has the following characteristics of (1) to (8):(1) the high load melt flow rate (HLMFR) is 1 to 10 g/10 min,{'sup': '3', '(2) the density is 0.940 to 0.960 g/cm,'}(3) the molecular weight distribution (Mw/Mn) is 25 or more,(4) the strain hardening parameter of elongation viscosity (λmax) is 1.05 to 1.50,{'sup': '2', '(5) the Charpy impact strength is 7 kJ/mor more,'}{'sup': '2', '(6) the tensile impact strength is 130 kJ/mor more,'}(7) the swell ratio (SR) is 50 to 65%, and(8) the rupture time in the full notch creep test is 40 hours or more.2. The ethylene-based polymer as claimed in claim 1 , wherein the chromium catalyst is a catalyst obtained by having a chromium compound (b) supported on an inorganic oxide support (a) having a specific surface area of 625 to 1 claim 1 ,000 m/g and a pore volume of 1.0 to 5.0 cm/g claim 1 , and drying and calcining the obtained inorganic oxide support (a) in a non-reducing atmosphere.3. The ethylene-based polymer as claimed in claim 1 , which is a copolymer of ethylene and α-olefin having 3 to 8 carbon atoms.4. A method for manufacturing an ethylene-based polymer comprising homopolymerizing ethylene or copolymerizing ethylene and α-olefin using a catalyst claim 1 , in which the catalyst is obtained by activating a catalyst precursor (d) at 250° C. to 550° C. in a non- ...

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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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06-03-2014 дата публикации

HIGH ACTIVITY, LOW MOLECULAR WEIGHT OLEFIN POLYMERIZATION PROCESS

Номер: US20140066585A1
Принадлежит: Dow Global Technologies LLC

Group 4 metal complexes comprising a polyvalent, heteroaryl donor ligand and their use as components of olefin polymerization catalysts, especially suited for preparing propylene copolymer products having high isotacticity and low molecular weight, are disclosed. 1copolymerizing propylene and 1-octene at a temperature from 100 to 130° C., a pressure from 100 kPa to 10 MPa, and a hydrogen partial pressure from 25 to 500 kPa in the presence of a metal complex corresponding to the formula:. A propylene/octene copolymer wherein the copolymer is made by the process comprising:wherein, X is an anionic ligand group; andcovalent bonds are represented by lines and coordination interactions are represented by arrows. This invention relates to a Group 4 metal complex, to a catalyst composition and to a process for polymerizing addition polymerizable unsaturated monomers, especially olefins. In particular, the invention is directed to certain Group 4 metal complexes, to catalyst compositions comprising the same, and to addition polymerization processes using the same.Advances in polymerization and catalysis have resulted in the capability to produce many new polymers having improved physical and chemical properties useful in a wide variety of superior products and applications. With the development of new catalysts the choice of polymerization-type (solution, slurry, high pressure or gas phase) for producing a particular polymer has been greatly expanded. Also, advances in polymerization technology have provided more efficient, highly productive and economically enhanced processes. Recently, several new disclosures related to metal complexes based on polyvalent metal-centered, heteroaryl donor ligands have published. Among these are U.S. Pat. No. 6,103,657, U.S. Pat. No. 6,906,160, U.S. Pat. No. 6,919,407, U.S. Pat. No. 6,927,256, US-A-2002/0142912, US-A-2004/0220050, US-A-2004/0005984, WO 2000/020377, and WO 2002/038628.Regardless of the technological advances in the ...

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20-03-2014 дата публикации

PROPYLENE-HEXENE RANDOM COPOLYMER PRODUCED IN THE PRESENCE OF A ZIEGLER NATTA CATALYST

Номер: US20140079899A1
Принадлежит: Borealis AG

Propylene copolymer a. comprising at least 1-hexene as a comonomer, b. having a comonomer content in the range of 1.0 to 3.0 wt.-%, c. having a xylene soluble fraction equal or below 2.5 wt.-%, and d. being partially crystallized in the β-modification. 1. Propylene copolymer (A)(a) comprising at least 1-hexene as a comonomer,(b) having a comonomer content in the range of 1.0 to 3.0 wt.-%,(c) having a xylene soluble fraction equal or below 2.5 wt.-%, and(d) being partially crystallized in the β-modification.2. Propylene copolymer according to claim 1 , wherein the copolymer (A) comprises a β-nucleating agent (B).3. Propylene copolymer (A)(a) comprising at least 1-hexene as a comonomer,(b) having a comonomer content in the range of 1.0 to 3.0 wt.-%,(c) having a xylene soluble fraction equal or below 2.5 wt.-%, and(d) comprising a β-nucleating agent (B).4. Propylene copolymer according to claim 3 , wherein the copolymer (A) is partially crystallized in the β-modification.5. Propylene copolymer (A) according to claim 1 , wherein propylene copolymer (A) has a MFR(230° C.) of not more than 0.8 g/10 min measured according to ISO 1133.6. Propylene copolymer (A) according to claim 1 , wherein the 1-hexene content of the propylene copolymer (A) is in the range of 1.0 to 2.0 wt.-%.7. Propylene copolymer (A) according to claim 1 , wherein the propylene copolymer (A) is only constituted by propylene and 1-hexene units.8. Propylene copolymer (A) according to claim 1 , wherein the comonomer content of the propylene copolymer (A) is in the range of 1.0 to 2.0 wt.-%.9. Propylene copolymer (A) according to claim 1 , wherein the propylene copolymer (A) has a polydispersity index (PI) of 3.0 to 8.0 Pa.10. Propylene copolymer (A) according to claim 1 , wherein the amount of the β-modification of the propylene copolymer (A) is at least 50%.11. Propylene copolymer (A) according to claim 1 , wherein the propylene copolymer (A) has a flexural modulus measured according to ISO 178 of at ...

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27-03-2014 дата публикации

Synthetic lubricant basestocks and methods of preparation thereof

Номер: US20140087984A1
Принадлежит: ExxonMobil Research and Engineering Co

This disclosure relates to vinyl terminated macromer (VTM) based synthetic basestocks and their methods of preparation, lubricant compositions, methods of lubrication and products so lubricated. The VTM based synthetic basestocks useful for fuels and lubricants include oligomerization or polymerization products of one or more allylic vinyl terminated macromers (VTMs) having a molecular weight from 84 to 10080. The one or more allylic VTMs are oligomerized or polymerized in the presence of a catalyst under oligomerization or polymerization conditions sufficient to give the VTM based synthetic basestock. The catalyst can be a metallocene catalyst or an acid catalyst, e.g., Lewis acid. The one or more allylic vinyl terminated macromers (VTMs) can be one or more allylic vinyl terminated atactic polypropylene macromers (VTM aPP) having a molecular weight from 84 to 2250 and having a terminal allylic vinyl olefin content of at least 90%.

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27-03-2014 дата публикации

Catalytic Hydroformylation of Vinyl Terminated Polyolefins

Номер: US20140088261A1
Принадлежит: ExxonMobil Chemical Patents Inc

This invention relates to a polyolefin composition comprising one or more of the following formulae: wherein the PO is the residual portion of a vinyl terminated macromonomer (VTM) having had a terminal unsaturated carbon of an allylic chain and a vinyl carbon adjacent to the terminal unsaturated carbon; and wherein the VTM is preferably a vinyl terminated polymer having greater than 30% allyl chain ends with an Mn of greater than 10,000.

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03-04-2014 дата публикации

Polyolefin and preparation method thereof

Номер: US20140094574A1
Принадлежит: LG Chem Ltd

A polyolefin has 1) a density in the range of 0.93 to 0.97 g/cm 3 , 2) a BOCD (Broad Orthogonal Co-monomer Distribution) index defined by a given equation in the range of 1 to 5, and 3) a molecular weight distribution (weight average molecular weight/number average molecular weight) in the range of 4 to 10. A supported hybrid metallocene catalyst comprises a first metallocene compound represented by a first given formulae, a second metallocene compound represented by one of three given formulae, and a support.

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04-01-2018 дата публикации

Recovery of hydrocarbons from a hydrocarbon recycle

Номер: US20180002458A1
Принадлежит: SABIC Global Technologies BV

The invention relates to a process for the polymerization of olefins comprising the comprising the steps of a. Polymerizing olefins in a reaction mixture comprising monomers, diluent, processing as aids to prepare a product stream comprising polyolefins, monomers and diluent; b. Removing the polyolefins from the product stream to obtain a purge stream; c. Removing gaseous components from the purge stream to obtain a liquid fraction; d. Treating the liquid fraction with at least one ionic liquid to obtain a fraction containing unsaturated hydrocarbons; e. Recycling the fraction containing unsaturated hydrocarbons to the reaction mixture, optionally after purification of said fraction containing unsaturated hydrocarbons. The invention also relates to an olefin polymerization system comprising a polymerization reactor, a purge vessel, a vent gas recovery and an ionic liquid separator for separating liquid alkenes from liquid alkanes, wherein the liquid alkenes which are separated from the alkanes in the ionic liquid separator can be recycled to the polymerization reactor.

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07-01-2021 дата публикации

PROCESS FOR PREPARING PROPYLENE COPOLYMERS COMPRISING C4-C12-APHA OLEFIN COMONOMER UNITS

Номер: US20210002397A1
Принадлежит:

The present invention relates to a process for producing a copolymer of propylene, optionally ethylene, and at least one comonomer selected from alpha olefins having from 4 to 12 carbon atoms using a specific class of metallocene complexes in combination with a cocatalyst system comprising a boron containing cocatalyst and an aluminoxane cocatalyst, preferably in a multistage polymerization process including a gas phase polymerization step. 3. The process according to claim 1 , wherein the boron based cocatalyst is one of formula (Z){'br': None, 'sub': '3', 'BY\u2003\u2003(Z)'}wherein Y independently is the same or can be different and is a hydrogen atom, an alkyl group of from 1 to about 20 carbon atoms, an aryl group of from 6 to about 15 carbon atoms, alkylaryl, arylalkyl, haloalkyl or haloaryl each having from 1 to 10 carbon atoms in the alkyl radical and from 6-20 carbon atoms in the aryl radical or fluorine, chlorine, bromine or iodine.4. The process according to claim 1 , wherein the boron based cocatalyst is one of compounds containing a borate anion.5. The process according to claim 1 , wherein the molar ratio of boron in the boron containing cocatalyst to the metal ion M in the complex of formula (I) is in the range of 0.5:1 to 10:1 mol/mol.6. The process according to claim 1 , wherein the molar ratio of aluminium in the aluminoxane cocatalyst to the metal ion M in the complex of formula (I) is in the range of 1:1 to 2000:1 mol/mol.7. The process according to comprising the steps ofa) introducing propylene monomer units, alpha-olefin comonomer units having from 4 to 12 carbon atoms, optionally ethylene comonomer units and hydrogen into a polymerization reactor;b) polymerizing the propylene monomer units, the optional ethylene comonomer, and alpha-olefin comonomer units having from 4 to 12 carbon atoms to form a copolymer of propylene and at least one comonomer selected alpha-olefins from having from 4 to 12 carbon atoms in the presence the single-site ...

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11-01-2018 дата публикации

CATALYST SYSTEMS FOR OLEFIN POLYMERIZATION

Номер: US20180009958A1
Принадлежит: Dow Global Technologies LLC

The instant invention provides procatalysts and catalyst systems for olefin polymerization, olefin based polymers polymerized therewith, and process for producing the same. In one embodiment, the instant invention provides a procatalyst comprising a metal-ligand complex of formula (I): 2. The procatalyst according to wherein Z is O.3. A catalyst system comprising the reaction product of:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'one or more procatalysts of ; and'}one or more cocatalysts; wherein the ratio of total number of moles of the one or more metal-ligand complexes of formula (I) to total number of moles of the one or more cocatalysts is from 1:10,000 to 100:1.4. A polymerization process comprising the steps of:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'polymerizing one or more α-olefins in the presence of one or more catalyst systems of under olefin polymerizing conditions; and thereby forming an olefin based polymer.'}5. An olefin based polymer comprising the polymerization reaction product of:{'claim-ref': {'@idref': 'CLM-00003', 'claim 3'}, 'one or more α-olefins in the presence of one or more catalyst systems of under olefin polymerizing conditions.'} The present application is a continuation of U.S. patent application Ser. No. 14/437,543, filed on Apr. 22, 2015, which is a national stage entry of PCT/US2013/073976, filed on Dec. 10, 2013, which claims the benefit of U.S. Provisional Application No. 61/746,151, filed on Dec. 27, 2012.The instant invention relates to procatalysts and catalyst systems for olefin polymerization, olefin based polymers polymerized therewith, articles made from such polymers, and process for producing the same.Olefin based polymers such as polyethylene and/or polypropylene are produced via various catalyst systems. Selection of such catalyst system used in the polymerisation process of the olefin based polymers is an important factor contributing to the characteristics and properties of such olefin based ...

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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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09-01-2020 дата публикации

COATED PIGMENT, AQUEOUS PIGMENT DISPERSION, USE THEREOF, AND PRODUCTION METHOD THEREFOR

Номер: US20200010709A1
Автор: TSURUTANI Shinsuke
Принадлежит:

A purpose of the present invention is to provide a fine coated pigment which is inhibited from becoming coarse particles and is easily dispersible. The coated pigment is a pigment, the surface of which has been coated with a resin, wherein the resin is an α-olefin copolymer having an acid group and the amount of the resin with which the pigment has been coated is 10-50 parts by mass per 100 parts by mass of the uncoated pigment (X). 1. A coated pigment , where its surface has been coated with a resin , wherein the resin is an α-olefin copolymer having an acid group and an amount of resin coating of the coated pigment is equal to or greater than 10 parts by mass and equal to or less than 50 parts by mass per 100 parts by mass of an uncoated pigment (X).2. The coated pigment according to claim 1 , wherein the resin is an α-olefin copolymer having a side chain and an acid group.4. The coated pigment according to claim 1 , wherein the resin contains one or more kinds selected from a group consisting of a styrene-(meth)acrylic resin claim 1 , a styrene-maleic (anhydride) resin claim 1 , and a (meth)acrylic resin.5. An aqueous pigment dispersion comprising:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'the coated pigment according to ;'}water; anda basic compound.6. The aqueous pigment dispersion according to claim 5 , further comprising:a crosslinking agent.7. An inkjet printing ink comprising:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'the coated pigment according to .'}8. An inkjet printing ink comprising:{'claim-ref': {'@idref': 'CLM-00002', 'claim 2'}, 'the coated pigment according to .'}9. An inkjet printing ink comprising:{'claim-ref': {'@idref': 'CLM-00005', 'claim 5'}, 'the aqueous pigment dispersion according to .'}10. A flexographic printing ink comprising:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'the coated pigment according to .'}11. A flexographic printing ink comprising:{'claim-ref': {'@idref': 'CLM-00002', 'claim 2'}, 'the coated ...

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16-01-2020 дата публикации

Polyethylene composition and film

Номер: US20200017668A1
Принадлежит: Nova Chemicals International SA

In some embodiments disclosed herein are polyethylene composition including a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution Mw/Mn of <2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of less than 75,000 and a molecular weight distribution Mw/Mn of <2.3, a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of less than 75,000 and a molecular weight distribution Mw/Mn of <2.3, and a fourth polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 100,000 to 250,000 and a molecular weight distribution Mw/Mn of >2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene. The polyethylene composition may have a soluble fraction in a CEF analysis of at least 7.5 weight percent. Film made from the polyethylene composition may have a machine direction 1% secant modulus of ≥200 MPa (at a film thickness of about 1 mil) and an oxygen transmission rate (OTR) of ≥550 cm3 per 100 inch2 (at a film thickness of about 1 mil). Film made from the polyethylene composition retains much of its dart impact performance on downgauging from a thickness of 1 mil to a thickness of 0.75 mil.

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16-01-2020 дата публикации

Polyethylene composition and film having high stiffness, outstanding sealability and high permeability

Номер: US20200017669A1
Принадлежит: Nova Chemicals International SA

A polyethylene composition includes a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution Mw/Mn of <2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 15,000 to 100,000, a molecular weight distribution Mw/Mn of >2.3, and a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution Mw/Mn of >2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene. The polyethylene composition has a soluble fraction in a CEF analysis of at least 10 weight percent. Film made from the polyethylene composition may have a machine direction 1% secant modulus of ≥200 MPa (at a film thickness of about 1 mil), a seal initiation temperature (SIT) of ≤90° C. (at a film thickness of about 2 mil), an area of hot tack window (AHTW) of ≥160 Newtons·C° (at a film thickness of about 2 mil) and an oxygen transmission rate (OTR) of ≥600 cm3 per 100 inch2 (at a film thickness of about 1 mil).

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16-01-2020 дата публикации

COLD FLOW ADDITIVE FOR MIDDLE DISTILLATE FUELS

Номер: US20200017786A1
Принадлежит:

Disclosed are cloud point depressants and methods of making and using them. The disclosed cloud point depressants comprise copolymers of an unsaturated anhydride polymerized with alkyl α-olefins and then contacted with a phenyl alkyl alcohol or alkyl phenol alkoxylate, fatty alcohol and primary or secondary fatty amine to provide a cloud depressant reaction product. When the disclosed reaction products are added to middle distillate fuels or blends of middle distillate fuels with biodiesel, the cloud point depressants inhibit the precipitation of waxes and/or biowaxes in the fuels and the fuels exhibit reduced precipitation, gelling, and/or crystallization when subjected to low or cold temperatures. 1. A cold flow additive for middle distillate fuel comprising a solvent and a reaction product that lowers cloud point temperatures consisting essentially of an alkyl α-olefin , an unsaturated anhydride , a phenyl alkyl alcohol or an alkyl phenol alkoxylate , a fatty alcohol , and a primary or secondary fatty amine.2. The cold flow additive of claim 1 , wherein the alkyl α-olefin is a C-Cα-olefin claim 1 , a C-Cα-olefin claim 1 , a C α-olefin claim 1 , or combinations thereof.3. The cold flow additive of claim 1 , wherein the unsaturated anhydride is maleic anhydride claim 1 , six-membered cyclic anhydride claim 1 , seven-member cyclic anhydride claim 1 , or combinations thereof.4. The cold flow additive of claim 1 , wherein the phenyl alkyl alcohol is benzyl alcohol claim 1 , 2-phenyl-1-propanol claim 1 , 3-phenyl-1-propanol claim 1 , 2-phenyl ethanol claim 1 , or combinations thereof and the alkyl phenol alkoxylate is ethoxylated alkyl phenol claim 1 , propoxylated alkyl phenol claim 1 , ethoxylated and propoxylated alkyl phenol claim 1 , ethoxylated nonylphenol claim 1 , ethoxylated octylphenol claim 1 , phenolglycol claim 1 , or combinations thereof.5. The cold flow additive of claim 1 , wherein the fatty alcohol is C-COH claim 1 , C-COH claim 1 , C-COH claim 1 , COH ...

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28-01-2016 дата публикации

Low Density Polyolefin Resins With Low Molecular Weight and High Molecular Weight Components, and Films Made Therefrom

Номер: US20160024236A1
Принадлежит:

Disclosed herein are ethylene-based polymers produced using dual metallocene catalyst systems. These polymers have low densities, high molecular weights, and broad molecular weight distributions, as well as having the majority of the long chain branches in the lower molecular weight component of the polymer, and the majority of the short chain branches in the higher molecular weight component of the polymer. Films produced from these polymers have improved impact and puncture resistance. 110-. (canceled)11. A blown film comprising an ethylene polymer having a melt index less than or equal to about 0.4 g/10 min , wherein the film has a dart impact strength greater than or equal to about 300 g/mil.12. The film of claim 11 , wherein the polymer comprises a higher molecular weight component and a lower molecular weight component claim 11 , wherein:a ratio of the Mp of the higher molecular weight component to the Mp of the lower molecular weight component in a range from about 5:1 to about 100:1;the lower molecular weight component has a Mp in a range from about 15 to about 80 kg/mol; andthe higher molecular weight component has a Mp in a range from about 150 to about 800 kg/mol.13. The film of claim 12 , wherein the polymer comprises a higher molecular weight component and a lower molecular weight component claim 12 , wherein:a number of LCB of the lower molecular weight component is in a range from about 5 to about 50 LCB per million total carbon atoms;a number of LCB of the higher molecular weight component is less than or equal to about 5 LCB per million total carbon atoms;a number of LCB of the ethylene polymer is in a range from about 2 to about 30 LCB per million total carbon atoms; anda ratio of the number of LCB of the ethylene polymer to the number of LCB of the higher molecular weight component, per millions total carbon atoms, is in a range from about 2:1 to about 100:1.14. The film of claim 11 , wherein the polymer is an ethylene/1-butene copolymer claim 11 ...

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28-01-2021 дата публикации

Catalyst Systems and Polymerization Processes for Using the Same

Номер: US20210023540A1
Принадлежит:

A catalyst system including the product of the combination of an unbridged Group 4 metallocene compound and a 2,6-bis(imino)pyridyl iron complex is provided. A process for the polymerization of monomers (such as olefin monomers) and a polymer produced therefrom are also provided. 1. An ethylene copolymer composition comprising 90 wt % or more of ethylene derived units and from 6 wt % to 10 wt % Cto Cα-olefin derived units , based on the total weight of the ethylene composition;{'sup': '3', 'wherein the ethylene copolymer composition has density within the range from 0.910 to 0.960 g/cmand a ratio of weight average molecular weight to number-average molecular weight (Mw/Mn) of greater than 3; and'}further wherein the ethylene copolymer composition has one or more of the following properties:a mole-basis reversed comonomer index (RCI,m) within the range from 150 to 500;a comonomer distribution ratio (CDR-2,m) within the range from 1 to 4; and{'sub': 75', '25, 'a composition distribution breadth (T-Tvalue as measured by TREF) within the range from 15 to 50° C.'}2. The ethylene copolymer composition of claim 1 , wherein the Cto Cα-olefin derived units are selected from the group consisting of 1-butene claim 1 , 1-hexene claim 1 , 1-octene claim 1 , and combinations thereof.3. The ethylene copolymer composition of claim 1 , having T-Tvalue as measured by TREF greater than 30° C.4. The ethylene copolymer composition of claim 1 , having both (1) RCI claim 1 ,m within the range from 150 to 500 and (2) CDR-2 claim 1 ,m within the range from 1 to 4.5. The ethylene copolymer composition of claim 1 , further having one or more of the following properties:(a) weight average molecular weight (Mw) within the range from 75,000 to 200,000 g/mol;(b) ratio of z-average molecular weight to weight average molecular weight (Mz/Mw) within the range from 1 to 10; and{'sub': 'vis', '(c) g′greater than 0.9.'}6. The ethylene copolymer composition of claim 5 , having all of the properties (a ...

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23-01-2020 дата публикации

MALEIC ANHYDRIDE COPOLYMER WITH BROADLY DISPERSED ESTER SIDE CHAIN AS WAX INHIBITOR AND WAX CRYSTALLIZATION ENHANCER

Номер: US20200024504A1
Принадлежит:

A wax inhibitor composition, the composition having at least one alpha-olefin maleic anhydride copolymer of the formula: 2. The wax inhibitor composition as recited in claim 1 , wherein the at least one alpha olefin maleic anhydride copolymer is prepared by reacting an alpha-olefin containing greater than 10 carbon atoms with maleic anhydride in the presence of a free radical initiator to obtain a high molecular weight copolymer claim 1 , followed by reacting the high molecular weight copolymer with an alcohol mixture having a dispersed chain length ranging from 10 to 80 carbon atoms.3. The wax inhibitor composition as recited in claim 2 , wherein the alpha-olefin comprises a range of about 10-30 carbon atoms.4. (canceled)5. The wax inhibitor composition as recited in claim 2 , wherein the alpha-olefin is 1-octadecene claim 2 , 1-eicosene claim 2 , 1-docosene claim 2 , 1-tetracosene claim 2 , 1-hexacosene claim 2 , 1-octacosene claim 2 , 1-hexadecene claim 2 , 1-tetradecane claim 2 , or 1-dodecene.6. The wax inhibitor composition as recited in claim 2 , wherein the alcohol mixture contains more than 25% by weight of alcohols in the alcohol mixture contain greater than 35 carbon atoms.7. The wax inhibitor composition as recited in claim 2 , wherein the alcohol mixture has a dispersed chain length ranging from (i) C10-C60 claim 2 , (ii) C20-C70 claim 2 , or (iii) C30-C80.89-. (canceled)10. The wax inhibitor composition as recited in claim 2 , wherein the alcohol mixture comprises a linear aliphatic alcohol containing more than 25% by weight of alcohols in the alcohol mixture contain greater than 35 carbon atoms.12. The comb polymer composition as recited in claim 11 , wherein the at least one alpha olefin maleic anhydride copolymer is prepared by reacting an alpha-olefin or alpha-olefin mixture with a chain length of greater than 24 carbon atoms with a dicarboxylic acid to obtain a copolymer claim 11 , followed by reacting the copolymer with an alcohol mixture in 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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24-04-2014 дата публикации

METHOD FOR PRODUCING OLEFIN POLYMER

Номер: US20140114032A1
Принадлежит: IDEMITSU KOSAN CO., LTD.

A method for producing an olefin polymer including: polymerizing one or more α-olefins each having 6 to 20 carbon atoms in the presence of a metallocene catalyst to obtain an olefin polymer, and diluting a polymerization reaction liquid with a solvent before or simultaneously with deactivation of the catalyst, thereby to lower the liquid viscosity of the polymerization reaction liquid to 10 mPa·s or less to promote deactivation and decalcification of the catalyst. 1. A method for producing an olefin polymer , the method comprising:polymerizing one or more α-olefins each having 6 to 20 carbon atoms in the presence of a metallocene catalyst to obtain an olefin polymer, anddiluting a polymerization reaction liquid with a solvent before or simultaneously with deactivation of the metallocene catalyst, thereby to lower liquid viscosity of the polymerization reaction liquid to 10 mPa·s or less to promote deactivation and decalcification of the metallocene catalyst.2. The method according to claim 1 ,wherein the solvent has a boiling point which enables a removal of the solvent by distillation in a post process.3. The method according to claim 1 ,wherein the solvent is an un-reacted monomer or a polymerization reaction solvent removed in a post process.4. An olefin polymer obtained by the method according to . The invention relates to a method for producing an olefin polymer and an olefin polymer obtained by this method.Usually, in many cases, polymerization reaction of poly-α-olefin using a metallocene catalyst are continuously performed, and the monomer conversion rate is about 30 to 70%. Under such circumstances, a still higher productivity has been desired.For example, according to Patent Document 1, in the production technology of a conventional olefin-based polymer, the concentration of the olefin-based polymer at the time of the end of a reaction was 2 to 40 mass % in a polymerization reaction solution. In order to prevent an excessive polymerization reaction, an ...

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24-04-2014 дата публикации

OLEFIN BLOCK COPOLYMERS AND PRODUCTION METHODS THEREOF

Номер: US20140114033A1
Принадлежит: LG CHEM, LTD.

The present description relates to olefin block copolymers having excellent elasticity and processability in conjunction with enhanced heat resistance, and to a preparation method thereof. The olefin block copolymers comprise a plurality of blocks or segments that comprise ethylene or propylene repeating units and α-olefin repeating units at different mole fractions from one another, wherein the block copolymer shows peaks at the 2θ of 21.5±0.5° and 23.7±0.5° in a wide-angle x-ray diffraction (WAXD) pattern, and the peak ratio defined by (the peak area at 21.5±0.5°)/(the peak area at 23.7±0.5°) is no more than 3.0. 17-. (canceled)18. A method of producing an olefin block copolymer , comprising:subjecting ethylene or propylene and an α-olefin to copolymerization at a temperature of 70 to 150° C. in the presence of a catalyst composition comprising a metallocene catalyst having a Group IV transition metal and a Lewis base functional group, and a cocatalyst having a Lewis acid element and an organic functional group;wherein at the copolymerization temperature, there occur alternatively between the metallocene catalyst and the cocatalyst a first state in which the Lewis base functional group and the Lewis acid element form an acid-base bond and a second state in which the metallocene catalyst and the cocatalyst has no interaction therebetween; andwherein the Group IV transition metal of the metallocene catalyst and the organic functional group of the cocatalyst do interaction with each other in the first state.19. The method of producing an olefin block copolymer in accordance with claim 18 , wherein the α-olefin is at least one selected from the group consisting of 1-butene claim 18 , 1-pentene claim 18 , 4-methyl-1-pentene claim 18 , 1-hexene claim 18 , 1-heptene claim 18 , 1-octene claim 18 , 1-decene claim 18 , 1-undecene claim 18 , 1-do decene claim 18 , 1-tetradecene claim 18 , 1-hexadecene claim 18 , and 1-itocene.21. The method of producing an olefin block ...

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04-02-2016 дата публикации

METHODS FOR PRODUCING ALPHA-OLEFIN POLYMER AND HYDROGENATED ALPHA-OLEFIN POLYMER

Номер: US20160032033A1
Принадлежит: IDEMITSU KOSAN CO., LTD.

Provided is a method for producing an α-olefin polymer, comprising the step of polymerizing one or more kinds of α-olefins each having 3 to 30 carbon atoms with a polymerization catalyst obtained by using: (A) a metallocene compound; (B) an ionic compound capable of reacting with the metallocene compound to transform the compound into a cation; (C) an organometallic compound; and (D) one or more kinds of compounds selected from the group consisting of (d-1) an alcohol, (d-2) a phenol, and (d-3) an ether compound, the catalyst having a ratio between the component (A) and the component (D) of from 10:1 to 1:100 in terms of a molar ratio, and having a ratio of the component (D) to the component (C) of less than 1 in terms of a molar ratio. 1. A method for producing an α-olefin polymer , comprising:polymerizing one or more α-olefins with a polymerization catalyst;wherein:each of the one or more α-olefins has 3 to 30 carbon atoms; a metallocene compound;', 'an ionic compound capable of reacting with the metallocene compound to transform the metallocene compound into a cation;', 'an organometallic compound; and', 'one or more compounds selected from the group consisting of an alcohol, a phenol, and an ether;, 'the polymerization catalyst comprisesthe polymerization catalyst has a molar ratio of the metallocene compound to the ionic compound of from 10:1 to 1:100, and a molar ratio of the one or more compounds selected from the group consisting of an alcohol, a phenol and an ether to the organometallic compound of less than 1.2. The method according to claim 1 , wherein the metallocene compound is a two-crosslinked metallocene compound.4. The method according to claim 1 , wherein the polymerization catalyst is prepared by:mixing at least the metallocene compound and the organometallic compound to obtain a first mixture, andmixing at least the first mixture and the one or more compounds selected from the group consisting of an alcohol, a phenol and an ether.5. The method ...

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01-02-2018 дата публикации

METHOD OF REDUCING DRAG IN A CONDUIT

Номер: US20180030178A1
Принадлежит:

A method of reducing drag in a conduit. The method includes producing ultra high molecular weight (UHMW) C-Cα-olefin drag reducing agent (DRA) and introducing the UHMW C-Cα-olefin polymer DRA into the conduit to reduce drag in the conduit. The catalyst consists essentially of at least one tertiary monophenyl amine selected from the group consisting of N,N-diethylaniline, N-ethyl-N-methylparatolylamine, N,N-dipropylaniline, N,N-diethylmesitylamine, and combinations thereof; at least one titanium halide having a formula TiX, where m is from 2.5 to 4.0 and X is a halogen containing moiety; and at least one cocatalyst having a formula AlRYwhere R is a hydrocarbon radical, Y is a halogen or hydrogen, and n is 1-20. Further, the catalyst is absent of a carrier or support. 1. A method of reducing drag in a conduit comprising:{'sub': 4', '30, 'claim-text': at least one tertiary monophenyl amine selected from the group consisting of N,N-diethylaniline, N-ethyl-N-methylparatolylamine, N,N-dipropylaniline, N,N-diethylmesitylamine, and combinations thereof;', {'sub': 'm', 'at least one titanium halide having a formula TiX, where m is from 2.5 to 4.0 and X is a halogen containing moiety; and'}, {'sub': n', '3-n, 'at least one cocatalyst having a formula AlRYwhere R is a hydrocarbon radical, Y is a halogen or hydrogen, and n is 1-3; and'}], 'producing a UHMW C-Cα-olefin copolymer DRA by polymerizing in a reactor a first α-olefin monomer in the presence of a catalyst and a hydrocarbon solvent, where the catalyst consists essentially of{'sub': 4', '30, 'introducing the UHMW C-Cα-olefin polymer DRA into the conduit to reduce drag in the conduit.'}2. The method of where the UHMW C-Cα-olefin polymer DRA has a non-crystalline structure.3. The method of where the UHMW C-Cα-olefin polymer DRA has a molecular weight distribution (MWD) of at least 3.25 claim 1 , where MWD is defined as M/Mwith Mw being a weight average molecular weight and Mbeing a number average molecular weight.4. The ...

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17-02-2022 дата публикации

Olefin-Based Polymer

Номер: US20220049030A1
Принадлежит: LG CHEM, LTD.

An olefin-based polymer and method of making the same is disclosed herein. In some embodiments, the olefin-based polymer has multiple crystallinity and satisfies the following: (1) two or more peaks in a temperature range of −20° C. to 120° C. when measured by cross-fractionation chromatography (CFC), and T(90)−T(50)<8.0° C., (2) a soluble fraction (SF) of 1 wt % or less at −20° C. in CFC, (3) 15° C. Подробнее

17-02-2022 дата публикации

Alkane-soluble non-metallocene precatalysts

Номер: US20220049032A1
Принадлежит: Dow Global Technologies LLC

A compound of formula (1) as drawn in the description, wherein M is a Group 4 metal, one R is a silicon-containing organic solubilizing group, and the other R is a silicon-containing organic solubilizing group or a silicon-free organic solubilizing group. A method of synthesizing the compound (1). A solution of compound (1) in alkane solvent. A catalyst system comprising or made from compound (1) and an activator. A method of polymerizing an olefin monomer with the catalyst system.

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30-01-2020 дата публикации

POLYMERIZATION CATALYSTS WITH IMPROVED ETHYLENE ENCHAINMENT

Номер: US20200031958A1
Принадлежит: UNIVATION TECHNOLOGIES, LLC

Embodiments of the present disclosure directed towards polymerization catalysts having improved ethylene enchainment. As an example, the present disclosure provides a polymerization catalyst having improved ethylene enchainment, the polymerization catalyst comprising a zirconocene catalyst of Formula (I) where Ris a Cto Calkyl, aryl or aralkyl group, wherein Ris an Cto Calkyl, aryl or aralkyl group, and where Ris a Cto Calkyl or a hydrogen, and where each X is independently a halide, Cto Calkyl, aralkyl group or hydrogen. 2. The polymerization catalyst of claim 1 , wherein Ris a Calkyl.3. The polymerization catalyst of claim 2 , wherein Ris a Calkyl.4. The polymerization catalyst of claim 3 , wherein Ris a linear Calkyl.5. The polymerization catalyst of claim 3 , wherein Ris an Calkyl.6. The polymerization catalyst of claim 2 , wherein Ris a hydrogen.7. The polymerization catalyst of claim 6 , wherein Ris an Calkyl.8. The polymerization catalyst of claim 6 , wherein Ris a Calkyl.9. The polymerization catalyst of claim 1 , wherein the polymerization catalyst of Formula I is included in a bimodal polymerization catalyst system further including a non-metallocene olefin polymerization catalyst.11. The bimodal polyethylene composition of claim 10 , wherein the low molecular weight polyethylene has a butyl branching frequency of from 0.43 to 0.72. Embodiments of the present disclosure are directed towards polymerization catalysts with improved ethylene enchainment, more specifically, embodiments are directed towards bimodal polymerization catalysts that can be utilized to form bimodal polymers with improved ethylene enchainment.Polymers may be utilized for a number of products including films and pipes, among other. Polymers can be formed by reacting one or more types of monomer in a polymerization reaction. There is continued focus in the industry on developing new and improved materials and/or processes that may be utilized to form polymers.Ethylene alpha-olefin ( ...

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30-01-2020 дата публикации

TIRE SIDEWALL SUPPORT FOR RUNFLAT TIRE

Номер: US20200031963A1
Принадлежит:

A sidewall support and/or a bead apex that is manufactured from a rubber composition that is based upon a cross-linkable rubber composition comprising a rubber component selected from the group consisting of a polybutadiene and at least one of a natural rubber and a polyisoprene. Such rubber compositions may further include a carbon black and also include a sulfur curing agent and a peroxide curing agent. 1. A run-flat tire having a sidewall support and a bead apex , the sidewall support and/or the bead apex manufactured from a rubber composition that is based upon a cross-linkable rubber composition , the cross-linkable rubber composition comprising , per 100 parts by weight of rubber (phr):a rubber component selected from the group consisting of a polybutadiene and at least one of a natural rubber and a polyisoprene;a carbon black reinforcing filler; anda sulfur curing agent and a peroxide curing agent.2. The run-flat tire of claim 1 , wherein the cross-linkable elastomer composition comprises between 30 phr and 75 phr of the carbon black.3. The run-flat tire of claim 2 , wherein the cross-linkable elastomer composition comprises between 35 phr and 60 phr of the carbon black.4. The fun-flat tire of claim 1 , wherein the carbon black is a low-surface area claim 1 , high-structure carbon black having a nitrogen surface area of between 15 m/g and 25 m/g and a COAN of between 65 ml/100 g and 85 ml/100 g.5. The run-flat tire of claim 1 , wherein an OAN of the low-surface area claim 1 , high-structure carbon black is between 100 ml/100 g and 150 ml/100 g.6. The run-flat tire of claim 1 , wherein an iodine number of the low-surface area claim 1 , high-structure carbon black is between 10 mg/g and 25 mg/g.7. The run-flat tire of claim 1 , wherein the cross-linkable rubber composition comprises between 0 phr and 15 phr of an additional rubber component selected from the group consisting of a butadiene copolymer claim 1 , an isoprene copolymer and mixtures of these ...

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04-02-2021 дата публикации

Olefin polymerization activators

Номер: US20210032382A1
Принадлежит: Dow Global Technologies LLC

Embodiments of this disclosure include processes of polymerizing olefins, the process comprising contacting ethylene and a (C 3 -C 40 )alpha-olefin comonomer in the presence of a catalyst system, the catalyst system comprising a Group IV metal-ligand complex and an ionic metallic activator complex, the ionic metallic activator complex comprising an anion and a countercation, the anion having a structure according to formula (I):formula (I)

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04-02-2021 дата публикации

Polyethylene Copolymer and Method for Preparing Same

Номер: US20210032449A1
Принадлежит: LG CHEM, LTD.

The present invention relates to a polyethylene copolymer which has excellent processability and long-term durability, and thus is useful for hollow molding of a pipe or the like. 1. A polyethylene copolymer comprising an ethylene-derived repeating unit and an alpha-olefin-derived repeating unit having 3 or more carbon atoms , and satisfying the following Equation 1 and Equation 2:{'br': None, 'sup': '1/2', 'SCG index≤(carbon number of the alpha olefin)×5\u2003\u2003[Equation 1]'}wherein, in the above Equation 1, {'br': None, 'i': 'c/d', 'Comonomer distribution index (CDI)=\u2003\u2003[Equation 2]'}, 'the SCG index is a value (p/q) obtained by dividing melt index (p) of the polyethylene copolymer measured according to ASTM 1238 (load of 21.6 kg, 190° C.) by comonomer distribution index (q) of the polyethylene copolymer, and'}wherein, in the above Equation 1,the comonomer distribution index (CDI) is calculated by the above Equation 2 based on a molecular weight distribution curve graph, measured by gel permeation chromatography with respect to the polyethylene copolymer, where the x-axis represents the molecular weight of the polymer chain and the y-axis represents the content of the polymer chain,c is short-chain branch (SCB) content (measured by FT-IR) of 2 to 7 carbon atoms per 1000 carbon atoms of the polymer chain, which is a molecular weight value m in which an area (s1) between the molecular weight distribution curve and the x-axis in the section of a≤x≤m is 80% of the area (s2) between the molecular weight distribution curve and the x-axis in the section of a≤x≤b,d is short chain branch (SCB) content (measured by FT-IR) of 2 to 7 carbon atoms per 1000 carbon atoms of the polymer chain, which is a molecular weight value n in which an area (s3) between the molecular weight distribution curve and the x-axis in the section of a≤x≤n is 20% of the area (s4) between the molecular weight distribution curve and the x-axis in the section of a≤x≤b, anda is the minimum ...

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04-02-2021 дата публикации

ETHYLENE COPOLYMERS AND FILMS WITH EXCELLENT SEALING PROPERTIES

Номер: US20210032450A1
Принадлежит: NOVA CHEMICALS (INTERNATIONAL) S.A.

An ethylene copolymer composition comprises: a first ethylene copolymer having a density of from 0.855 to 0.913 g/cm, a molecular weight distribution, M/Mof from 1.7 to 2.3, and a melt index, 12 of from 0.1 to 20 g/10 min; a second ethylene copolymer having a density of from 0.875 to 0.936 g/cm, a molecular weight distribution, M/Mof from 2.3 to 6.0, and a melt index, 12 of from 0.3 to 100 g/10 min; and optionally a third ethylene copolymer; where the first ethylene copolymer has more short chain branches per thousand carbon atoms than the second ethylene copolymer and the density of the second ethylene copolymer is equal to or higher than the density of the first ethylene copolymer. The ethylene copolymer composition has a density of from 0.865 to 0.913 g/cm; a melt index, 12 of from 0.5 to 10 g/10 min; and a fraction eluting at from 90 to 105° C., having an integrated area of greater than 4 weight percent in a CTREF analysis; and at least 0.0015 parts per million (ppm) of hafnium. 1. An ethylene copolymer composition comprising:{'sup': '3', 'sub': w', 'n', '2, '(i) from 20 to 80 weight percent of a first ethylene copolymer having a density of from 0.855 to 0.913 g/cm; a molecular weight distribution, M/Mof from 1.7 to 2.3; and a melt index, Iof from 0.1 to 20 g/10 min;'}{'sup': '3', 'sub': w', 'n', '2, '(ii) from 80 to 20 weight percent of a second ethylene copolymer having a density of from 0.875 to 0.936 g/cm; a molecular weight distribution, M/Mof from 2.3 to 6.0; and a melt index, Iof from 0.3 to 100 g/10 min; and'}(iii) from 0 to 40 weight percent of a third ethylene copolymer;wherein the number of short chain branches per thousand carbon atoms in the first ethylene copolymer (SCB1) is greater than the number of short chain branches per thousand carbon atoms in the second ethylene copolymer (SCB2);wherein the density of the second ethylene copolymer is equal to or greater than the density of the first ethylene copolymer;{'sup': '3', 'sub': '2', 'wherein the ...

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07-02-2019 дата публикации

TRI-N-OCTYL ALUMINUM CO-CATALYST FOR HIGHER DENSITY HOMOPOLYMERS FOR THE SOLUTION PROCESS

Номер: US20190040162A1
Принадлежит: Equistar Chemicals, LP

Catalyst systems and solution olefin polymerization processes using a combination of titanium compounds (e.g. halides) with vanadium compounds (e.g. halides or oxyhalides) with tri-n-octyl aluminum (TNOAL) as a co-catalyst, which provides lower in situ oligomerization of olefins that are incorporated into the homopolymer. This feature provides a higher density homopolymer using TNOAL, which enhances polymer properties such as increased moisture barrier and stiffness. Multi-reactor systems and solution olefin polymerization processes comprising this catalyst system. 1. A process for polymerizing olefins , the process comprising:a) contacting an olefin composition comprising ethylene with a catalyst system in a reactor, the catalyst system comprising a titanium halide, a vanadium halide, and tri-n-octyl aluminum co-catalyst; andb) forming a polyethylene under olefin polymerization conditions which provide a polyethylene homopolymer having a higher homopolymer density at equivalent homopolymer Melt Index (MI), as compared to a polyethylene homopolymer made under the olefin polymerization conditions with a reference catalyst system comprising the titanium halide, the vanadium halide, and triethyl aluminum co-catalyst.2. The process of claim 1 , wherein the olefin composition is absent an α-olefin co-monomer and the polyethylene is a polyethylene homopolymer.3. The process of claim 1 , wherein the olefin composition further comprises an α-olefin co-monomer is selected from propylene claim 1 , 1-butene claim 1 , 1-pentene claim 1 , 1-hexene claim 1 , 1-octene claim 1 , or 4-methyl-1-pentene claim 1 , and the polyethylene is a polyethylene co-polymer.4. The process of claim 1 , wherein the titanium halide comprises titanium trichloride (TiCl) or titanium tetrachloride (TiCl) claim 1 , and wherein the vanadium halide comprises vanadium oxytrichloride (VOCl) or vanadium tetrachloride (VCl).5. The process of claim 1 , wherein the molar ratio of the tri-n-octyl aluminum co- ...

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12-02-2015 дата публикации

Methods for Controlling Dual Catalyst Olefin Polymerizations With An Alcohol Compound

Номер: US20150045521A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

Methods for controlling properties of an olefin polymer using an alcohol compound are disclosed. The MI and the HLMI of the polymer can be decreased, and the Mw and the Mz of the polymer can be increased, via the addition of the alcohol compound. 1. A method of controlling a polymerization reaction in a polymerization reactor system , the method comprising:(i) contacting a dual catalyst system with an olefin monomer and an optional olefin comonomer in the polymerization reactor system under polymerization conditions to produce an olefin polymer,wherein the dual catalyst system comprises a first metallocene catalyst component, a second metallocene catalyst component, an activator, and a co-catalyst; and(ii) introducing an amount of an alcohol compound into the polymerization reactor system to (I) reduce a melt index parameter of the olefin polymer; (II) increase a molecular weight parameter of the olefin polymer selected from Mw, Mz, or both; or (III) reduce a melt index parameter of the olefin polymer and increase a molecular weight parameter of the olefin polymer selected from Mw, Mz, or both.2. The method of claim 1 , wherein the alcohol compound comprises methanol claim 1 , ethanol claim 1 , propanol claim 1 , butanol claim 1 , pentanol claim 1 , hexanol claim 1 , heptanol claim 1 , octanol claim 1 , decanol claim 1 , hexadecanol claim 1 , cyclohexanol claim 1 , phenol claim 1 , benzyl alcohol claim 1 , or a combination thereof.3. The method of claim 1 , wherein the dual catalyst system comprises:a first metallocene catalyst component comprising an unbridged metallocene compound containing zirconium;a second metallocene catalyst component comprising a bridged metallocene compound containing zirconium or hafnium;an activator comprising an activator-support, an aluminoxane compound, an organoboron or organoborate compound, an ionizing ionic compound, or any combination thereof; anda co-catalyst comprising an organoaluminum compound.4. The method of claim 3 , ...

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16-02-2017 дата публикации

Diluent for the production of butyl rubber

Номер: US20170044283A1

Methods are provided to efficiently produce butyl rubber via a slurry polymerization process. The process comprises providing at least two monomers, wherein at least one monomer is an isoolefin and at least one monomer is a multiolefin. The monomers are combined with an initiator and an organic diluent comprising 40-60 volume % of methyl chloride and 40-60 volume % of 1,1,1, 2-tetrafluoroethane and polymerized.

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25-02-2021 дата публикации

OLEFIN POLYMERIZATION ACTIVATORS

Номер: US20210054119A1
Принадлежит: Dow Global Technologies LLC

Embodiments of this disclosure include processes of polymerizing olefins, the process comprising contacting ethylene and a (C-C)alpha-olefin comonomer in the presence of a catalyst system, the catalyst system comprising a Group IV metal-ligand complex and a metallic activator ionic complex, the metallic activator ionic complex comprising an anion and a countercation, the anion having a structure according to formula (I): 2. The process for polymerizing olefins according to claim 1 , wherein the procatalyst is a bis-biphenylphenoxy Group IV metal-ligand complex.3. The process for polymerizing olefins according to claim 1 , wherein n is 0 and each X group is independently −C(H)(CF) claim 1 , —CF claim 1 , or —C(CF).4. The process for polymerizing olefins according to claim 1 , wherein n is 1 claim 1 , and R is −C(CF)and each X is —CF.5. The process for polymerizing olefins according to claim 1 , wherein n is 0 claim 1 , and three of the four X groups are —CF.6. The process for polymerizing olefins according to claim 1 , wherein n is 0 claim 1 , and all four X groups are —CF.7. The process for polymerizing olefins according to claim 1 , wherein the countercation is chosen from substituted ammonium claim 1 , substituted and unsubstituted triarylcarbonium or substituted and unsubstituted ferrocenium.8. The process for polymerizing olefins according to claim 1 , wherein the countercation is N(H)R claim 1 , where each Ris independently chosen from (C-C)alkyl or (C-C)aryl.9. The process for polymerizing olefins according to claim 6 , wherein the countercation is N(H)R claim 6 , where at least two Rare independently chosen from (C-C)alkyl.10. The process for polymerizing olefins according to claim 1 , wherein the countercation is C(CH).11. The process for polymerizing olefins according to claim 1 , wherein the countercation is C(CHR) claim 1 , wherein Ris (C-C)alkyl.12. The process for polymerizing olefins according to claim 1 , wherein n is 0.14. The process for ...

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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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08-05-2014 дата публикации

Low Density Polyolefin Resins and Films Made Therefrom

Номер: US20140128563A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

Disclosed herein are broad molecular weight distribution olefin polymers having densities in the 0.895 to 0.930 g/cmrange, and with improved impact and tear resistance. These polymers can have a ratio of Mw/Mn in the 8 to 35 range, a high load melt index in the 4 to 50 range, less than about 0.008 LCB per 1000 total carbon atoms, and a reverse comonomer distribution. 1. An olefin polymer comprising a higher molecular weight component and a lower molecular weight component , wherein the olefin polymer has:{'sup': '3', 'a density in a range from about 0.895 to about 0.930 g/cm;'}a ratio of Mw/Mn in a range from about 8 to about 35;a HLMI in a range from about 4 to about 50 g/10 min;less than about 0.008 LCB per 1000 total carbon atoms; anda reverse comonomer distribution.2. The polymer of claim 1 , wherein the olefin polymer has a ratio of HLMI/MI in a range from about 50 to about 300.3. The polymer of claim 1 , wherein the olefin polymer has:a Mw in a range from about 100,000 to about 600,000 g/mol; anda Mn in a range from about 10,000 to about 25,000 g/mol.4. The polymer of claim 1 , wherein the olefin polymer has a density in a range from about 0.905 to about 0.925 g/cm.5. The polymer of claim 1 , wherein the olefin polymer has a HLMI in a range from about 4 to about 35 g/10 min.6. The polymer of claim 1 , wherein the olefin polymer has less than about 0.005 LCB per 1000 total carbon atoms.7. The polymer of claim 1 , wherein the olefin polymer has a ratio of HLMI/MI in a range from about 70 to about 250.8. The polymer of claim 1 , wherein the olefin polymer has a Mw in a range from about 150 claim 1 ,000 to about 500 claim 1 ,000 g/mol.9. The polymer of claim 1 , wherein the olefin polymer has a ratio of Mz/Mw in a range from about 3 to about 12.10. The polymer of claim 1 , wherein the olefin polymer has a ratio of the Mw of the higher molecular weight component to the Mw of the lower molecular weight component in a range from about 5:1 to about 50:1.11. The ...

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13-02-2020 дата публикации

POLYETHYLENE COPOLYMERS HAVING A PARTICULAR COMONOMER DISTRIBUTION

Номер: US20200048379A1
Автор: Kuhlman Roger L.
Принадлежит: UNIVATION TECHNOLOGIES, LLC

Novel polyethylene copolymers having a relatively high comonomer partitioning tendency are disclosed as are methods for their preparation. The comonomer partitioning tendency is the tendency for a copolymer to have comonomer in the higher molecular weight chains. Novel metrics for describing the comonomer partitioning tendency are also disclosed. 1. A method for preparing a polyethylene copolymer having a comonomer partitioning tendency of greater than 1.16 by polymerizing ethylene and one or more comonomers in the presence of one or more catalyst compositions.2. A method according to claim 1 , wherein the one or more catalyst compositions comprises a catalyst compound having a titanium claim 1 , a zirconium or a hafnium atom.3. A method according to claim 2 , wherein the catalyst composition comprises two or more catalyst compounds comprising a titanium claim 2 , a zirconium or a hafnium atom.4. A method according to any one of to claim 2 , wherein the catalyst composition further comprises one or more activators or co-catalysts.9. A method according to any one of to wherein the catalyst composition comprises two or more of the catalyst compounds according to any one of to in any ratio.10. A method according to any one of to claim 2 , wherein the comonomer is one or more comonomers containing 3 to 16 carbon atoms.11. A method according to any one of to claim 2 , wherein the polymerization is performed in gas phase claim 2 , slurry phase claim 2 , solution phase claim 2 , high pressure or combinations thereof.12. A method according to any one of to claim 2 , wherein the polymerization is performed in a single gas phase reactor. This application is a Divisional of U.S. National Stage Application Ser. No. 15/568,662 filed Oct. 23, 2017 and published as U.S. Publication No. 2018-0155473 A1 on Jun. 7, 2018, which claims priority to International Application Number PCT/US2016/028545, filed Apr. 21, 2016 and published as WO 2016/172279 on Oct. 27, 2016, which claims the ...

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22-02-2018 дата публикации

CATALYST COMPOSITION FOR MAKING ULTRA HIGH MOLECULAR WEIGHT POLY (ALPHA-OLEFIN) DRAG REDUCING AGENTS

Номер: US20180051110A1
Принадлежит:

A catalyst consisting essentially of at least one tertiary monophenyl amine having a formula RRN-aryl, where Rand Rare the same or different, and each is a hydrogen, an alkyl, or a cycloalkyl group, where at least one of Rand Rcontain at least one carbon atom; at least one titanium halide having a formula TiX, where m is from 2.5 to 4.0 and X is a halogen containing moiety; and at least one cocatalyst having a formula AlRYwhere R is a hydrocarbon radical, Y is a halogen or hydrogen, and n is 1-3. Further, the catalyst is absent of a carrier or support. 1. A catalyst consisting essentially of:{'sup': 1', '2', '1', '2', '1', '2, 'at least one tertiary monophenyl amine having the formula RRN-aryl, where Rand Rmay each be a hydrogen, an alkyl, or a cycloalkyl group with the proviso that at least one of Rand Rcontains at least one carbon atom;'}{'sub': 'm', 'at least one titanium halide having a formula TiX, where m is from 2.5 to 4.0 and X is a halogen containing moiety; and'}{'sub': n', '3-n, 'at least one cocatalyst having a formula AlRYwhere R is a hydrocarbon radical, Y is a halogen or hydrogen, and n is 1-3,'}where the catalyst is absent a carrier or support.2. The catalyst of where at least one tertiary monophenyl amine is selected from the group consisting of N claim 1 ,N-diethylaniline claim 1 , N-ethyl-N-methylparatolylamine claim 1 , N claim 1 ,N-dipropylaniline claim 1 , N claim 1 ,N-diethylmesitylamine claim 1 , and combinations thereof.3. The catalyst of where the cocatalyst is Al(CHCH)Cl.4. The catalyst of where the titanium halide is TiCl⅓AlCl.5. The catalyst of where the cocatalyst comprises one or more organoaluminum compounds selected from the group consisting of trimethyl aluminum claim 1 , triethyl aluminum claim 1 , tri-n-proyl aluminum claim 1 , tri-n-butyl aluminum claim 1 , tri-isobutyl aluminum claim 1 , tri-n-hexyl aluminum claim 1 , tri(2-methylpentyl) aluminum claim 1 , tri-n-octyl aluminum claim 1 , diethyl aluminum hydride claim 1 , ...

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23-02-2017 дата публикации

METHOD FOR ALTERING MELT FLOW RATIO OF ETHYLENE POLYMERS

Номер: US20170051091A1
Принадлежит: NOVA CHEMICALS (INTERNATIONAL) S.A.

A method for altering the melt flow ratio (MFR) of ethylene copolymers made in a gas phase reactor using a supported Ziegler-Natta catalyst treated with a catalyst modifier. The method involves changing the amount of the catalyst modifier added to the supported Ziegler-Natta polymerization catalyst to effect changes in the MFR of the resulting polymer. 2. The method of wherein the catalyst modifier comprises at least one compound of the formula: RN((CH)OH)((CH)OH) where Ris a hydrocarbyl group having from 5 to 30 carbon atoms claim 1 , and n and m are integers from 1 to 20.3. The method of wherein the catalyst modifier comprises at least one compound of the formula: RN((CH)OH)where Ris a hydrocarbyl group having from 6 to 30 carbon atoms claim 1 , and x is independently an integer from 1 to 20.4. The method of wherein the catalyst modifier comprises at least one compound of the formula: RN((CH)OH)where Ris a hydrocarbyl group having from 6 to 30 carbon atoms claim 1 , and x is 2 or 3.5. The method of wherein the catalyst modifier comprises at least one compound of the formula: RN(CHCHOH)where Ris a hydrocarbyl group having from 8 to 22 carbon atoms.6. The method of wherein the catalyst modifier comprises a compound of the formula: CFN(CHCHOH).7. The method of wherein the catalyst modifier comprises compounds of the formulas: CHN(CHCHOH)and ClHN(CHCHOH).8. The method of wherein the catalyst modifier comprises a mixture of compounds of the formula: RN(CHCHOH)where Ris a hydrocarbyl group having from 8 to 18 carbon atoms.9. The method of wherein the polymerization catalyst is produced in a process wherein the catalyst modifier is added at any step during production of the Ziegler-Natta type catalyst combined with the inert support.10. The method of wherein the amount of catalyst modifier added to the polymerization catalyst is at least 0.75 wt % based on the weight of a) claim 1 , b) claim 1 , and c) of the polymerization catalyst.11. The method of wherein the amount ...

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10-03-2022 дата публикации

Organometallic chain transfer agents

Номер: US20220073539A1
Принадлежит: Dow Global Technologies LLC

Embodiments relate to organometallic compositions that are useful for chain transfer during olefin polymerization. Such compositions are chain transfer agents comprising an organoaluminum compound of the formula Al(CH2CH(Y2)A2)3 and an organozinc compound of the formula Zn(CH2CH(Y2)A2)2.

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10-03-2022 дата публикации

CURABLE COMPOSITIONS COMPRISING UNSATURATED POLYOLEFINS

Номер: US20220073540A1
Принадлежит:

The present disclosure relates to unsaturated polyolefins and processes for preparing the same. The present disclosure further relates to curable formulations comprising the unsaturated polyolefins that show improved crosslinking. 1. A curable composition comprising (A) a polyolefin component comprising an unsaturated polyolefin of the formula ALthat has a viscosity less than 100 ,000 cP and (B) a curing component comprising a cross-linking agent , wherein:{'sup': '1', 'Lis a polyolefin;'}{'sup': 1', '1', '1', '1', '1', '1', '1', '1', '1, 'sub': 2', '2', '2', '2, 'Ais selected from the group consisting of a vinyl group, a vinylidene group of the formula CH═C(Y)—, a vinylene group of the formula YCH═CH—, a mixture of a vinyl group and a vinylene group of the formula YCH═CH—, a mixture of a vinyl group and a vinylidene group of the formula CH═C(Y)—, a mixture of a vinylidene group of the formula CH═C(Y)— and a vinylene group of the formula YCH═CH—, and a mixture of a vinyl group, a vinylidene group of the formula CH═C(Y)—, and a vinylene group of the formula YCH═CH—; and'}{'sup': '1', 'sub': 1', '30, 'Yat each occurrence independently is a Cto Chydrocarbyl group.'}2. A curable composition comprising (A) a polyolefin component comprising a telechelic polyolefin of the formula ALLAthat has a viscosity less than 100 ,000 cP and (B) a curing component comprising a cross-linking agent , wherein:{'sup': '1', 'Lis a polyolefin;'}{'sup': 1', '1', '1', '1', '1', '1', '1', '1', '1, 'sub': 2', '2', '2', '2, 'Ais selected from the group consisting of a vinyl group, a vinylidene group of the formula CH═C(Y)—, a vinylene group of the formula YCH═CH—, a mixture of a vinyl group and a vinylene group of the formula YCH═CH—, a mixture of a vinyl group and a vinylidene group of the formula CH═C(Y)—, a mixture of a vinylidene group of the formula CH═C(Y)— and a vinylene group of the formula YCH═CH—, and a mixture of a vinyl group, a vinylidene group of the formula CH═C(Y)—, and a ...

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10-03-2022 дата публикации

TELECHELIC POLYOLEFINS AND PROCESSES FOR PREPARING THE SAME

Номер: US20220073658A1
Принадлежит:

The present disclosure relates to novel telechelic polyolefins of the formula (I) and processes for preparing the same. In at least one aspect, the telechelic polyolefins of the formula (I) comprise unsaturations at both termini. 2. The telechelic polyolefin of claim 1 , wherein Lis an ethylene-based polymer.3. The telechelic polyolefin of or claim 1 , wherein Lis an ethylene homopolymer or an ethylene/alpha-olefin copolymer comprising units derived from ethylene and a Cto Calpha-olefin.4. The telechelic polyolefin of claim 3 , wherein the Cto Calpha-olefin is selected from the group consisting of propylene claim 3 , 1-butene claim 3 , 1-hexene claim 3 , and 1-octene.5. The telechelic polyolefin of any of the preceding claims claim 3 , wherein the hindered double bond is selected from the group consisting of the double bond of a vinylidene group claim 3 , the double bond of a vinylene group claim 3 , the double bond of a trisubstituted alkene claim 3 , and the double bond of a vinyl group attached to a branched alpha carbon.6. The telechelic polyolefin of any of the preceding claims claim 3 , wherein Ais a Cto Ccyclic hydrocarbyl group or a Cto Cacyclic hydrocarbyl group.7. The telechelic polyolefin of any of the preceding claims claim 3 , wherein Ais selected from the group consisting of an unsubstituted cycloalkene claim 3 , an alkyl-substituted cycloalkene claim 3 , and an acyclic alkyl group.9. The telechelic polyolefin of any of the previous claims claim 3 , wherein the telechelic polyolefin of the formula (I) comprises a weight average molecular weight (Mw) range from 1 claim 3 ,000 to 1 claim 3 ,000 claim 3 ,000 g/mol.10. The telechelic polyolefin of any of the previous claims claim 3 , wherein Lis covalently bonded to each of Aand Lthrough carbon-carbon single bonds claim 3 , and wherein Lis covalently bonded to Athrough a carbon-carbon single bond.11. A composition comprising the telechelic polyolefin of any of the previous claims.12. A process for ...

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10-03-2022 дата публикации

4-METHYL-1-PENTENE/alpha-OLEFIN COPOLYMER, COMPOSITION COMPRISING THE COPOLYMER AND 4-METHYL-1-PENTENE COPOLYMER COMPOSITION

Номер: US20220073659A1
Принадлежит: Mitsui Chemicals, Inc.

The present invention provides a 4-methyl-1-pentene/α-olefin copolymer being excellent in lightness, stress absorption, stress relaxation, vibration damping properties, scratch resistance, abrasion resistance, toughness, mechanical properties and flexibility, having no stickiness during molding operation and being excellent in the balance among these properties; a composition comprising the polymer; and uses thereof. The 4-methyl-1-pentene/α-olefin copolymer (A) of the present invention satisfies specific requirements, and comprises 5 to 95 mol % of a structural unit (i) derived from 4-methyl-1-pentene, 5 to 95 mol % of a structural unit (ii) derived from at least one kind of α-olefin selected from α-olefins having 2 to 20 carbon atoms excluding 4-methyl-1-pentene and 0 to 10 mol % of a structural unit (iii) derived from a non-conjugated polyene, provided that the total of the structural units (i), (ii), and (iii) is 100 mol %. 1. A 4-methyl-1-pentene/α-olefin copolymer composition (X21) comprising:50 to 95 parts by weight of the 4-methyl-1-pentene/α-olefin copolymer (A2) comprising 50 to 75 mol % of a structural unit (i) derived from 4-methyl-1-pentene, 50 to 25 mol % of a structural unit (ii) derived from at least one kind of α-olefin selected from ethylene and propylene and 0 to 5 mol % of a structural unit (iii) derived from a non-conjugated polyene, provided that the total of the structural units (i), (ii), and (iii) is 100 mol %, wherein the copolymer (A2) satisfies the following requirements (a) to (d) and (e1):(a): the intrinsic viscosity [η], as measured in decalin at 135° C., is 0.01 to 1.7 dL/g,(b): the ratio (Mw/Mn) of a weight-average molecular weight (Mw) to a number-average molecular weight (Mn), as measured by gel permeation chromatography (GPC), is 1.0 to 3.5,(c): the tensile modulus (YM) is 0.1 to 1000 MPa,(d): the melting point [Tm], as measured by differential scanning calorimetry (DSC), is lower than 110° C. or not observed, and {'br': None, 'i ...

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10-03-2022 дата публикации

CURABLE COMPOSITIONS COMPRISING UNSATURATED POLYOLEFINS

Номер: US20220073716A1
Принадлежит:

The present disclosure relates to unsaturated polyolefins and processes for preparing the same. The present disclosure further relates to curable formulations comprising the unsaturated polyolefins that show improved crosslinking. 1. A curable composition for a cable insulation layer , the curable composition comprising (A) a polyolefin component comprising an unsaturated polyolefin of the formula ALand (B) a curing component comprising a cross-linking agent , wherein:{'sup': '1', '#text': 'Lis a polyolefin;'}{'sup': ['1', '1', '1', '1', '1', '1', '1', '1', '1'], 'sub': ['2', '2', '2', '2'], '#text': 'Ais selected from the group consisting of a vinyl group, a vinylidene group of the formula CH═C(Y)—, a vinylene group of the formula YCH═CH—, a mixture of a vinyl group and a vinylene group of the formula YCH═CH—, a mixture of a vinyl group and a vinylidene group of the formula CH═C(Y)—, a mixture of a vinylidene group of the formula CH═C(Y)— and a vinylene group of the formula YCH═CH—, and a mixture of a vinyl group, a vinylidene group of the formula CH═C(Y)—, and a vinylene group of the formula YCH═CH—; and'}{'sup': '1', 'sub': ['1', '30'], '#text': 'Yat each occurrence independently is a Cto Chydrocarbyl group.'}2. A curable composition for a cable insulation layer , the curable composition comprising (A) a polyolefin component comprising a telechelic polyolefin of the formula ALLAand (B) a curing component comprising a cross-linking agent , wherein:{'sup': '1', '#text': 'Lis a polyolefin;'}{'sup': ['1', '1', '1', '1', '1', '1', '1', '1', '1'], 'sub': ['2', '2', '2', '2'], '#text': 'Ais selected from the group consisting of a vinyl group, a vinylidene group of the formula CH═C(Y)—, a vinylene group of the formula YCH═CH—, a mixture of a vinyl group and a vinylene group of the formula YCH═CH—, a mixture of a vinyl group and a vinylidene group of the formula CH═C(Y)—, a mixture of a vinylidene group of the formula CH═C(Y)— and a vinylene group of the formula YCH═CH—, ...

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10-03-2022 дата публикации

RANDOM PROPYLENE POLYMER COMPOSITION AND USE IN EXTRUSION BLOW MOULDING

Номер: US20220073718A1
Принадлежит:

The present invention is directed to a propylene polymer composition comprising at least one propylene copolymer (C-PP), and an α-nucleating agent (NU), wherein the propylene copolymer (C-PP) comprises two propylene copolymer fractions (PP1) and (PP2), wherein propylene copolymer fraction (PP1) is contained in the propylene copolymer (C-PP) in an amount of 30 to 70 wt. % and the propylene copolymer fraction (PP2) is contained in the propylene copolymer (C-PP) in an amount of 70 to 30 wt. %, the comonomer content of propylene copolymer fraction (PP1) is in the range of 0.5 to 2.5 wt.-% and the comonomer content of the propylene copolymer fraction (PP1) is lower compared to the comonomer content of the propylene copolymer fraction (PP2), and the propylene polymer composition has (a) a melt flow rate MFR(230° C.) measured according to according to ISO 1133 of 1 to 5 g/10 min., and (b) a comonomer content of 4.0 to 8.0 wt. %, the comonomer(s) being ethylene and/or at least one Cto Cα-olefin. The above propylene polymer composition has improved impact and optical properties. The invention further provides a method of producing the above propylene polymer composition and an extrusion blow molded article comprising the above propylene polymer composition. 1. A propylene polymer composition comprising at least one propylene copolymer (C-PP) , and an α-nucleating agent (N) , wherein the propylene copolymer (C-PP) comprises two propylene copolymer fractions (PP1) and (PP2) , whereinpropylene copolymer fraction (PP1) is contained in the propylene copolymer (C-PP) in an amount of 30 to 70 wt. % and the propylene copolymer fraction (PP2) is contained in the propylene copolymer (C-PP) in an amount of 70 to 30 wt. %,the comonomer content of propylene copolymer fraction (PP1) is in the range of 0.5 to 2.6 wt.-% and the comonomer content of the propylene copolymer fraction (PP1) is lower compared to the comonomer content of the propylene copolymer fraction (PP2), and the propylene ...

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21-02-2019 дата публикации

STRETCHABLE STRUCTURE, MULTILAYERED STRETCHABLE SHEET, SPUN YARN, AND FIBER STRUCTURE

Номер: US20190054719A1
Принадлежит: Mitsui Chemicals, Inc.

An object of the present invention is to provide a stretchable structure that has stretchability together with high stress relaxation properties, and provides fit feeling with less tightening by recovering slowly after stretching. The object is achieved by a stretchable structure having the following characteristics: a tensile permanent set (PS ) of 1% or more and 50% or less, wherein the tensile permanent set (PS) is a value obtained 10 minutes after 150% elongation at a tension rate of 200 mm/minute in accordance with JIS K and a ratio PS/PSof 1.10 or more, wherein the PSis the tensile permanent set obtained 10 minutes after the elongation and the PSis the tensile permanent set obtained 1 minute after the elongation. 1. A stretchable structure having following characteristics:{'sub': 10M', '10M, 'a tensile permanent set (PS) of 1% or more and 50% or less, wherein the tensile permanent set (PS) is a value obtained 10 minutes after 150% elongation at a tension rate of 200 mm/minute in accordance with JIS K7127, and'}{'sub': 1M', '10M', '10M', '1M, 'a ratio PS/PSof 1.10 or more, wherein the PSis the tensile permanent set obtained 10 minutes after the elongation and the PSis the tensile permanent set obtained 1 minute after the elongation.'}2. The stretchable structure according to claim 1 , wherein a surface layer (Z) including a thermoplastic elastomer (C) is laminated on a surface of a core layer (Y) including a resin composition (X) which contains a 4-methyl-1-pentene/α-olefin copolymer (A) satisfying the following requirement (a):Requirement (a): the copolymer (A) contains 50 to 90 mol % of a structural unit (i) derived from 4-methyl-1-pentene and 10 to 50 mol % of a structural unit (ii) derived from an α-olefin (excluding 4-methyl-1-pentene), a total of the structural unit (i) and the structural unit (ii) being 100 mol %.3. The stretchable structure according to claim 2 , wherein the thermoplastic elastomer (C) is at least one member selected from a polyolefin- ...

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15-05-2014 дата публикации

METHOD FOR PRODUCING OLEFIN POLYMER

Номер: US20140135461A1
Принадлежит: IDEMITSU KOSAN CO., LTD.

A method for producing an olefin polymer including: polymerizing one or more α-olefins each having 6 to 20 carbon atoms in the presence of a metallocene catalyst to obtain an olefin polymer; deactivating and decalcifying the catalyst to obtain a decalcified polymerization reaction liquid; mixing the decalcified polymerization reaction liquid containing the olefin polymer with water; and washing the liquid with stirring at a stirring intensity of 0.1 kW/mor more for 1 minute or longer. 1. A method for producing an olefin polymer , comprising:polymerizing an α-olefin having 6 to 20 carbon atoms in the presence of a metallocene catalyst to obtain an olefin polymer;deactivating and decalcifying the catalyst to obtain a decalcified polymerization reaction liquid;mixing the decalcified polymerization reaction liquid comprising the olefin polymer with water; and{'sup': '3', 'washing the liquid with stirring at a stirring intensity of 0.1 kW/mor more for 1 minute or longer.'}2. The method according to claim 1 , wherein the mixing with water takes presence in a continuous flow stirring chamber.3. An olefin polymer obtained by the method according to .4. An olefin polymer obtained by the method according to . The invention relates to a method for producing an olefin polymer and an olefin polymer obtained by this method.An olefin polymer is manufactured in recent years using a metallocene-based catalyst, and used as a wax component or a lubricating oil component. In the production of an olefin polymer, in order to deactivate a catalyst after the completion of a polymerization reaction or in order to remove metal components derived from a polymerization reaction catalyst, in general, an aqueous alkaline solution such as sodium hydroxide and a polymerization reaction liquid are mixed (liquid-liquid mixture), whereby metal components are extracted in an aqueous alkaline phase. When a product is manufactured without removing the metal component in the polymerization reaction ...

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21-02-2019 дата публикации

Low Density Polyolefin Resins With Low Molecular Weight and High Molecular Weight Components, and Films Made Therefrom

Номер: US20190055329A1
Принадлежит: Chevron Phillips Chemical Co LP

Disclosed herein are ethylene-based polymers produced using dual metallocene catalyst systems. These polymers have low densities, high molecular weights, and broad molecular weight distributions, as well as having the majority of the long chain branches in the lower molecular weight component of the polymer, and the majority of the short chain branches in the higher molecular weight component of the polymer. Films produced from these polymers have improved impact and puncture resistance.

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05-03-2015 дата публикации

Adhesive using wire pigment and manufacturing method thereof

Номер: US20150065602A1
Принадлежит: Samsung Electro Mechanics Co Ltd

The present invention relates to an adhesive using wire pigments and a manufacturing method thereof. According to an embodiment of the present invention, an adhesive using wire pigments, which includes an adhesive resin composition including a photocurable adhesive material; and wire pigments formed in a nano-sized wire structure to be immersed in the adhesive resin composition and having light shielding properties, is provided. Further, a manufacturing method of an adhesive using wire pigments is provided.

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28-02-2019 дата публикации

Polyolefin production with chromium-based catalysts

Номер: US20190062475A1
Принадлежит: Univation Technologies Llc

A system and method for feeding a chromium-based catalyst to a polymerization reactor; adding a reducing agent to the chromium-based catalyst, and polymerizing an olefin into a polyolefin in the polymerization reactor in the presence of the chromium-based catalyst.

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17-03-2022 дата публикации

Curable compositions comprising unsaturated polyolefins

Номер: US20220081500A1
Принадлежит: Dow Global Technologies LLC

The present disclosure relates to unsaturated polyolefins and processes for preparing the same. The present disclosure further relates to curable formulations comprising the unsaturated polyolefins that show improved crosslinking.

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10-03-2016 дата публикации

Dual Catalyst Systems for Producing Polymers with a Broad Molecular Weight Distribution and a Uniform Short Chain Branch Distribution

Номер: US20160068625A1
Принадлежит:

Disclosed herein are ethylene-based polymers having a melt index less than 50 g/10 min, a ratio of Mw/Mn from 4 to 20, a density from 0.90 to 0.945 g/cm, and a substantially constant short chain branch distribution. These polymers can be produced using a dual catalyst system containing a boron bridged metallocene compound with a cyclopentadienyl group and an indenyl group, and a single atom bridged metallocene compound with a fluorenyl group. 110-. (canceled)11. A polymerization process , the process comprising:contacting a catalyst composition with an olefin monomer and an optional olefin comonomer in a polymerization reactor system under polymerization conditions to produce an olefin polymer, wherein the catalyst composition comprises catalyst component I, catalyst component II, an activator, and an optional co-catalyst, wherein:catalyst component I comprises a boron bridged metallocene compound with a cyclopentadienyl group and an indenyl group; andcatalyst component II comprises a single atom bridged metallocene compound with a fluorenyl group.12. The process of claim 11 , wherein:the catalyst composition comprises an organoaluminum co-catalyst; andthe activator comprises a fluorided solid oxide, a sulfated solid oxide, or both.13. The process of claim 11 , wherein the activator comprises an aluminoxane compound claim 11 , an organoboron or organoborate compound claim 11 , an ionizing ionic compound claim 11 , or any combination thereof.14. The process of claim 11 , wherein:the polymerization reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof andthe olefin monomer comprises ethylene, and the olefin comonomer comprises 1-butene, 1-hexene, 1-octene, or a mixture thereof.1520-. (canceled)21. The process of claim 11 , wherein the catalyst composition comprises a co-catalyst claim 11 , and wherein the activator comprises an activator-support claim 11 , the activator-support comprising a solid oxide treated ...

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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

TOUGHENED POLYOLEFIN AND BIOCARBON BASED LIGHT-WEIGHT BIOCOMPOSITES AND METHOD OF MAKING THE SAME

Номер: US20180066087A1
Принадлежит:

Toughened polyolefins and methods used to produce toughened polyolefins in presence of a bio-filler. These materials can substitute traditional thermoplastic polyolefins known as TPOs or mineral filled TPOs. Exemplary compositions include a phase based on α-olefin elastomers and the use of biobased fillers. The bio-based filler used, can be a material rich in elemental carbon content. The use of additives is of regular usage for these compositions as they may be related to coupling agents, UV absorbers, light stabilizers, antioxidants, and so forth. These composition offer a remarkable lower density compared to traditional TPOs compositions altogether with bio-based value-performance addition. 1. A thermoplastic polyolefin composition comprising a polypropylene (PP) , an α-olefin copolymer , and biocarbon.2. The thermoplastic polyolefin composition of claim 1 , wherein the thermoplastic polyolefin composition further comprises one or more compatibilizing agents.3. The thermoplastic polyolefin composition of further comprising by weight percent:(a) 40-70% of the polypropylene,(b) 1-40% of the α-olefin copolymer,(c) 10-40% of the biocarbon, and(d) up to 10% of the one or more compatibilizing agents.4. The thermoplastic polyolefin composition of claim 2 , wherein the thermoplastic polyolefin comprises by weigh percent:(a) about 38-68% wt. of the polypropylene,(b) about 1-40% wt. of the α-olefin copolymer,(c), up to about 20% wt. of the biocarbon, and(d) up to about 10% wt. of the one or more compatibilizing agents.5. The thermoplastic polyolefin composition of claim 1 , wherein the polyolefin composition further comprises a β nucleating agent.6. The thermoplastic polyolefin composition of claim 1 , wherein up to 2% by weight of PP is replaced by a β nucleating agent.7. The thermoplastic polyolefin composition of claim 1 , wherein the thermoplastic polyolefin composition further comprises one or more of carbon fibers claim 1 , glass fibers claim 1 , peroxide claim 1 , a ...

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09-03-2017 дата публикации

Methods for Controlling Die Swell in Dual Catalyst Olefin Polymerization Systems

Номер: US20170066857A1
Принадлежит:

Methods for controlling the die swell of an olefin polymer produced using a dual catalyst system are disclosed. The die swell of the olefin polymer can be increased or decreased as a function of the catalyst weight ratio and the reactant molar ratio used during the olefin polymerization process. 1. A polymerization process , the process comprising:(1) contacting a dual catalyst system with an olefin monomer and an olefin comonomer in a polymerization reactor system under polymerization conditions to produce an olefin polymer,{'sub': 3', '10, 'wherein the olefin monomer comprises ethylene and the olefin comonomer comprises a C-Calpha-olefin,'}wherein the olefin polymer comprises a higher molecular weight component and a lower molecular weight component,wherein the dual catalyst system comprises a first metallocene catalyst component that produces the lower molecular weight component and a second metallocene catalyst component that produces the higher molecular weight component, and a catalyst weight ratio of the first:second catalyst component, and', 'a reactant molar ratio of the comonomer:monomer; and, 'wherein the polymerization conditions comprise(2) controlling a die swell of the olefin polymer by adjusting the catalyst weight ratio, by adjusting the reactant molar ratio, or by adjusting both the catalyst weight ratio and the reactant molar ratio,wherein the die swell decreases as the catalyst weight ratio increases, andwherein the die swell decreases as the reactant molar ratio increases.23-. (canceled)4. The process of claim 1 , wherein the polymerization reactor system comprises a slurry reactor claim 1 , a gas-phase reactor claim 1 , a solution reactor claim 1 , or a combination thereof.5. The process of claim 1 , wherein the polymerization reactor system comprises a single reactor.6. The process of claim 1 , wherein the olefin comonomer comprises 1-hexene.7. The process of claim 1 , further comprising the steps of:determining the die swell; andadjusting the ...

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15-03-2018 дата публикации

Catalyst Composition Comprising Fluorided Support and Processes for Use Thereof

Номер: US20180072823A1
Принадлежит:

This invention relates to a catalyst system including fluorided silica, alkylalumoxane activator and a bridged monocyclopentadienyl group 4 transition metal compound, where the fluorided support has not been calcined at a temperature of 400° C. or more, and is preferably, produced using a wet mix method, particularly an aqueous method. 1. A catalyst system comprising the reaction product of fluorided silica support , alkylalumoxane activator and a bridged monocyclopentadienyl group 4 transition metal compound where the fluorided silica support has not been calcined at a temperature of 400° C. or more.3. The catalyst system of claim 2 , wherein M is Ti.4. The catalyst system of claim 2 , wherein each Cp is a cyclopentadiene claim 2 , indene or fluorene claim 2 , which may be substituted or unsubstituted claim 2 , M is titanium claim 2 , and each X is claim 2 , independently claim 2 , a halide claim 2 , a hydride claim 2 , an alkyl group claim 2 , an alkenyl group or an arylalkyl group.5. The catalyst system of claim 1 , wherein the activator further comprises a non-coordinating anion activator.6. The catalyst system of claim 1 , where the activator comprises methylalumoxane.7. The catalyst system of claim 1 , where G is a heteroatom group represented by the formula: NR* claim 1 , where R* is methyl claim 1 , ethyl claim 1 , propyl claim 1 , butyl claim 1 , pentyl claim 1 , hexyl claim 1 , heptyl claim 1 , octyl claim 1 , nonyl claim 1 , cyclooctyl claim 1 , cyclododecyl claim 1 , decyl claim 1 , undecyl claim 1 , dodecyl claim 1 , adamantyl or an isomer thereof.8. The catalyst system of claim 1 , where the bridged monocyclopentadienyl transition metal compound comprises one or more of:dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethyl,dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dichloride,dimethylsilyl (tetramethylcyclopentadienyl)(t-butylamido)titanium dimethyl,dimethylsilyl (tetramethylcyclopentadienyl)(t- ...

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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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19-03-2015 дата публикации

AMINE TREATED MALEIC ANHYDRIDE POLYMERS, COMPOSITIONS AND APPLICATIONS THEREOF

Номер: US20150079506A1
Принадлежит:

Disclosed herein are various amine treated maleic anhydride containing polymers and compositions thereof, which are useful for forming self-imageable films. In some embodiments, such polymers encompass norbornene-type repeating units and maleic anhydride-type repeating units where at least some of such maleic anhydride-type repeating units are either ring-opened or have been transformed into maleimide repeat units. The films formed from such copolymer compositions provide self imageable, low-k, thermally stable layers for use in microelectronic and optoelectronic devices. 5. The polymer of wherein:{'sub': '2', 'X=CH;'} [{'sub': 1', '2', '3', '4', '2', '2', '1', '2', '3', '6, 'claim-text': [{'br': None, 'sub': 2', 'a', '2', '2', 'b, '—(CH)—(OCH—CH)—OR\u2003\u2003(A)'}, 'wherein:', 'a is 1 or 2;', 'b is 2 or 3; and', 'R is methyl, ethyl, n-propyl or n-butyl;, 'R, R, Rand Rindependently represents hydrogen, hexyl, decyl, oxiranyl-CHOCH—, di(C-C)alkylmaleimide(C-C)alkyl or a group of formula (A), {'sub': 8', '9', '10', '11, 'R, R, Rand Rare the same or different and each independently of one another is selected from hydrogen, methyl, ethyl, n-propyl, n-butyl, iso-butyl, tert-butyl, n-pentyl, iso-pentyl, neo-pentyl, phenyl, trimethylsilyl and triethylsilyl; or'}, {'sub': 8', '10', '9', '11, 'Rand Rare the same or different and each independently of one another is selected from hydrogen, methyl or ethyl; and Rtaken together with Rand the carbon atoms to which they are attached form cyclohexyl, cycloheptyl or cyclooctyl ring;'}, {'sub': 12', '13, 'Rand Rare the same or different and each independently of one another is selected from hydrogen, methyl or ethyl; and'}, {'sub': 14', '4', '18, 'Ris (C-C)alkyl.'}], 'm=0;'}6. The polymer of wherein said polymer comprises one or more first type of repeating units.7. The polymer of wherein said polymer comprises one or more second type of repeating units.8. The polymer of wherein said polymer comprises 0 to 75 mole percent of first ...

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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

CATALYST MODIFICATION TO CONTROL POLYMER ARCHITECTURE

Номер: US20180079846A1
Принадлежит: NOVA CHEMICALS (INTERNATIONAL) S.A.

By controlling the ratio of catalyst components or the type of activator the homogeneity of a polymer produced using a single site catalyst may be improved. 2. The method according to claim 1 , wherein in the catalyst n is 2.3. The method according to claim 2 , where in one L is a phosphinimine ligand.4. (canceled)5. The process according to claim 3 , wherein the starting ratio of catalyst components aluminoxane:catalyst:ionic activator is 100:1:greater than 1.1 and is reduced to 50-100:1: 0.3-1.05.6. The process according to claim 5 , where in the ionic activator is chosen from triphenylcarbenium tetrakis(pentafluorophenyl)borate and tris(pentafluorophenyl)borane.7. The method according to claim 6 , wherein the aluminoxane is methyl aluminoxane which is optionally used in conjunction with a hindered phenol to provide a molar ratio of hindered phenol:Al up to 0.6:1.8. The method according to claim 7 , wherein the catalyst is cyclopentadienyl tri-tert-butylphosphinimine titanium dichloride.9. The method according to claims 8 , wherein the catalyst is alkylated within ten minutes prior to use. The present disclosure relates to a method to improve the homogeneity of a copolymer produced in a solution polymerization using a single site catalyst in the presence of aluminoxane and an ionic activator. In conducting a solution phase polymerization, there is a tradeoff between catalyst activity and circulation rate through the reactor. It is desirable to have a highly reactive catalyst or catalyst system. In some instances, the polymer produced may have a degree of in-homogeneity in that the polymer has up to 10 wt. % or more of a component having a molecular weight of greater than 10. In further embodiments, this component may have a molecular weight greater than 10. It may be desirable to reduce the amount of this component.There are a number of copolymers produced in the presence of a single site catalyst which are “bimodal”. Typically, these resins have a TREF having an ...

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26-03-2015 дата публикации

Immunological analysis method and reagent

Номер: US20150086975A1
Принадлежит: Denka Seiken Co Ltd

Disclosed are an immunoassay method which can measure an antigen with high sensitivity and accuracy; and a reagent therefor. In the immunoassay method, an antigen-antibody reaction and/or a measurement is(are) carried out in the presence of a polycarboxylic acid type surfactant. The immunoassay reagent for use in the method is characterized by comprising the polycarboxylic acid type surfactant. By employing such a simple means that the polycarboxylic acid type surfactant is allowed to be present in the reaction and/or measurement system, non-specific reactions can be suppressed effectively even in a highly sensitive immunoassay, and an antigen can be measured accurately and specificity can be improved in the immunoassay.

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25-03-2021 дата публикации

PROCESS FOR PREPARATION OF AMORPHOUS POLYOLEFINIC IONOMERS

Номер: US20210087310A1
Принадлежит:

The present invention relates to an amorphous polyolefinic ionomer and a process for the preparation of an amorphous polyolefinic ionomer. 2. The process according to claim 1 , wherein the at least one olefin monomer is selected from the group consisting of propylene claim 1 , 1-butene claim 1 , 3-methyl-1-butene claim 1 , 1-pentene claim 1 , 4-methyl-1-pentene claim 1 , 1-hexene claim 1 , vinyl cyclohexane claim 1 , and 1-octene.3. The process according to wherein the at least one functionalized olefin monomer is selected from the group consisting of allyl alcohol claim 1 , 3-buten-1-ol claim 1 , 3-buten-2-ol claim 1 , 3-buten-1 claim 1 ,2-diol claim 1 , 5-hexene-1-ol claim 1 , 5-hexene-1 claim 1 ,2-diol claim 1 , 7-octen-1-ol claim 1 , 7-octen-1 claim 1 ,2-diol claim 1 , 9-decen-1-ol claim 1 , 10-undecene-1-ol claim 1 , 5-norbornene-2-methanol claim 1 , 3-butenoic acid claim 1 , 4-pentenoic acid or 10-undecenoic acid.4. The process according to claim 1 , wherein the amount of the functionalized olefin monomers in step a1) is from 0.01 to 30 mol % claim 1 , with respect to the total molar amount of the olefin monomers and the functionalized olefin monomers.5. The process according to claim 1 , wherein the masking agent is selected from trialkyl aluminum complexes claim 1 , dialkyl magnesium complexes claim 1 , dialkyl zinc complexes or trialkyl boron complexes.6. The process according to claim 1 , wherein in step b1) or b2) the metal salt is a fluoride claim 1 , chloride claim 1 , bromide claim 1 , iodide claim 1 , hydroxide claim 1 , nitrite claim 1 , nitrate claim 1 , formate claim 1 , acetate claim 1 , bicarbonate claim 1 , carbonate claim 1 , sulfite claim 1 , sulfate claim 1 , chlorate claim 1 , perchlorate claim 1 , bromate or EDTA salt of a metal selected from one or more of lithium claim 1 , sodium claim 1 , potassium and silver and/or the monofunctional amine is selected from NH claim 1 , MeNH claim 1 , NMe claim 1 , EtNH claim 1 , EtN claim 1 , BuNH.7. ...

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29-03-2018 дата публикации

Supported Catalyst Systems and Processes for Use Thereof

Номер: US20180086859A1
Принадлежит:

This invention relates to a supported catalyst system and process for use thereof. In particular, the catalyst system includes a pyridyldiamido transition metal complex, an activator and a support material. The catalyst system may be used for preparing ultrahigh molecular weight polyolefins. 4. The supported catalyst system of claim 1 , wherein the metal represented by M comprises Ti claim 1 , Zr claim 1 , or Hf.5. The supported catalyst system of claim 1 , wherein the groups represented by R claim 1 , Rto R claim 1 , or Rto Rcontain 2 to 20 carbon atoms.6. The supported catalyst system of claim 1 , wherein the group represented by E is carbon claim 1 , and Rand Rare independently selected from phenyl groups that are variously substituted with between zero to five substituents that include F claim 1 , Cl claim 1 , Br claim 1 , I claim 1 , CF claim 1 , NO claim 1 , alkoxy claim 1 , dialkylamino claim 1 , hydrocarbyl claim 1 , and substituted hydrocarbyls claim 1 , groups with from one to ten carbons.7. The supported catalyst system of claim 1 , wherein the group represented by L is selected from halide claim 1 , alkyl claim 1 , aryl claim 1 , alkoxy claim 1 , amido claim 1 , hydrido claim 1 , phenoxy claim 1 , hydroxy claim 1 , silyl claim 1 , allyl claim 1 , alkenyl claim 1 , and alkynyl; and the group represented by L′ is selected from ethers claim 1 , thio-ethers claim 1 , amines claim 1 , nitriles claim 1 , imines claim 1 , pyridines claim 1 , and phosphines.8. The supported catalyst system of claim 1 , wherein the support material has a surface area in the range of from 10 to 700 m/g and an average particle diameter in the range of from 10 to 500 μm.9. The supported catalyst system of claim 1 , wherein the support material is selected from the group consisting of silica claim 1 , alumina claim 1 , silica-alumina claim 1 , and combinations thereof.10. The supported catalyst system of claim 1 , wherein the support material is fluorided.11. The supported catalyst ...

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30-03-2017 дата публикации

Heterogeneous Ziegler-Natta Catalysts with Fluorided Silica-Coated Alumina

Номер: US20170088646A1
Принадлежит: Chevron Phillips Chemical Co LP

Catalyst systems containing a Ziegler-Natta catalyst component are disclosed. Such catalyst systems can contain a co-catalyst and a supported catalyst containing a fluorided silica-coated alumina, a magnesium compound, and vanadium and/or tetravalent titanium.

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05-05-2022 дата публикации

HIGHLY BRANCHED, LOW MOLECULAR WEIGHT POLYOLEFINS AND METHODS FOR THEIR PRODUCTION

Номер: US20220135713A1
Принадлежит:

Low molecular weight, highly branched polyolefins are provided. Also provided are catalyst-mediated methods of making the low molecular weight, highly branched polyolefins and a catalyst system for carrying out the methods. The catalyst system is a homogeneous catalytic system that includes a single-site organozirconium complex and hydrocarbon-soluble perfluoroarylborate co-catalyst that is highly active for the oligomerization of olefin monomers in non-polar media.

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19-06-2014 дата публикации

POLYOLEFIN STRAP COMPRISING A RANDOM COPOLYMER OF PROPYLENE WITH 1-HEXENE

Номер: US20140171610A1
Принадлежит: BASELL POLIOLEFINE ITALIA S.R.L.

A strap comprising a propylene and 1-hexene copolymer containing from 0.3 wt % to less than 5 wt % of 1-hexene derived units said copolymer having a melt flow rate (MFR) determined according to ISO method 1133 (230° C., 2.16 kg ranging from 0.3 to less than 11 g/10 min. 1. A strap comprising a propylene and 1-hexene copolymer containing from 0.25 wt % to less than 5 wt % of 1-hexene derived units said copolymer having a melt flow rate (MFR) determined according to ISO method 1133 (230° C. , 2.16 kg ranging from 0.3 to less than 11 g/10 min.2. The strap according to wherein the propylene and 1-hexene copolymer contains from 0.5 wt % to less than 3 wt % of 1-hexene derived units.3. The strap according to wherein the propylene and 1-hexene copolymer containing from 0.8 wt % to 2.4 wt % of 1-hexene derived units.4. The strap according to wherein the propylene and 1-hexene copolymer has a melt flow rate (MFR2) determined according to ISO method 1133 (230° C. claim 1 , 2.16 kg ranging from 0.5 dl/10 min to 8 dl/10.5. The strap according to wherein the propylene and 1-hexene copolymer has a melting point higher than 145° C.6. The strap according to having a stretching ratio comprised between 1:8 to 1:15 claim 1 ,7. The strap according to having a stretching ratio comprised between 1:11 to 1:14. The present invention relates to strap comprising random copolymers of propylene with 1-hexene.Steel and plastic strapping are used for a wide variety of applications, often to secure very large coils of steel, synthetic fiber bales and heavy palletized boxes. Steel strapping has advantages in that it has high strength and temperature resistance and outstanding creep resistance. Steel strapping is typically used on heavy loads where high strap strengths and low creep properties are required. However, steel strapping, although very useful in maintaining the quality of the packaging, may be more difficult to dispose of and the strap can have sharp edges.Plastic strap has found ...

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01-04-2021 дата публикации

Olefin-Based Copolymer and Method for Preparing the Same

Номер: US20210095062A1
Принадлежит: LG CHEM, LTD.

An olefin-based copolymer and a method of making the same are disclosed herein. In some embodiments, an olefin-based copolymer has a density (d) of 0.85 to 0.89 g/cc, a melt index (MI), measured at 190° C. and 2.16 kg load, of 15 g/10 min to 100 g/10 min, a number of unsaturated functional groups (total V) per 1,000 carbon atoms of 0.8 or less, a vinylene content, and a vinyl content, wherein the vinylene content, the vinyl content and the total V satisfy (a) vinylene content/total V=0.1 to 0.7 and (b) vinylene content/vinyl content=0.8 to 1.6. The olefin-based copolymer has controlled content and kind of an unsaturated functional group in the olefin-based copolymer and thus, has high flowability, and may show improved physical properties of hardness, flexural strength and tensile strength. 1. An olefin-based copolymer having a density (d) of 0.85 to 0.89 g/cc ,a melt index (MI), measured at 190° C. and 2.16 kg load, of 15 g/10 min to 100 g/10 min,a number of unsaturated functional groups (total V) per 1,000 carbon atoms of 0.8 or less,a number of vinylene (vinylene content) per 1,000 carbon atoms, anda number of vinyl (vinyl content) per 1,000 carbon atoms,wherein the vinylene content, the vinyl content, and the total V satisfy the following (a) and (b):(a) vinylene content/total V=0.1 to 0.7(b) vinylene content/vinyl content=0.8 to 1.6.2. The olefin-based copolymer according to claim 1 , wherein the olefin-based copolymer has a weight average molecular weight (Mw) of 10 claim 1 ,000 g/mol to 80 claim 1 ,000 g/mol.3. The olefin-based copolymer according to claim 1 , wherein the olefin-based copolymer has a molecular weight distribution (MWD) of 1.5 to 3.0.4. The olefin-based copolymer according to claim 1 , wherein the total V is 0.15 to 0.7.5. The olefin-based copolymer according to claim 1 , wherein:(a) vinylene content/total V=0.2 to 0.6(b) vinylene content/vinyl content=0.8 to 1.5.6. The olefin-based copolymer according to claim 1 , wherein the olefin-based ...

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05-04-2018 дата публикации

Sterically Hindered Metallocenes, Synthesis and Use

Номер: US20180094088A1
Принадлежит:

In at least one embodiment, a catalyst compound is represented by Formula (I): 2. The catalyst compound of claim 1 , wherein Ris linear or branched C-Csubstituted or unsubstituted hydrocarbyl.3. The catalyst compound of claim 1 , wherein Ris linear or branched C-Csubstituted or unsubstituted hydrocarbyl.4. The catalyst compound of claim 1 , wherein each of Rand Ris independently linear or branched C1-Cunsubstituted hydrocarbyl.5. The catalyst compound of claim 1 , wherein each X is independently a halide or C-Csubstituted or unsubstituted hydrocarbyl.6. The catalyst compound of claim 1 , wherein Ris hydrogen or C-Csubstituted or unsubstituted hydrocarbyl claim 1 , and wherein each of R claim 1 , R claim 1 , R claim 1 , and Ris independently C-Csubstituted or unsubstituted hydrocarbyl.8. A catalyst system comprising:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, '(a) the catalyst compound of ;'}(b) optionally, a bridged or unbridged metallocene catalyst compound other than a catalyst compound represented by the Formula (I); and(c) an activator.9. The catalyst system of claim 8 , wherein the metallocene catalyst compound of (b) is an unbridged metallocene catalyst compound represented by the formula: CpCpM′X′ claim 8 , wherein each Cpand Cpis independently selected from the group consisting of cyclopentadienyl ligands claim 8 , one or both Cpand Cpmay contain heteroatoms claim 8 , and one or both Cpand Cpmay be substituted by one or more R″ groups claim 8 , wherein M′ is selected from the group consisting of Groups 3 through 12 atoms and lanthanide Group atoms claim 8 , wherein X′ is an anionic leaving group claim 8 , wherein n is 0 or an integer from 1 to 4 claim 8 , wherein R″ is selected from the group consisting of alkyl claim 8 , lower alkyl claim 8 , substituted alkyl claim 8 , heteroalkyl claim 8 , alkenyl claim 8 , lower alkenyl claim 8 , substituted alkenyl claim 8 , heteroalkenyl claim 8 , alkynyl claim 8 , lower alkynyl claim 8 , substituted alkynyl ...

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28-03-2019 дата публикации

Hydrocarbon Polymer Additives and Compositions Prepared Thereof

Номер: US20190092937A1
Принадлежит:

The present invention provides an elastomeric composition comprising: at least one first elastomer; at least one first hydrocarbon polymer additive; and at least one second hydrocarbon polymer additive; wherein each of the first hydrocarbon polymer additive and the second hydrocarbon polymer additive is selected from the group consisting of: Caliphatic resins, Caromatic resins, mixed C/Cresins, pure aromatic monomer resins, dicyclopentadiene (DCPD) resins, aromatic modified cycloaliphatic resins, coumarone indene resins, rosin resins, rosin esters, terpene resins, modified terpene resins, terpene phenolic resins, and hydrogenated resins thereof. The composition may further comprise a second elastomer which is immiscible with the first elastomer. 1. A composition comprising:a) a first elastomer;b) a first hydrocarbon polymer additive; andc) a second hydrocarbon polymer additive, wherein the second hydrocarbon polymer additive is different from the first hydrocarbon polymer additive;{'sub': 5', '9', '5', '9, 'wherein each of the first hydrocarbon polymer additive and the second hydrocarbon polymer additive is selected from the group consisting of: Caliphatic resins, Caromatic resins, mixed C/Cresins, aromatic pure monomer resins, dicyclopentadiene (DCPD) resins, aromatic modified cycloaliphatic resins, coumarone indene resins, rosin resins, terpene resins, modified terpene resins, terpene phenolic resins, hydrogenated resins thereof, and combinations thereof.'}2. The composition of claim 1 , wherein the first elastomer is selected from the group consisting of butyl rubber claim 1 , halogenated butyl rubber claim 1 , branched (“star-branched”) butyl rubber claim 1 , halogenated star-branched butyl rubber claim 1 , poly(isobutylene-co-p-methylstyrene) claim 1 , halogenated poly(isobutylene-co-p-methylstyrene) claim 1 , general purpose rubber claim 1 , natural rubber claim 1 , polybutadiene rubber claim 1 , polyisoprene rubber claim 1 , styrene-butadiene rubber claim 1 , ...

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26-06-2014 дата публикации

Mono- and multi-layer films and articles made therefrom

Номер: US20140178614A1
Принадлежит: Dow Global Technologies LLC

Mono- and multi-layer films comprising a polyethylene composition which comprises the reaction product of ethylene and optionally one or more alpha olefin comonomers in the presence of a catalyst composition comprising a multi-metallic procatalyst via a solution polymerization process in at least one reactor; wherein said polyethylene composition is characterized by one or more of the following properties: a melt index, I 2 , measured according to ASTM D 1238 (2.16 kg@190° C.), from 0.1 to 5 g/10 min; density, measured according to ASTM D-792, from 0.910 to 0.935 g/cc; melt flow ratio, I 10 /I 2 , wherein I 10 is measured according to ASTM D1238 (10 kg@190° C.), from 6 to 7.4; and molecular weight distribution, (M w /M n ) from 2.5 to 3.5 are provided. Also provided are articles made from the mono- and/or multi-layer films.

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26-06-2014 дата публикации

Systems and Methods for Real-Time Catalyst Particle Size Control in a Polymerization Reactor

Номер: US20140179881A1
Принадлежит: Chevron Phillips Chemical Co LP

Polymerization reactor systems providing real-time control of the average particle size of catalyst system components are disclosed. Methods for operating such polymerization reactor systems also are described.

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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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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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21-04-2016 дата публикации

Lubricant Compositions Including Alpha-Olefin Copolymers

Номер: US20160108335A1
Принадлежит: Elevance Renewable Sciences Inc

A lubricant composition may include a copolymer having constitutional units formed from monomers including an alpha-olefin and an α-ester-alk-ω-ene molecule, where the composition has a kinematic viscosity at 100° C. of at most 20 centistokes, or of at least 40 centistokes. A lubricant composition may include a copolymer having constitutional units formed from monomers including an alpha-olefin, an α-ester-alk-ω-ene molecule and an α-(carboxylic acid)-alk-ω-ene molecule, where the composition has a viscosity that varies as the molar ratio of the α-ester-alk-ω-ene molecule α-(carboxylic acid)-alk-ω-ene molecule in the monomers varies.

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23-04-2015 дата публикации

Processes to Control Fouling and Improve Compositions

Номер: US20150112005A1
Принадлежит:

Improved reaction processes comprise reacting a mixture to form a product comprising a metal alkyl, metal oxide, or mixture thereof and then passing said product to a post-reactor heat exchanger. The improvement comprises one or more of the following: 14-. (canceled)5. A reaction process comprising: (a) an ethylene/α-olefin multiblock interpolymer comprising at least 50 mole percent ethylene which is characterized before any crosslinking by one or more of the following characteristics:', '(1) an average block index greater than zero and up to about 1.0 and a molecular weight distribution, Mw/Mn, greater than about 1.3; or', '(2) at least one molecular fraction which elutes between 40° C. and 130° C. when fractionated using TREF, characterized in that the fraction has a block index of at least 0.5 and up to about 1; or', {'br': None, 'i': T', 'd', 'd, 'sub': 'm', 'sup': '2', '>−6553.3+13735()−7051.7(); or'}, '(3) an Mw/Mn from about 1.7 to about 3.5, at least one melting point, Tm, in degrees Celsius, and a density, d, in grams/cubic centimeter, wherein the numerical values of Tm and d correspond to the relationship, [{'br': None, 'i': T>−', 'H', 'H, 'Δ0.1299(Δ)+62.81 for Δgreater than zero and up to 130 J/g,'}, {'br': None, 'i': T≧', 'H, 'Δ48° C. for Δgreater than 130 J/g,'}], '(4) an Mw/Mn from about 1.7 to about 3.5, and a heat of fusion, ΔH in J/g, and a delta quantity, ΔT, in degrees Celsius defined as the temperature difference between the tallest DSC peak and the tallest CRYSTAF peak, wherein the numerical values of ΔT and ΔH have the following relationships, 'wherein the CRYSTAF peak is determined using at least 5 percent of the cumulative polymer, and if less than 5 percent of the polymer has an identifiable CRYSTAF peak, then the CRYSTAF temperature is 30° C.; or', {'br': None, 'i': Re>', 'd, '1481−1629(); or'}, '(5) an elastic recovery, Re, in percent at 300 percent strain and 1 cycle measured with a compression-molded film of the ethylene/α-olefin ...

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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

Maleinated Derivatives

Номер: US20180111912A1
Принадлежит: ELEVANCE RENEWABLE SCIENCES, INC.

This invention relates to malienated derivatives made from maleic anhydride, functionalized monomers, and one or more additional reagents, e.g., an oxygen-containing reagent (e.g., alcohol, polyol), a nitrogen-containing reagent (e.g., amine, polyamine, aminoalcohol), a metal and/or a metal compound. The invention relates to lubricants, functional fluids, fuels, dispersants, detergents and functional compositions (e.g., cleaning solutions, food compositions, etc.) 176-. (canceled)77. A maleinated derivative composition comprising: a functionalized polymer , wherein the functionalized polymer is reacted with maleic anhydride on one or more carbon-carbon double bonds of the functionalized polymer to form a maleinated functionalized polymer;wherein the functionalized polymer is formed via olefin metathesis from one or more functionalized monomers; andwherein the one or more functionalized monomers are unsaturated fatty acid glycerides.78. The maleinated derivative of claim 77 , wherein the unsaturated fatty acid glycerides comprise unsaturated fatty acid monoglycerides claim 77 , unsaturated fatty acid diglycerides claim 77 , unsaturated fatty acid triglycerides claim 77 , or combinations of two or more of the foregoing.79. The maleinated derivative of claim 77 , wherein the unsaturated fatty acid glycerides are derived from a natural oil.80. The maleinated derivative of claim 79 , wherein the natural oil is a vegetable oil claim 79 , an algae oil claim 79 , a fungus oil claim 79 , an animal fat claim 79 , a tall oil claim 79 , or any combination of two or more of the foregoing.81. The maleinated derivative of claim 80 , wherein the natural oil is a vegetable oil.82. The maleinated derivative of claim 80 , wherein the natural oil is canola oil claim 80 , rapeseed oil claim 80 , coconut oil claim 80 , corn oil claim 80 , cottonseed oil claim 80 , olive oil claim 80 , palm oil claim 80 , peanut oil claim 80 , safflower oil claim 80 , sesame oil claim 80 , soybean oil ...

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27-04-2017 дата публикации

Dual Catalyst Systems for Producing Polymers with a Broad Molecular Weight Distribution and a Uniform Short Chain Branch Distribution

Номер: US20170114169A1
Принадлежит: Chevron Phillips Chemical Co LP

Disclosed herein are ethylene-based polymers having a melt index less than 50 g/10 min, a ratio of Mw/Mn from 4 to 20, a density from 0.90 to 0.945 g/cm 3 , and a substantially constant short chain branch distribution. These polymers can be produced using a dual catalyst system containing a boron bridged metallocene compound with a cyclopentadienyl group and an indenyl group, and a single atom bridged metallocene compound with a fluorenyl group.

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13-05-2021 дата публикации

4-METHYL-1-PENTENE POLYMER, RESIN COMPOSITION AND MOLDED ARTICLE

Номер: US20210139622A1
Принадлежит: Mitsui Chemicals, Inc.

A 4-methyl-1-pentene polymer (X) wherein a content of a constitutional unit derived from 4-methyl-1-pentene is 90 to 100% by mol; a content of a constitutional unit derived from at least one olefin selected from ethylene and an α-olefin, other than 4-methyl-1-pentene, having 3 to 20 carbon atoms is 0 to 10% by mol; and the 4-methyl-1-pentene polymer satisfies certain requirements (a) to (f): (a) a meso diad fraction (m) measured by C-NMR falling within a certain range; (b) a ratio of weight-average molecular weight Mw within a certain range; (c) a melt flow rate (MFR) within a certain range; (d) a cumulative weight fraction within a certain range; (e) a proportion of a polymer having a molecular weight of a certain range; and (f) a heat of fusion and a melting point of the 4-methyl-1-pentene polymer within certain ranges. 2. A resin composition comprising a 4-methyl-1-pentene polymer (X) according to .3. A molded article comprising a 4-methyl-1-pentene polymer (X) according to or a resin composition according to .4. The molded article according to claim 3 , wherein the molded article is an injection molded article or an extrusion molded article.5. The molded article according to claim 3 , wherein the molded article is a film.6. The molded article according to claim 3 , wherein the molded article is a blow molded article. The present invention relates to a 4-methyl-1-pentene polymer having specific physical properties, and a resin composition and a molded article comprising the same.4-Methyl-1-pentene-α-olefin copolymers with 4-methyl-1-pentene as a main constitutional monomer are excellent in heat resistance, mold release properties, and chemical resistance and therefore widely used for various applications. For example, films made of the copolymers are used in FPC mold releasing films, films for composite material molding, mold releasing films, etc. by exploiting features such as favorable mold release properties, or used in experimental instruments and mandrels ...

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03-05-2018 дата публикации

ZIEGLER-NATTA CATALYST FOR HIGH TEMPERATURE POLYMERIZATION

Номер: US20180118863A1
Принадлежит: NOVA CHEMICALS (INTERNATIONAL) S.A.

The various embodiments of the invention provide, a magnesium titanium polymerization procatalyst, methods for making and using the same. 134-. (canceled)35. A procatalyst for polymerization of ethylene and α-olefins , the procatalyst comprising at least 0.2% of a species detectable by EPR having a g value of 1.950.36. The procatalyst of claim 35 , comprising from about 0.2 to about 1% of a species detectable by EPR having a g value of 1.950.37. (canceled)38. The procatalyst of claim 35 , wherein the species detectable by EPR having a g value of 1.950 can be associated with a tetrahedral Ti species.39. The procatalyst of claim 36 , wherein the species detectable by EPR having a g value of 1.950 can be associated with a tetrahedral Ti species.40. The procatalyst of claim 35 , wherein the procatalyst for polymerization of ethylene and a-olefins comprises a Ti complex of the formula TiCl*[[R][RO]AlX] a is 0 to 1;', 'b is 0 to 1;', 'c=a+b;', 'd is from about 0.33 to about 1.0;', {'sup': 4', '5, 'sub': '1-8', 'each Rand Ris independently selected from Calkyl radicals;'}, 'each X is independently chosen from the halogen radicals;, 'wherein'}the Mg/Ti molar ratio is from about 5 to about 10;{'sup': '3+', 'and further wherein at least 60% of the total Ti present is in the Ti oxidation state.'}41. The procatalyst of claim 40 , wherein X is Cl.42. The procatalyst of claim 40 , wherein a is 0 and b is 0.43. The procatalyst of claim 40 , wherein a is 0 and b is 1.44. The procatalyst of claim 40 , wherein a is 1 and b is 0.45. The procatalyst of claim 40 , wherein each Ris ethyl.46. The procatalyst of claim 40 , wherein the Mg/Ti ratio is from about 5 to about 8.47. The procatalyst of claim 40 , wherein the Ti complex is TiCl*[OEtAlCl] claim 40 , and the Mg/Ti molar ratio is from about 5 to about 8.48. The procatalyst of claim 40 , wherein the Ti complex is TiCl*[ClAlCl] claim 40 , and the Mg/Ti molar ratio is from about 5 to about 8. Magnesium-titanium catalysts for olefin ...

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25-08-2022 дата публикации

Method for Producing Metallocene-Supported Catalyst and Metallocene-Supported Catalyst

Номер: US20220267486A1
Принадлежит: LG CHEM, LTD.

The present invention relates to: a method for producing a metallocene-supported catalyst, the method including (1) a step of producing a reaction solution 1 by reacting one or more metallocene compounds with one or more co-catalyst compounds, (2) a step of performing supporting by mixing a support with the reaction solution 1, (3) a step of producing a reaction solution 2 by reacting one or more metallocene compounds with one or more co-catalyst compounds, and (4) a step of mixing the reaction solution 2 with the supporting material of the step (2); and a metallocene-supported catalyst produced by the same. 1. A method for producing a metallocene-supported catalyst , the method comprising:(1) a step of producing a reaction solution 1 by reacting one or more metallocene compounds with one or more first co-catalyst compounds;(2) a step of performing supporting by mixing a support with the reaction solution 1 to obtain a supporting material;(3) a step of producing a reaction solution 2 by reacting one or more metallocene compounds, which are the same as or different from the metallocene compounds used in the step (1), with one or more second co-catalyst compounds; and(4) a step of mixing the reaction solution 2 with the supporting material of the step (2).2. The method for producing a metallocene-supported catalyst of claim 1 , wherein a weight ratio of the metallocene compounds used in the step (1) to the metallocene compounds used in the step (3) is 6:1 to 1:6.3. The method for producing a metallocene-supported catalyst of claim 1 , wherein the metallocene compounds used in the step (1) and the metallocene compounds used in the step (3) each include at least one or selected from the group consisting of a first metallocene compound claim 1 , a second metallocene compound claim 1 , and a third metallocene compound.4. The method for producing a metallocene-supported catalyst of claim 1 , wherein a weight ratio of the first co-catalyst compounds used in the step (1) to ...

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25-04-2019 дата публикации

Unbridged Indacenyl Metallocenes

Номер: US20190119418A1
Принадлежит:

The present disclosure provides novel unbridged group 4 indacenyl-containing metallocene compounds. The catalyst system may be used for olefin polymerization processes. 2. The catalyst of claim 1 , wherein:M is a group 4 metal;{'sup': 1', '2', '3', '4', '5, 'sub': 1', '20, 'each of R, R, R, R, and Ris independently hydrogen, halogen, C-Csubstituted or unsubstituted hydrocarbyl, halocarbyl or silylcarbyl;'}{'sup': 5', '5′', '6', '6′', '7', '7′, 'sub': 1', '10, 'each of R, R, R, R, Rand R is independently hydrogen or a C-Calkyl;'}each X is independently a leaving group, or two Xs are joined and bound to the metal atom to form a metallocycle ring, or two Xs are joined to form a chelating ligand, a diene, or an alkylidene; and{'sup': 9', '10', '11', '12', '13', '9', '10', '12', '13, 'sub': 1', '20, 'each of R, R, R, Rand Ris hydrogen or C-Csubstituted or unsubstituted hydrocarbyl, or Rand Ror Rand Rtogether form a substituted or unsubstituted 5-8 membered saturated or unsaturated cyclic ring.'}3. The catalyst of claim 1 , wherein Rand Rtogether form an unsaturated cyclic ring.4. The catalyst of claim 1 , wherein the unsaturated cyclic ring is substituted with bromo or phenyl which may be substituted or unsubstituted.5. The catalyst of claim 1 , wherein Ris selected from aryl claim 1 , alkyl claim 1 , bromo claim 1 , chloro claim 1 , fluoro or —R—SiR′ claim 1 , where R is C-Calkyl and R′ is halogen claim 1 , C-Calkyl or C-Caryl.6. The catalyst of claim 1 , wherein Ris C-Cunsubstituted hydrocarbyl or —R—SiR′ claim 1 , where R is C-Calkyl and R′ is halogen claim 1 , C-Calkyl or C-Caryl.7. The catalyst of claim 6 , wherein Ris butyl.8. The catalyst of claim 1 , wherein Ris C-Cunsubstituted hydrocarbyl.9. The catalyst of claim 8 , wherein Ris methyl.10. The catalyst of claim 1 , wherein Ris hydrogen.13. A catalyst system comprising:{'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'the catalyst of ;'}a support material; andan activator.14. The catalyst system of claim 13 , ...

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12-05-2016 дата публикации

PROPYLENE BASED TERPOLYMER FOR CONTAINERS

Номер: US20160130378A1
Принадлежит: BASELL POLYOLEFINE ITALIA S.R.L.

A container comprising a propylene, ethylene, 1-hexene terpolymer wherein: 1. A container comprising a propylene , ethylene and 1-hexene terpolymer wherein:(i) the content of ethylene derived units ranges from 0.2 wt % to 1.0 wt %;(ii) the content of 1-hexene derived units ranges from 3.5 wt % to 5.5 wt %; {'br': None, 'i': C', 'C, '2<6*0.16\u2003\u2003(I);'}, '(iii) the content of ethylene derived units fulfills the following equation (I);'}wherein C2 is the content of ethylene derived units wt % and C6 is the content of 1-hexene derived units wt %; and(iv) the melt flow rate MFR measured according to ISO 1133,230° C., 2.16 kg ranges from 15 to 80 g/10 min.2. The container of claim 1 , wherein the content of 1-hexene derived units ranges from 3.8 wt % to 5.0 wt %.3. The container of claim 1 , wherein the content of ethylene derived units ranges from 0.3 wt % to 0.8 wt %.4. The container of claim 1 , wherein equation (I) is C2 Подробнее

10-05-2018 дата публикации

Crosslinked Polyolefins for Biomedical Applications and Method of Making Same

Номер: US20180127525A1
Принадлежит: INNOLENE LLC

A method for preparing a copolymer that involves polymerizing at least one branched alkene monomer and at least one olefin monomer having a pendant benzocyclobutene (BCB) group to form a copolymer comprising a random distribution of a plurality of constitutional units corresponding to the at least one branched alkene monomer and the at least one olefin monomer. The polymerizing includes a carbocationic polymerization reaction involving sequential addition of a plurality of mixtures without terminating the carbocationic polymerization reaction, wherein the plurality of mixtures includes a mixture that includes the at least one branched alkene monomer and does not include the at least one olefin monomer having a pendant BCB group and a mixture that includes both the at least one branched alkene monomer and the at least one olefin monomer having a pendant BCB group. The copolymer composition can undergo crosslinking at elevated temperatures (preferably above 180° C.). 1. A method of preparing a copolymer comprising:polymerizing at least one branched alkene monomer and at least one olefin monomer having a pendant benzocyclobutene (BCB) group to form a copolymer comprising a random distribution of a plurality of constitutional units that include constitutional units corresponding to the at least one branched alkene monomer and constitutional units corresponding to the at least one olefin monomer having a pendant BCB group;wherein the polymerizing includes a carbocationic polymerization reaction involving sequential addition of a plurality of mixtures without terminating the carbocationic polymerization reaction, wherein the plurality of mixtures includes a mixture that includes the at least one branched alkene monomer and does not include the at least one olefin monomer having a pendant BCB group and a mixture that includes both the at least one branched alkene monomer and the at least one olefin monomer having a pendant BCB group.2. A method according to claim 1 , ...

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