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Небесная энциклопедия

Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

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Мониторинг СМИ

Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

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Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
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Применить Всего найдено 3995. Отображено 200.
27-06-2010 дата публикации

СПОСОБ ПОЛИМЕРИЗАЦИИ ВИНИЛСОДЕРЖАЩИХ МОНОМЕРОВ

Номер: RU2393170C2

Изобретение относится к способам полимеризации винилсодержащих мономеров, например мономерных винилгалогенидов. Полимеризацию осуществляют в реакционной смеси, представляющей собой водную суспензию. При этом из реакционной смеси выделяют по меньшей мере один продукт полимеризации, а реакционную смесь очищают и используют снова. Устройство содержит реакционный сосуд, соединенный с помощью соединительного средства для текучей среды с устройством для выделения из реакционной смеси продукта полимеризации, устройство для выделения из реакционной смеси продукта полимеризации, соединенное с помощью последующего соединительного средства для текучей среды с устройством для очистки реакционной смеси. Устройство для очистки реакционной смеси соединено с помощью соединительного средства с реакционным сосудом. Способ позволяет уменьшить количество отходов и/или сточных вод и получать полимер экологически чистым путем без ухудшения характеристик продукта полимеризации. 2 н. и 14 з.п. ф-лы, 4 ил., 10 ...

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20-11-2002 дата публикации

ВИНИЛИДЕНФТОРИДНЫЕ ТЕРМОПЛАСТИЧЕСКИЕ СОПОЛИМЕРЫ И СПОСОБ ИХ ПОЛУЧЕНИЯ

Номер: RU2193043C2
Принадлежит: АУСИМОНТ С.П.А. (IT)

Изобретение относится к винилиденфторидным термопластичным сополимерам, имеющим повышенное сопротивление удару. Сополимеры содержат 0,1-10 мол.% фтордиоксола формулы где y = Rf, Rf - перфторалкил C1-C5, Y=Z, X1 и Х2 - одинаковые или отличные, означают - F или CF3, Z=-F,-Н,-Cl, и до 100 мол.% винилиденфторида (ВДФ). Сополимеры получают сополимеризацией ВДФ с фтордиоксолом формулы (I) в суспензии с водой или без воды или в водной эмульсии в присутствии радикального инициатора при от -40 до 130oС и давлении 0,5-150 бар, причем фтордиоксол вводят в начале сополимеризации. Изобретение позволяет повысить сопротивление удару и сохранить механические свойства при высоких температурах изделий на основе сополимеров ВДФ и фтордиоксола. 2 с. и 6 з.п. ф-лы, 1 табл.

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27-08-2011 дата публикации

СПОСОБ ПОЛИМЕРИЗАЦИИ ОЛЕФИНОВ

Номер: RU2010105696A
Принадлежит:

... 1. Способ полимеризации олефинов, включающий: ! a) полимеризацию, по меньшей мере, жидкого олефинового мономера в реакторе-полимеризаторе для образования полимеризационной суспензии, содержащей полиолефин и указанный жидкий мономер; ! b) непрерывный перенос полимеризационной суспензии из реактора-полимеризатора в испарительную камеру с помощью транспортной линии, содержащей трубу, в которой устанавливается турбулентное течение трехфазного потока, содержащего полимер, жидкие мономеры и газообразные мономеры; ! c) отделение испаренного мономера от полимера в указанной испарительной камере; отличающийся тем, что непрерывно вводят средство против обрастания в жидкой форме выше впускного отверстия указанной трубы на стадии b). ! 2. Способ по п.1, где указанный турбулентный поток в трубе на стадии b) является таким, что, по меньшей мере, одно из чисел Рейнольдса паровой фазы Re(vap) или жидкой фазы Re(liq) превышает 2000000. ! 3. Способ по п.2, где в трубе на стадии b), по меньшей мере, одно ...

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23-08-1990 дата публикации

Сополимеры N-винилпирролидона с N,N-диметил-N,N-диаллиламмонийхлоридом в качестве добавок для очистки соков и способ их получения

Номер: SU1587056A1
Принадлежит:

Изобретение относится к химии полимеров, может быть использовано в пищевой промышленности и позволяет создать эффективную полимерную добавку для очистки соков. Сополимер общей формулы [(CH 2-CH/N-CO-CH 2-CH 2-CH 2/) X-(CH 2-CH-CH/CH 2-N(CH 3) 2-CH 2/-CH 2) Y] Z, где X=5-95 мол.%, Y=5-95 мол.%, с характеристической вязкостью в 0,1 н.водном растворе NACL при 30°С, равной 0,1-3,5 дл/г, получают радикальной сополимеризацией 5-95 мол.% N-винилпирролидона с 5-95 мол.% N,N-диметил-N,N-диаллиламмонийхлорида в органических, водно-органических или водных средах, PH 6,0-7,9, при 35-90°С в течение 6-48 ч. 2 табл.

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17-01-1968 дата публикации

Improvements in and relating to process for the manufacture of graft copolymers

Номер: GB0001099991A
Автор:
Принадлежит:

In a process for the manufacture of graft-copolymers, a monomer containing a vinyl or vinylidene group is graft-polymerized on to a trunk polymer or copolymer comprising units of a monomer containing at least one halogen atom that is activated by an ester or a phenyl group, in the presence of a free radical polymerization catalyst and under the action of ultra-violet light or high energy ionizing radiation. The trunk polymer may be derived from an ester of a -bromoacrylic acid, a vinyl ester of a bromo- or dibrom-butyric acid or bromoacetic acid, p-bromostyrene or diethyl bromomaleate or bromofumarate, optionally together with vinyl, acrylic, methacrylic or maleic esters, vinyl aromatic compounds, acrylonitrile, vinyl chloride, vinylidene chloride or butadiene. The grafted monomer may comprise a styrene derivative, a vinyl aromatic compound, a vinyl ester or ether, or vinylidene chloride; and may comprise a monomer of similar structure to a comonomer of the trunk copolymer. Alternatively ...

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15-07-1967 дата публикации

Sophisticated method of preparation of polymers in pearls starting from ethylene unsaturated monomers.

Номер: OA0000000713A
Автор:
Принадлежит:

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29-12-1980 дата публикации

PROCEDURE FOR THE POLYMERIZATION OF VINYL HALIDE MONOMERS IN WAESSERIGER SUSPENSION

Номер: AT0000360233B
Автор:
Принадлежит:

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11-02-1980 дата публикации

PROCEDURE FOR THE PRODUCTION OF A COAT MASS

Номер: AT0000355150B
Автор:
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10-12-1986 дата публикации

Apparatus for introducing monomers into the reaction during emulsion polymerization

Номер: AT0000381946B
Принадлежит:

An apparatus for introducing monomers into the reaction during emulsion polymerization has a feed pipe for the monomer or the monomer mixture, and this pipe terminates above the curved surface of a conical distributor which has been secured above the liquid surface and centrally on the stirrer shaft within a stirred reactor. Compared with conventional apparatus, the apparatus proposed achieves faster incorporation of the monomer feed into the reaction. ...

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25-07-1986 дата публикации

DEVICE FOR REGISTERING MONOMERS INTO THE REACTION PROPERTY WITH THE EMULSION POLYMERIZATION

Номер: AT0000380887B
Принадлежит:

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25-08-1972 дата публикации

Procedure for the production of aqueous polymer dispersions

Номер: AT0000301176B
Принадлежит:

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15-08-2009 дата публикации

AQUEOUS POLYMER DISPERSIONS

Номер: AT0000437898T
Принадлежит:

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15-09-2009 дата публикации

ADHESIVE COMPOSITION

Номер: AT0000440113T
Принадлежит:

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15-01-2012 дата публикации

PROCEDURE FOR THE PRODUCTION OF FORM POWDER

Номер: AT0000538141T
Принадлежит:

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15-07-1979 дата публикации

PROCEDURE FOR THE PRODUCTION OF A COAT MASS

Номер: AT0000771275A
Автор:
Принадлежит:

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15-02-1977 дата публикации

PROCEDURE FOR THE PRODUCTION OF EMULSION POLYVINYL CHLORIDE

Номер: AT0000683475A
Автор:
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15-12-1985 дата публикации

DEVICE FOR REGISTERING MONOMERS INTO THE REACTION PROPERTY WITH THE EMULSION POLYMERIZATION

Номер: AT0000369584A
Принадлежит:

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15-03-1992 дата публикации

COPOLYMER AS WELL AS ITS USE

Номер: AT0000132689A
Принадлежит:

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15-06-1997 дата публикации

ROTARY AGITATING DEVICE

Номер: AT0000153874T
Принадлежит:

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10-08-1979 дата публикации

PROCEDURE FOR THE PRODUCTION OF NEW THERMAL PLASTIC TERPOLYMERISATE

Номер: AT0000351762B
Автор: SU-HSIANG LI GEORGE
Принадлежит:

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15-10-1996 дата публикации

PROCEDURE FOR THE PRODUCTION OF AQUEOUS DISPERSIONS OF COPOLYMERS

Номер: AT0000143381T
Принадлежит:

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15-04-1995 дата публикации

CASTINGCASH, LIQUID TENSIDKONZENTRAT.

Номер: AT0000121124T
Принадлежит:

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15-12-1988 дата публикации

DISPERSION OF ADDITION POLYMERS IN ORGANIC LIQUIDS.

Номер: AT0000038842T
Принадлежит:

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15-03-1990 дата публикации

PROCEDURE FOR THE SUSPENSION POLYMERIZATION OF VINYLHALOGENID.

Номер: AT0000050783T
Принадлежит:

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15-04-1994 дата публикации

PROCEDURE FOR THE INTERMITTENT SUSPENSION POLYMERIZATION OF VINYLIDENFLUORID IN WAESSRIGEM MEDIUM.

Номер: AT0000103616T
Принадлежит:

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15-04-1992 дата публикации

WITH RESINS EMULSION POLYMERS AND PROCEDURE FOR THEIR PRODUCTION STRENGTHENED.

Номер: AT0000074609T
Принадлежит:

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15-11-1987 дата публикации

POLYMERIZATION EMULSIFYING AGENTS.

Номер: AT0000030327T
Принадлежит:

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15-08-1986 дата публикации

VINYL CHLORIDE POLYMERIZATION PROCEDURE.

Номер: AT0000020750T
Принадлежит:

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15-05-1992 дата публикации

PROCEDURE FOR THE PRODUCTION OF AN IMPACT RESISTANT THERMOPLASTIC RESIN.

Номер: AT0000074932T
Принадлежит:

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15-10-1993 дата публикации

PROCEDURE FOR THE PRODUCTION OF WAESSRIGEN POLYMER DISPERSIONS.

Номер: AT0000095202T
Принадлежит:

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15-10-1993 дата публикации

AMPHOTERE HYDROPHILIC ONES OF POLYMERS, PROCEDURES FOR THEIR PRODUCTION AND THEIR USE AS ABSORBING MEANS.

Номер: AT0000095201T
Автор: MALLO PAUL, MALLO, PAUL
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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15-08-1985 дата публикации

PROCEDURE FOR THE PRODUCTION OF POLYMER DISPERSIONS.

Номер: AT0000014738T
Принадлежит:

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15-12-1984 дата публикации

PROCEDURE FOR THE PRODUCTION OF A COPOLYMER.

Номер: AT0000010501T
Принадлежит:

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15-04-1983 дата публикации

PRODUCTION OF CARBOXYLIERTER LATICEN AND IT CONTAINING COMPOSITIONS.

Номер: AT0000002960T
Принадлежит:

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15-08-1997 дата публикации

PROPFKOPOLYMERE

Номер: AT0000156138T
Принадлежит:

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10-10-1969 дата публикации

Procedure for the production of aqueous Polymerlatices

Номер: AT0000275144B
Автор:
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25-11-1969 дата публикации

Molecular sieve for the gel chromatography

Номер: AT0000276309B
Автор:
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10-01-1968 дата публикации

Procedure for the polymerization and/or Copolymerisation of vinyl chloride in aqueous emulsion

Номер: AT0000259224B
Автор:
Принадлежит:

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10-02-1975 дата публикации

Procedure for the production of dispersions

Номер: AT0000320279B
Принадлежит:

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15-09-2001 дата публикации

PROCEDURE FOR THE PRODUCTION OF VINYLAROMAT COPOLYMER REDISPERGIERBAREN IN WATER REDISPERSIONSPULVERN

Номер: AT0000204307T
Принадлежит:

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10-08-1965 дата публикации

Procedure for the production of porous plastics

Номер: AT0000241828B
Принадлежит:

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15-01-1999 дата публикации

HIGH SPEED ALKALI-SOURCECASH RHEOLOGIC ADDITIVES FOR AQUEOUS SYSTEMS

Номер: AT0000174606T
Принадлежит:

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10-08-1964 дата публикации

Procedure for the production of Perl polymers

Номер: AT0000235021B
Автор:
Принадлежит:

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15-08-2001 дата публикации

PROCEDURE FOR THE PRODUCTION OF PARTICLES AND PARTICLE WITH THE HELP OF OF THIS PROCEDURE MANUFACTURED ABILITY

Номер: AT0000203755T
Принадлежит:

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10-12-1969 дата публикации

Procedure for the production of aqueous polymer dispersions

Номер: AT0000276755B
Автор:
Принадлежит:

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25-02-1970 дата публикации

Procedure for the production of Vinylpolymeren

Номер: AT0000279164B
Принадлежит:

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27-05-1968 дата публикации

Procedure for the production of fine pored fixed polymers

Номер: AT0000261916B
Автор:
Принадлежит:

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12-04-1965 дата публикации

Procedure for the production of aqueous emulsions of ethylen copolymers

Номер: AT0000239522B
Автор:
Принадлежит:

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21-03-2013 дата публикации

INTERLOCK AND PROCESS

Номер: US20130072644A1
Принадлежит:

The present invention relates to production of polymer, and in particular provides an interlock for use in a process for production of a polymer in a reactor, which process comprises: a. polymerising a monomer and optionally a comonomer in the reactor to produce polymer, optionally in the presence of an inert hydrocarbon, and b. withdrawing produced polymer from the reactor, said interlock being based on the temperature in the reactor, and comprising: 1. measuring the temperature in the reactor or a temperature representative of the temperature in the reactor, and 2. comparing said measured temperature to a threshold temperature, said interlock being characterised in that withdrawal is allowed if the measured temperature is greater than the threshold temperature but is prevented if the measured temperature is lower than the threshold temperature. 114-. (canceled)15. An interlock for use in a process for production of a polymer in a reactor , which process comprises:a. polymerising a monomer and optionally a comonomer in the reactor to produce polymer, optionally in the presence of an inert hydrocarbon, andb. withdrawing produced polymer from the reactor, 1. measuring the temperature in the reactor or a temperature representative of the temperature in the reactor, and', '2. comparing said measured temperature to a threshold temperature,, 'said interlock being based on the temperature in the reactor, and comprisingsaid interlock being characterised in that withdrawal is allowed if the measured temperature is greater than the threshold temperature but is prevented if the measured temperature is lower than the threshold temperature.16. An interlock for use in a process for production of a polymer in a reactor , which process comprises:a. polymerising a monomer and optionally a comonomer in the reactor to produce polymer, optionally in the presence of an inert hydrocarbon, andb. withdrawing produced polymer from the reactor, 1. measuring the pressure in the reactor or a ...

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28-03-2013 дата публикации

INTERLOCK AND PROCESS

Номер: US20130079476A1
Принадлежит: Ineos Commercial Services UK Limited

The present invention relates to the degassing of polymer powder, and in particular to an interlock for use in a process for degassing of a polymer powder in a degassing vessel, which interlock comprises: 1. measuring the temperature of the polymer powder within or exiting the degassing vessel, 2. comparing said measurement value to a threshold value in order to ascertain whether it is lower than the threshold value or not, and 3. if the measured temperature is lower than the threshold value taking one or more actions to reduce the concentration of hydrocarbons in the polymer powder exiting the degassing vessel and/or to stop the polymer powder withdrawal from that degassing vessel. 112-. (canceled)13. An interlock for use in a process for degassing of a polymer powder in a degassing vessel , which interlock comprises:1. measuring the temperature of the polymer powder within or exiting the degassing vessel,2. comparing said measured value to a threshold value in order to ascertain whether it is lower than the threshold value or not, and3. if the measured temperature is lower than said threshold value taking one or more actions to reduce the concentration of hydrocarbons in the polymer powder exiting the degassing vessel and/or to stop the polymer powder withdrawal from the degassing vessel.14. An interlock according to wherein the powder temperature is measured within the degassing vessel and in the half of the degassing vessel closest to the polymer powder exit.15. An interlock according to wherein the degassing vessel is a purge vessel in which polymer is contacted with a purge gas to remove monomers and other entrained hydrocarbons claim 13 , and the powder temperature is measured by measurement of the temperature of the purge gas after contact with the polymer powder.16. An interlock according to wherein the threshold value is adjusted depending on the polymer to be degassed and is defined by a fixed temperature differential between an upstream process condition ...

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11-04-2013 дата публикации

Process for the Gas-Phase Polymerization of Olefins

Номер: US20130090436A1
Принадлежит: Basell Poliolefine Italia, S.r.l.

A process for the gas-phase copolymerization of: (a) propylene, (b) at least one C-Cα-olefin, and (c) optionally ethylene, 1. A process for the gas-phase copolymerization of:(a) propylene,{'sub': 4', '8, '(b) at least one C-Cα-olefin, and'}(c) optionally ethylene,the process being carried out in a reactor having two interconnected polymerization zones, wherein the growing polymer particles flow through the first of said polymerization zones (riser) under fast fluidization conditions, leave said riser and enter the second of said polymerization zones (downcomer) through which they flow downward in a densified form, leave said downcomer and are reintroduced into said riser, thus establishing a circulation of polymer between the riser and the downcomer,{'sub': 4', '8, 'the gas mixture present in the riser being at least partially prevented from entering the downcomer by introducing into the upper part of said downcomer a liquid barrier having a composition different from the gaseous mixture present in the riser and comprising at least one C-Cα-olefin in a total amount of from 0.1% to 35% by mol.'}2. The process according to claim 1 , wherein the partial evaporation of said liquid barrier generates in the upper part of the downcomer a flow of gas moving counter-currently to the flow of descendent polymer.3. The process according to claim 1 , wherein the C-Cα-olefin is 1-hexene and its amount ranges from 0.1% to 10% by mol.4. The process according to claim 3 , wherein the liquid barrier further comprises:from 70 to 90% by mol of propylene;from 5 to 15% by mol of propane; andfrom 0 to 5% by mol of ethylene;5. The process according to claim 4 , wherein the obtained polyolefin contains from 0.2 to 8.0% by weight of recurring units derived from 1-hexene.6. The process according to claim 1 , wherein the C-Cα-olefin is 1-butene and its amount ranges from 2% to 30% by mol.7. The process according to claim 6 , wherein the liquid barrier further comprises:from 50 to 90% by mol of ...

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18-04-2013 дата публикации

PROCESS FOR PRODUCING FUNCTIONALIZED POLYMERS

Номер: US20130096267A1
Принадлежит: BRIDGESTONE CORPORATION

A method for preparing a functionalized polymer, the method comprising the steps of (a) polymerizing monomer in the presence of a coordination catalyst to form a polymer, (b) inhibiting said step of polymerizing with a Lewis base, and (c) reacting the polymer with a functionalizing agent. 1. A continuous polymerization method for preparing a functionalized polymer , the method comprising the steps of:(a) continuously introducing monomer and a coordination catalyst to form a polymerization mixture;(b) allowing at least a portion of the monomer to polymerize into a reactive polymer within a first zone;(c) continuously removing the polymerization mixture from the first zone and transferring the mixture to a second zone;(d) continuously introducing a Lewis base to the polymerization mixture after removal from the first zone;(e) continuously introducing a functionalizing agent to the polymerization mixture after removal from the first zone.2. The method of claim 1 , polymerization mixture includes less than about 20% by weight solvent.3. The method of claim 1 , where said step of introducing a Lewis base includes introducing the Lewis base in a sufficient amount to substantially cease the polymerization of monomer.4. The method of claim 1 , after said step of continuously introducing a Lewis base claim 1 , further comprising continuously removing the polymerization mixture from the second zone and transferring the mixture to a third zone.5. The method of claim 1 , where the reactive polymer has an active terminus.6. The method of claim 5 , where the functionalizing agent reacts with the reactive polymer at its active terminus.7. The method of claim 1 , where the polymerization mixture includes less than about 5% by weight solvent.8. The method of claim 1 , where said steps of continuously introducing monomer and said step of allowing at least a portion of the monomer to polymerize take place within an elongated reactor.9. The method of claim 1 , where said step of ...

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25-04-2013 дата публикации

PROCESS FOR IMPROVING THE DEVOLATILIZATION OF POLYMER SLURRY PRODUCED IN A POLYMERIZATION REACTOR

Номер: US20130102741A1
Принадлежит: TOTAL PETROCHEMICALS RESEARCH FELUY

The present invention relates to a process for improving the devolatilization of polymer slurry produced in an olefin polymerization reactor. The process is characterized in that it involves an adjustment of the temperature of the interior surface of the flash line for periodically transferring polymer slurry from the polymerization reactor to a downstream processing unit. In particular, in accordance with the present process, the temperature of the interior surface of the flash line is adjusted to a temperature which is equal to or higher than the softening temperature of the polymer passing through said flash line whereby said temperature is higher in a first half of the length of the flash line than in the remaining length of the flash line. 113-. (canceled)15. The process of claim 14 , wherein the flash line comprises different flash line zones claim 14 , and wherein the temperature of the interior surface of the flash line varies in the different zones.16. The process of claim 14 , wherein the temperature of the interior surface of the flash line or a zone thereof is adjusted by adjusting temperature claim 14 , pressure and/or flow of the fluid heating the flash line or a zone thereof.17. The process of claim 14 , wherein the temperature of the interior surface of the flash line is up to 10% higher in the first half of the length of the flash line than in the remaining length of the flash line.18. The process of further comprising periodically withdrawing the polymer slurry from the polymerization reactor through one or more settling legs; and passing the withdrawn polymer slurry from the settling legs through one or more heated flash lines into a flash tank.19. The process of claim 19 , wherein the one or more settling legs comprise at least two settling legs.20. The process of claim 14 , wherein the flash tank is operated at a pressure of between 0.1 and 4 bar. The present invention relates to the field of olefin polymerization. In particular, the present ...

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25-04-2013 дата публикации

PUMPING APPARATUS AND PROCESS FOR POLYMERIZATION IN LOOP REACTORS

Номер: US20130102742A1
Принадлежит:

An olefin polymerization process and apparatus wherein a fluid slurry comprising monomer, diluent and catalyst is circulated in a continuous loop reactor by two or more pumps. The process and apparatus allow operating the reaction at significantly higher solids content in the circulating fluid slurry. In a preferred embodiment, the fluid slurry is circulated by two impellers arranged so that the downstream impeller benefits from the rotational energy imparted by the upstream impeller. An olefin polymerization process operating at higher reactor solids by virtue of more aggressive circulation has improved efficiencies, particularly in larger-volume reactors. 1. A loop slurry polymerization process comprising:introducing monomer, and catalyst to a loop reactor;polymerizing the monomer to form a slurry comprising solid polyolefin particles in a liquid medium;circulating the slurry using two impellers;imparting a first rotational motion to the slurry with a first of the impellers;imparting a second rotational motion to the slurry with a second of the impellers, wherein the second rotational motion is opposite to the first rotational motion.2. The loop slurry polymerization process of further comprising pre-swirling the slurry upstream of the first impeller claim 1 , in a direction opposite to the first rotational motion of the impeller of the first impeller.3. The loop slurry polymerization process of further comprising post-swirling the slurry downstream of the second pump claim 1 , in the same direction as the second rotational motion of the impeller of the second pump.4. A loop slurry polymerization process according to claim 1 , further comprising minimizing a clearance between at least one impeller and a portion of the loop reactor housing the impeller.5. A loop slurry polymerization process according to claim 1 , wherein the slurry has a concentration of the solid polyolefin particles of at least about 45 weight percent and at most about 75 weight percent.6. A ...

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09-05-2013 дата публикации

Method and Apparatus for Monitoring and Restoring Electrical Properties of Polymerization Reactor Wall Film

Номер: US20130116391A1
Принадлежит: UNIVATION TECHNOLOGIES, LLC

Described herein are methods for monitoring and restoring electrical properties of polymerization reactor wall films. The method may comprise using a reactor wall monitor to monitor and determine an electrical property, such as the bed voltage or breakdown voltage, of the wall film The method may further comprise adding continuity additive to the reactor and/or adjusting the feed rate of continuity additive being added to the reactor in response to the measured electrical property. 1. A method for polymerizing olefins comprising: (i) during a first interval of time during the reaction in the reactor system, operating the static probe to generate high speed data indicative of bubbling in the fluid bed; and', '(ii) determining from the high speed data at least one electrical property of the coating;, '(a) during a polymerization reaction using at least one static probe in a fluid bed reactor system to monitor a coating comprising a film of polymer on a surface of the reactor system and a distal portion of each said static probe, wherein the coating is exposed to flowing fluid within the system, said monitoring including steps of(b) comparing the electrical property determined in step (a) with a reference breakdown voltage of the coating; and(c) if the electrical property is less than the reference breakdown voltage of the coating adding continuity additive to the polymerization reactor for a period of time until the determined electrical property of the coating is greater than or equal to the reference breakdown voltage of the coating.2. The method of claim 1 , wherein said surface of the reactor system is a bed wall and the coating is exposed to flowing fluid within the fluid bed during the reaction.3. The method of claim 1 , wherein the coating is a film of polymer.4. The method of claim 1 , wherein the high speed data include frequency components in a range from about 1 Hz to about 10 Hz claim 1 , and the first interval is at least one minute in duration.5. The ...

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16-05-2013 дата публикации

Process for preparing polyolefins

Номер: US20130123441A1
Принадлежит: TOTAL RESEARCH & TECHNOLOGY FELUY

The present invention relates to a process of preparing a polyolefin in a loop reactor by introducing anti-fouling agent through a sleeve provided around at least part of the shaft of the pump. Also, the invention relates to the use of anti-fouling agent to prevent or reduce fouling by feeding the anti-fouling agent against the impeller of the pump upon introduction to the loop reactor. 1. Process of preparing a polyolefin in a loop reactor in the presence of anti-fouling agent , said loop reactor comprising interconnected pipes , defining a reactor path , and an axial pump comprising a motor , a shaft and an impeller , characterized in that at least part of the anti-fouling agent is introduced into said loop reactor through a sleeve provided around at least part of the shaft of said pump.2. Process according to claim 1 , wherein at least part of the anti-fouling agent is fed against the side of the impeller which is connected to the shaft of said pump.3. Process according to claim 1 , wherein all anti-fouling agent is fed through the sleeve into the reactor.4. Process according to claim 1 , wherein the anti-fouling agent is dissolved at a concentration of 0.1-10% by weight in a solvent.5. Process according to claim 1 , wherein the anti-fouling agent is fed under flushing with diluent.6. Process according to claim 1 , wherein the diluent comprises less than 15% by weight of monomer claim 1 , preferably less than 10% by weight claim 1 , more preferably less than 5% by weight claim 1 , most preferably less than 1% by weight of monomer.7. Process according to claim 1 , wherein said polyolefin is produced in slurry conditions.8. Process according to claim 1 , wherein said process is performed in a double loop reactor.9. Process according to claim 1 , wherein the anti-fouling agent is introduced into the first loop reactor of the double loop reactor through a sleeve provided around at least part of the shaft of the pump of the first loop reactor.10. Process according to ...

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16-05-2013 дата публикации

Process for preparing polyolefins and use of antifouling agents therein

Номер: US20130123443A1
Принадлежит: TOTAL RESEARCH & TCCHNOLOGY FELUY

The present invention relates to a process of preparing a polyethylene in a loop reactor in the presence of antifouling agent comprising the steps of: 1. Process of preparing polyethylene in a loop reactor in the presence of antifouling agent comprising the steps of:a) feeding into said loop reactor diluent, monomers, optionally hydrogen, and optionally one or more co-monomers to produce a liquid phase;b) introducing antifouling agent into said loop reactor,c) introducing a catalyst into the liquid phase to produce a slurry; andd) polymerizing the monomers and optional co-monomers to form the polyethylene, characterized in that the time difference between introduction of the antifouling agent and introduction of the catalyst is at most 3 hours.2. Process according to claim 1 , wherein said polyethylene is produced in slurry conditions.33. Process according to or claim 1 , wherein antifouling agent is introduced in said loop reactor at most hours before introduction of the catalyst of step c) in the liquid phase.4. Process according to any of to claim 1 , wherein antifouling agent is introduced in said loop reactor at least 1 minute before introduction of the catalyst of step c) in the liquid phase.5. Process according to any of to claim 1 , wherein antifouling agent is introduced in said loop reactor at most 1 hour after introduction of the catalyst of step c) in said liquid phase.6. Process according to any of to claim 1 , wherein antifouling agent is introduced in said loop reactor at least 1 minute after introduction of the catalyst of step c) in said liquid phase.7. Process according to any of to claim 1 , wherein in step c) the catalyst is introduced into the liquid phase when the concentration of antifouling agent is ranging from 0 to less than 0.3 ppm.8. Process according to any of to claim 1 , wherein said polyolefin is polyethylene.9. Process according to any of to claim 1 , wherein the process further comprises the step of (e) subsequently increasing the ...

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23-05-2013 дата публикации

METHOD FOR PRODUCING POLYETHYLENE

Номер: US20130131288A1
Принадлежит: TOTAL RESEARCH & TECHNOLOGY FELUY

The present invention relates to a method for consecutively producing at least two different polyethylene resins in one slurry loop reactor, comprising producing a first polyethylene resin in the presence of a Ziegler-Natta and/or a Chromium catalyst, and consecutively producing a second polyethylene resin in the presence of a metallocene catalyst, characterized in that the ratio of the melt flow index of the first produced polyethylene resin to the melt flow index of the second produced polyethylene resin is at least 0.3. 1. Method for consecutively producing at least two different polyethylene resins in one slurry loop reactor , comprising the steps of producing a first polyethylene resin in the presence of a Ziegler-Natta and/or a Chromium catalyst , and consecutively producing a second polyethylene resin in the presence of a metallocene catalyst , characterized in that the ratio of the melt flow index of the first produced polyethylene resin to the melt flow index of the second produced polyethylene resin is at least 0.3.2. Method according to claim 1 , wherein said production is performed continuously.3. Method according to claim 1 , wherein the ratio of the melt flow index of the first produced polyethylene to the melt flow index of the second produced polyethylene is at least 1.4. Method according to claim 1 , wherein the ratio of the melt flow index of the first produced polyethylene to the melt flow index of the second produced polyethylene is at least 3.5. Method according to claim 1 , wherein the ratio between the melt flow index of said first resin and the melt flow index of said second resin is between 0.3 and 15.6. Method according to claim 1 , wherein the first polyethylene resin is produced in the presence of a Ziegler-Natta catalyst.7. Method of transition between polyethylene resins of different grades comprising the steps of producing in a loop reactor a first polyethylene resin in the presence of a Ziegler-Natta and/or a Chromium catalyst claim 1 ...

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27-06-2013 дата публикации

Method for Continuously Producing Thermoplastic Resin From Conjugated Diene and Thermoplastic Resin Produced by the Same

Номер: US20130165604A1
Принадлежит: CHEIL INDUSTRIES INC.

A method for continuously producing a thermoplastic resin from a conjugated diene includes: primarily polymerizing a conjugated diene monomer with an aromatic vinyl monomer in a first solvent in a first reactor, and feeding a hydroxyl group-containing polymerization inhibitor and a polar hydrocarbon to the first reactor to prepare a rubber solution; and adding an aromatic vinyl monomer and a monomer copolymerizable with the aromatic vinyl monomer to the rubber solution, and subjecting the mixture to secondary polymerization in a second solvent of the same kind as the first solvent in a second reactor. The method can provide a thermoplastic resin that can have excellent color and low gloss characteristics. 1. A method for continuously producing a thermoplastic resin from a conjugated diene , the method comprising:primarily polymerizing a conjugated diene monomer with an aromatic vinyl monomer in a first solvent in a first reactor, and feeding a hydroxyl group-containing polymerization inhibitor and a polar hydrocarbon to the first reactor to prepare a rubber solution; andadding an aromatic vinyl monomer and a monomer copolymerizable with the aromatic vinyl monomer to the rubber solution, and subjecting the mixture to secondary polymerization in a second solvent of the same kind as the first solvent in a second reactor.2. The method as claimed in claim 1 , wherein the conjugated diene monomer is butadiene claim 1 , isoprene or a combination thereof.3. The method as claimed in claim 1 , wherein the polymerization in the first reactor is carried out using an organometallic catalyst.4. The method as claimed in claim 1 , wherein a vinyl modifier is added for the polymerization in the first reactor.5. The method as claimed in claim 1 , wherein the rubber solution prepared by the polymerization in the first reactor is concentrated by extrusion before being fed into the second reactor.6. The method as claimed in claim 1 , wherein the first and second solvents are aromatic ...

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18-07-2013 дата публикации

Ethylene-Based Interpolymers and Processes to Make the Same

Номер: US20130184419A1
Принадлежит:

Ethylene-based interpolymers, e.g., ethylene-acrylic acid copolymers, are made by a process comprising the steps of: A. Injecting a first feed comprising a chain transfer agent system (CTA system) and ethylene into a first autoclave reactor zone to produce a first zone reaction product, the CTA system of the first reactor zone having a transfer activity Z1; and B. (1) Transferring at least part of the first zone reaction product to a second reactor zone selected from a second autoclave reactor zone or a tubular reactor zone, and (2) at least one of transferring or freshly injecting a feed comprising a CTA system into the second reactor zone to produce a second zone reaction product, the CTA system of the second reactor zone having a transfer activity of Z2; and with the proviso that the ratio of Z1:Z2 is greater than 1. The comonomer comprises at least one carboxylic acid group or an anhydride group. 2. The process of claim 1 , further comprising one or more steps of transferring a zone reaction product produced in an (ith−1) reaction zone to an (ith) reaction zone claim 1 , where 3≦i≦n claim 1 , and n≧3 claim 1 , each zone operating at polymerization conditions claim 1 , and injecting an (ith) feed comprising a CTA system into the (ith) reaction zone claim 1 , the CTA system of the (ith) reaction zone having a transfer activity of Zi; andwith the proviso that the ratio of Z1/Zi is greater than 1.3. The process of claim 1 , in which the second feed further comprises ethylene.4. The process of claim 1 , in which the at least one comonomer is selected from acrylic acid claim 1 , methacrylic acid claim 1 , or a combination thereof.5. The process of claim 1 , in which at least part of the first zone reaction product is transferred to a second autoclave reactor zone.6. The process of claim 1 , in which at least part of the first zone reaction product is transferred to a tubular reactor zone.7. The process of claim 1 , in which each feed to each reactor zone contains the ...

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01-08-2013 дата публикации

CONTINUOUS PROCESS FOR PREPARING POLYFLUOROACRYLATE PARTICLES

Номер: US20130197170A1
Автор: Tyson George
Принадлежит: Relypsa, Inc.

The present invention is directed to a continuous process for preparing a crosslinked polymer comprising a fluoro group. 4. The process of wherein the polymer comprises structural units corresponding to Formulae 1 claim 1 , 2 and 3.5. The process wherein either:(i) the structural units corresponding to Formula 1 constitute at least about 85 wt. % based on the total weight of structural units of Formulae 1, 2, and 3 in the polymer calculated from the amounts of monomers used in the polymerization reaction, and the weight ratio of the structural unit corresponding to Formula 2 to the structural unit corresponding to Formula 3 is from about 4:1 to about 1:4, or(ii) the mole fraction of the structural unit of Formula 1 in the polymer is at least about 0.87 based on the total number of moles of the structural units of Formulae 1, 2, and 3 calculated from the amounts of monomers used in the polymerization reaction, and the mole ratio of the structural unit of Formula 2 to the structural unit of Formula 3 is from about 0.2:1 to about 7:1.6. The process of wherein the polymer comprises structural units corresponding to Formulae 1 and 2.7. The process of wherein the polymer comprises structural units corresponding to Formulae 1 and 3.10. The process of wherein the polymerization mixture further comprises a polymerization initiator.11. The process of claim 1 , further comprising a continuous reactor claim 1 , with an aqueous phase and an organic phase fed to the reactor.12. The process of claim 11 , wherein the organic phase comprises a mixture of monomers that are mixed in a mixer prior to being fed to the reactor.13. The process of claim 11 , wherein the aqueous phase comprises a mixture of water claim 11 , surfactant and salts are mixed prior to being fed to the reactor.14. The process of claim 11 , wherein the reactor is a plug flow reactor.15. The process of claim 14 , wherein the plug flow reactor additionally comprises an orifice plate.16. The process of claim 15 , ...

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08-08-2013 дата публикации

Method For Controlling Bubble Formation In Polymerization Reactors

Номер: US20130203946A1
Принадлежит:

Disclosed herein are methods for controlling bubble formation in a polymerization reactor. The method includes: (a) determining a concentration of at least one component at a location in the reactor using a mathematical model; (b) determining a vapor pressure of the composition based at least in part upon the concentration of the component; (c) determining an operating pressure of the reactor at the location; (d) determining a pressure difference as ΔP =P-P, wherein Pis the operating pressure and Pis the vapor pressure; (e) comparing the ΔP to a threshold value; and (f) implementing an effect when the ΔP is less than the threshold value. 1. A method for controlling bubble formation in a polymerization reactor , the reactor containing a composition comprising at least one component , the method comprising:(a) determining a concentration of the at least one component in the composition at a location in the reactor using a mathematical model;(b) determining a vapor pressure of the composition based at least in part upon the concentration of the at least one component;(c) determining an operating pressure of the reactor at the location;{'sub': X', 'V', 'X', 'V, '(d) determining a pressure difference as ΔP=P−P, wherein Pis the operating pressure and Pis the vapor pressure;'}(e) comparing the ΔP to a threshold value, wherein the threshold value reflects a desired difference between the vapor pressure and operating pressure, and wherein a ΔP that is greater than the threshold value produces an acceptable amount of bubble formation; and(f) implementing an effect when the ΔP is less than the threshold value.2. The method of claim 1 , wherein one or more of (a) through (f) are conducted on a real-time basis.3. The method of claim 1 , wherein the method is conducted during change of a reactant supplied to the reactor during a grade transition.4. The method of claim 1 , wherein steps (a) through (f) are conducted at more than one location within the reactor.5. The method of ...

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22-08-2013 дата публикации

CONTINUOUS FLOW POLYMERISATION PROCESS

Номер: US20130217841A1

The present invention relates to a process for continuously preparing polymer by RAFT solution polymerisation, the process comprising: introducing into a flow reactor a reaction solution comprising one or more ethylenically unsaturated monomers, RAFT agent, non-reactive solvent and free radical initiator; and promoting RAFT polymerisation of the one or more ethylenically unsaturated monomers within the reactor so as to form a polymer solution that flows out of the reactor. 1. A process for continuously preparing polymer by RAFT solution polymerisation , the process comprising:introducing into a flow reactor a reaction solution comprising one or more ethylenically unsaturated monomers, RAFT agent, non-reactive solvent and free radical initiator; andpromoting RAFT polymerisation of the one or more ethylenically unsaturated monomers within the reactor so as to form a polymer solution that flows out of the reactor.2. The process according to claim 1 , wherein the flow reactor is in the form of a tubular flow reactor.3. The process according to claim 2 , wherein the flow reactor is in the form of a capillary tubular flow reactor.4. The process according to claim 1 , wherein the flow reactor comprises one or more flow lines through which the reaction solution passes claim 1 , the one or more flow lines having an internal diameter of about 1 mm.5. The process according to claim 1 , wherein the flow reactor comprises multiple flow lines through which the reaction solution passes claim 1 , each flow line having an internal diameter of about 1 mm.6. The process according to claim 1 , wherein the flow reactor comprises one or more flow lines through which the reaction solution passes claim 1 , the one or more flow lines being made of metal.7. The process according to which further comprises introducing the resulting polymer solution into a flow reactor or a region of a flow rector claim 1 , together with a reaction solution comprising one or more ethylenically unsaturated ...

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26-09-2013 дата публикации

CONTINUOUS PROCESS FOR THE SYNTHESIS OF GRAFT POLYMERS BASED ON POLYETHERS

Номер: US20130253089A1
Принадлежит: BASF SE

The invention relates to a continuous process for the preparation of amphiphilic graft polymers, wherein a vinyl ester component (B) composed of vinyl acetate and/or vinyl propionate (B1) and, if desired, a further ethylenically unsaturated monomer (B2), is polymerized in the presence of a polyalkylene oxide (A), a free radical-forming initiator (C) and, if desired, an additive (D), at a mean polymerization temperature at which the initiator (C) has a decomposition half-time of from 1 to 500 min, in at least one tubular reactor segment with a feed side and an outlet side, through which the reaction mixture comprising at least a part of component (A) to (C), and if desired (D), streams, a tubular reactor segment and the use of the inventive amphiphilic graft polymer. The invention further relates to an inventive amphiphilic graft polymer and the use thereof. 123.-. (canceled)24. A continuous process for the preparation of amphiphilic graft polymers , wherein a vinyl ester component (B) composed of vinyl acetate and/or vinyl propionate (B 1) and , optionally , a further ethylenically unsaturated monomer (B2) , is polymerized in the presence of a polyalkylene oxide (A) , a free radical-forming initiator (C) and , optionally , an additive (D) , at a mean polymerization temperature at which the initiator (C) has a decomposition half-time of from 1 to 500 min , in at least one tubular reactor segment with a feed side and an outlet side , through which the reaction mixture comprising at least a part of component (A) to (C) , and optionally (D) , streams.25. The continuous process according to claim 24 , wherein the polymerization takes place in at least two tubular reactor segments connected in series.26. The continuous process according to claim 25 , wherein at least two tubular segments are connected in series claim 25 , wherein the first tubular reactor segment has a first feed side and a first outlet side claim 25 , wherein the first tubular reactor segment is ...

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07-11-2013 дата публикации

Copolymer Production System and Process

Номер: US20130296506A1
Принадлежит: ExxonMobil Chemical Patents Inc.

In a process for making a copolymer, a first product stream comprising a semi-crystalline polymer and a chain terminating agent is produced in a first reactor system. The first product is provided to a second reactor system wherein a low crystallinity polymer is produced in the presence of the semi-crystalline polymer. At least a portion of the chain terminating agent is removed from the second reactor system by an in-situ process. 1. A process for making a copolymer , the process comprising:a. producing in a first reactor system a first product stream comprising a semi-crystalline polymer and a chain terminating agent;b. providing at least a portion of the first product stream to a second reactor system;c. producing in the second reactor system a low crystallinity polymer in the presence of the semi-crystalline polymer; andd. removing at least a portion of the chain terminating agent introduced with the first product stream from the second reactor system by an in-situ process.2. The process of claim 1 , wherein the in-situ process comprises a catalytic hydrogenation reactor to consume hydrogen via reaction with monomer claim 1 , or a membrane unit to selectively remove the chain terminating agent from the reaction system.3. The process of claim 1 , wherein the copolymer has an intrinsic viscosity ratio (IVR) of greater than 4.4. The process of claim 1 , wherein the chain terminating agent is hydrogen.5. The process of claim 1 , wherein the monomer is selected from ethylene and propylene.6. The process of claim 1 , wherein the semi-crystalline polymer has a matrix claim 1 , and at least a portion of the low crystallinity polymer is formed within the pores of the matrix.7. The process of claim 1 , wherein the semi-crystalline polymer is polypropylene homopolymer and the low crystallinity polymer is ethylene propylene rubber (EPR).8. The process of claim 1 , wherein the first reactor system comprises a slurry loop reactor or a plurality of slurry loop reactors in ...

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07-11-2013 дата публикации

PROCESS FOR OPERATING A MIXING KNEADER

Номер: US20130296509A1
Принадлежит:

The invention relates to a process for operating a mixing kneader, comprising one or more shafts on whose surfaces are disposed kneading bars and which are surrounded by a casing, comprising the following steps:

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26-12-2013 дата публикации

Double Loop Technology

Номер: US20130345374A1
Принадлежит: TOTAL PETROCHEMICALS RESEARCH FELUY

A method for the copolymerization of ethylene and a C olefin in a loop reactor and polymers formed therefrom are described herein. The method generally includes introducing an ethylene monomer, a C olefin and a diluent carrier liquid into a loop reactor. A catalyst system can be supplied to said loop reactor. The diluent liquid, ethylene monomer, and C olefin can be circulated through said loop reactor, while copolymerizing said ethylene and C olefin in the presence of said catalyst system to produce a slurry. The slurry can be diverted into a settling leg, and sequentially discharged therefrom and withdrawn from said loop reactor. An ethylene monomer co-feed can be introduced into said loop reactor at spaced locations downstream of the ethylene and diluent. The ethylene co-feed can be introduced in an amount effective to reduce the variation in the ratio of ethylene and C olefin. 111-. (canceled)12. A method for controlling the injection of catalyst slurry in a polymerization reactor , wherein polyethylene is prepared , said catalyst slurry comprising solid catalyst in a hydrocarbon diluent , the method comprising:providing solid catalyst and a hydrocarbon diluent in one or more storage vessels such that a catalyst slurry is obtained in said one or more storage vessels,transferring said catalyst slurry from said one or more storage vessels to a mixing vessel wherein said catalyst slurry is diluted for obtaining a suitable concentration for use in a polymerization reaction,pumping said diluted catalyst slurry at a controlled flow rate from said mixing vessel to said polymerization reactor through one or more conduits, by means of a pumping means, provided in each of said conduits, and the dilution being adapted to the pumping means.13. The method according to wherein said catalyst is a metallocene catalyst.14. The method of wherein the metallocene catalyst is a supported metallocene catalyst.15. The method according to wherein said catalyst slurry is diluted with ...

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23-01-2014 дата публикации

ENERGY EFFICIENT POLYOLEFIN PROCESS

Номер: US20140024788A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

A manufacturing system for producing polyolefin includes a polymerization reactor, a flash chamber, and a purge column. In certain embodiments, the purge column may receive a solids stream directly from the flash chamber. Further, the purge column may function as a feed tank for an extruder within an extrusion/loadout system. According to certain embodiments, the manufacturing system may be configured to consume less than 445 kilowatt-hours of energy per metric ton of polyolefin produced based on consumption of electricity, steam, and fuel gas. 1. A system , comprising:a first polymerization reactor configured to produce a slurry comprising first polyolefin particles and a diluent;a separation vessel configured to receive the slurry to produce a lights stream comprising light components and a solids stream comprising the first polyolefin particles and residual diluent; anda second polymerization reactor configured to receive the solids stream and produce second polyolefin particles.2. The system of claim 1 , wherein the separation vessel comprises a flash chamber.3. The system of claim 1 , wherein the first and second polyolefin particles are mixed in the second polymerization reactor to produce a product polyolefin particle stream.4. The system of claim 3 , comprising a flash chamber configured to receive the product polyolefin particle stream and separate a portion of the diluent to produce a flash stream comprising separated diluent and an additional solids stream comprising the product polyolefin particle stream.5. The system of claim 4 , comprising a solids discharge conduit configured to convey the additional solids stream from the flash chamber claim 4 , wherein the solids discharge conduit does not comprise a low-pressure flash vessel or a low-pressure flash compressor or blower.6. The system of claim 1 , wherein the second polymerization reactor comprises a gas phase polymerization reactor.7. The system of claim 1 , wherein the second polymerization reactor ...

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27-03-2014 дата публикации

POLYMERIZATION REACTOR FOR BUTYL RUBBER PRODUCTION

Номер: US20140086801A1
Принадлежит: CONSER SPA

A low temperature polymerization reactor for the production of butyl rubber by catalytic polymerization of isobutylene with small amount of a conjugated diolefin such as isoprene includes: an extended upper head with fluid deflector fixed to the top tube-sheet, the shapes of the head and deflector being optimized in order to reach a very homogeneous slurry velocity in the rows of tubes and to minimize the pressure drop due to the inversion of flow from up-flow to down-flow and to the entrance of the slurry in the tubes; an hemispheric bottom head with fluid deflectors placed between the impeller and the bottom itself and designed to minimize the pressure drop due to the inversion of flow from down-flow to up-flow; and straightening baffles inside the draft tube, which shape and dimensions are optimized to turn the radial velocity components produced by the rotation of the impeller into axial velocity components. 110-. (canceled)11151119426) A single pass shell and tubes type polymerization reactor () , used to produce butyl rubber in slurry , copolymerizing at least 95 wt % of isobutylene with not more than about 5 wt % of isoprene , in concentration of about 35% to 45% by vol. in a solvent , preferably methyl chloride , in presence of 0.015% to 0.15% by weight of catalyst , preferably aluminum chloride , and at a temperature within the range of −104° C. to −90° C. , wherein the velocity in the tubes is in the range from 2.4 to 4.5 m/sec , wherein the reaction mixture is introduced from the bottom side near an impeller shaft () and the outflow () is in the top , with the reaction in tube side and a cooling media in the shell side () to remove the heat of reaction , and a circulation pump installed at the bottom () , to permit high velocity of the rubber slurry in the central draft tube () and in downflow smaller tubes () , the reactor comprising:{'b': 3', '15', '6', '6, 'a—an extended upper head (), containing a fluid deflector (), having an inclined bottom up drop ...

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27-03-2014 дата публикации

SCC EQUIPPED WITH FOAM REMOVAL UNIT

Номер: US20140088273A1
Принадлежит: LG CHEM, LTD.

The present invention provides a SCC (Spinning Cone Column) equipped with a foam removal unit comprising: a housing having a rotation axis; a supply part of at least one reactant formed inside of the housing; at least two spinning cones that are installed so as to have a constant gradient from the upper part to the lower part to the rotation axis, move supplied reactants through the reactant supply part, and rotate around the rotation axis; a fixed cone that is fixed and formed on the inner side of the housing, and provides a pathway for sequentially moving reactant from a spinning cone at the upper part to a spinning cone at the lower part; a product collection part for collecting reactants moved through the spinning cone and the fixed cone; and a driving part for rotating the spinning cone, wherein a foam removal unit is installed on one side of the housing. The SCC according to the present invention solves the problems that foam is generated when separating material to be removed to decrease removal yield and lower stability of the product, and may improve removal yield and product stability because a foam removal unit is for removing generated foam is installed. 1. A SCC (Spinning Cone Column) equipped with a foam removal unit comprisinga housing having a rotation axis;a supply part of at least one reactant formed inside of the housing;at least two spinning cones that are installed so as to have a constant gradient from the upper part to the lower part to the rotation axis, move reactants supplied through the reactant supply part, and rotate around the rotation axis;a fixed cone that is fixed and formed on the inner side of the housing, and provides a pathway for sequentially moving reactant from a spinning cone at the upper part to a spinning cone at the lower part;a product collection part for collecting reactants moved through the spinning cone and the fixed cone; anda driving part for rotating the spinning cone,wherein a foam removal unit is installed on one ...

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04-01-2018 дата публикации

Heat Transfer in a Polymerization Reactor

Номер: US20180001293A1
Принадлежит:

A process comprises polymerizing an olefin monomer in a loop reactor in the presence of a catalyst and a diluent, and producing a slurry comprising solid particulate olefin polymer and diluent. The Biot number is maintained at or below about 3.0 within the loop reactor during the polymerizing process. The slurry in the loop reactor forms a slurry film having a film coefficient along an inner surface of the reactor wall, and the film coefficient is less than about 500 BTU·hr·ft·° F.. 1. A reactor comprising:{'sup': −1', '−2', '−1, 'a continuous tubular shell comprising a thickness and a thermal conductivity, wherein the continuous tubular shell defines a continuous loop; wherein a ratio of the thermal conductivity to the thickness is greater than or equal to about 120 BTU·hr·ft·° F.; and'}a slurry disposed within the continuous tubular shell, wherein the slurry comprises solid particulate olefin polymer and a diluent, and wherein the volume fraction of the solids in the slurry is greater than about 0.65.2. The reactor of claim 1 , wherein the ratio of the thermal conductivity to the thickness is greater than or equal to about 160 BTU·hr·ft·° F..3. The reactor of claim 1 , wherein the ratio of the thermal conductivity to the thickness is greater than or equal to about 250 BTU·hr·ft·° F..4. The reactor of claim 1 , wherein the ratio of the thermal conductivity to the thickness is greater than or equal to about 300 BTU·hr·ft·° F..5. The reactor of claim 1 , wherein the thermal conductivity of the shell is between about 20 and about 40 BTU·hr·ft·° F..6. The reactor of claim 1 , wherein the shell comprises a steel selected from the group consisting of: A106 Gr 8 (60) claim 1 , A516 Gr 70 claim 1 , A537 Cl 2 claim 1 , A106 Gr C (40) claim 1 , A202 Gr 8 claim 1 , A285 Gr C claim 1 , A514 Gr 8 claim 1 , A/SA516 Gr 70 claim 1 , A515 Gr 70 claim 1 , A517 Gr A claim 1 , A517 Gr 8 claim 1 , A533 Ty A C13 claim 1 , A542 Ty A C12 claim 1 , A678 Gr C claim 1 , AISI 1010 claim 1 , ...

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05-01-2017 дата публикации

POLYOLEFIN PRODUCTION WITH MULTIPLE POLYMERIZATION REACTORS

Номер: US20170001167A1
Принадлежит:

A polyolefin production system including: a first reactor configured to produce a first discharge slurry having a first polyolefin; a second reactor configured to produce a second discharge slurry having a second polyolefin; and a post-reactor treatment zone having at least a separation vessel configured to receive the second discharge slurry or both the first discharge slurry and the second discharge slurry. 1. A polyolefin production system comprising:a first reactor configured to produce a first reactor discharge comprising a first polyolefin;a second reactor configured to produce a second reactor discharge comprising a second polyolefin; anda post-reactor treatment zone configured to receive the first reactor discharge and the second reactor discharge, wherein the first and second reactors are configured to allow the first reactor discharge to be (a) transferred to the second reactor and, alternatively, (b) diverted to by-pass the second reactor and fed into the post-reactor treatment zone wherein to the first and second polyolefins are first contacted in the post-reactor treatment zone,wherein the first polyolefin is 30 weight % to 70 weight % of the second polyolefin.2. The polyolefin production system of claim 1 , wherein the first reactor and the second reactor each comprise a loop reactor.3. The polyolefin production system of claim 1 , wherein:the post-reactor treatment zone comprises a separation vessel; andthe first and second polyolefins are transferred to the separation vessel such that the first and second polyolefins are first contacted in the separation vessel.4. The polyolefin production system of claim 1 , wherein:the post-reactor treatment zone comprises a purge column; andthe first and second polyolefins are transferred to the purge column such that the first and second polyolefins are first contacted in the purge column.5. The polyolefin production system of claim 1 , wherein:the post-reactor treatment zone comprises an extruder feed tank; ...

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01-01-2015 дата публикации

SYSTEM AND METHOD FOR RAPID TRANSITIONING OF POLYOLEFIN PROCESSES FROM ONE PRODUCT TO ANOTHER

Номер: US20150005462A1
Принадлежит: Ineos USA, LLC

A gas-phase polyolefin reactor system for rapidly transitioning from one polyolefin product to another is disclosed. The reactor system comprises a steady-state control valve, a high-flow valve, a polyolefin reactor, a flow meter, a totalizer, an online analyzer and an empirical model. During a transition, the on-line analyzer measures an initial concentration of a reaction component, the empirical model predicts a required amount based upon the measured initial concentration and a selected ending concentration, the flow meter measures a flow rate, the totalizer determines a totalized amount when the flow rate of the first stream reaches the required amount based upon the measured flow rate and outputs the totalized amount to the empirical model, and the empirical model compares the required amount to the totalized amount and determines a transition endpoint. A method of rapidly transitioning the reactor system from one polyolefin product to another is also disclosed. 1. A gas-phase polyolefin reactor system , comprising:a) a steady-state control valve, wherein a first stream is connected to an input end of the steady-state control valve and to an input end of a high-flow valve and a second stream is connected to an output end of the steady-state control valve and the high-flow valve, wherein the second stream is connected to a third stream, wherein the third stream is connected to an input of a gas-phase polyolefin reactor;b) wherein the first, second and third streams comprise a reaction component, wherein an on-line analyzer measures an initial concentration of the reaction component in the third stream upstream from the gas-phase polyolefin reactor, wherein an empirical model predicts a required amount of a reaction component based upon the measured initial concentration and a selected ending concentration, wherein a flow meter measures a flow rate of the first stream near the input end of the high-flow valve and outputs the measured flow rate to a totalizer, ...

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08-01-2015 дата публикации

Methods of Making Polyethylene Polymer Comprising Polar Comonomer and Polymer Compositions

Номер: US20150011717A1
Принадлежит:

A continuous process for producing high pressure polyethylene is described. The process includes contacting first amounts of ethylene, an optional polar comonomer, and a first Cto Cmodifier in the presence of a first amount of initiator in a reaction system under polymerization conditions to form a reaction system effluent comprising a first polyethylene resin having a first concentration of unreacted monomer therein; and directing an ethylene stream and the reaction system effluent to a pressure separation unit operated at separation conditions thereby removing at least a portion of the unreacted monomer from the reaction system effluent. 1. A continuous process for producing high pressure polyethylene , comprising:{'sub': 2', '12, 'contacting a first amount of ethylene and a first amount of a Cto Cmodifier in the presence of a first amount of initiator in a reaction system under polymerization conditions to form a reaction system effluent comprising a first polyethylene resin having a first concentration of an unreacted monomer therein; and'}directing an ethylene stream and the reaction system effluent to a pressure separation unit operated at separation conditions thereby removing at least a portion of the unreacted monomer from the reaction system effluent.2. The process of claim 1 , further including providing a first amount of polar monomer claim 1 , and contacting the first amount of ethylene claim 1 , the first amount of a Cto Cmodifier and the first amount of polar monomer claim 1 , wherein the unreacted monomer comprises unreacted polar monomer.3. The process of claim 2 , further including providing a second amount of ethylene claim 2 , a second amount of polar monomer claim 2 , and a second amount of a Cto Cmodifier to the reaction system.4. The process of claim 1 , wherein the first amount of a Cto Cmodifier includes at least one saturated or unsaturated modifier claim 1 , preferably a linear or branched claim 1 , substituted or unsubstituted aldehyde or ...

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08-01-2015 дата публикации

Pressure Management for Slurry Polymerization

Номер: US20150011718A1
Принадлежит:

Processes and systems for the production for pressure management of a polymerization product flowing from a loop polymerization reactor to a separation vessel in a slurry polymerization system are disclosed herein. For example, a process comprises withdrawing a polymerization product slurry from a loop polymerization reactor, conveying the polymerization product slurry through a first line comprising a continuous take-off valve to yield a mixture comprising a vapor phase, wherein the mixture exits the continuous take-off valve, and conveying the mixture through a second line comprising a flashline heater so that the mixture has a Froude number in a range from about 5 to about 100. 1. A process for pressure management of a polymerization product in slurry polymerization , the process comprising:withdrawing a polymerization product slurry from a loop polymerization reactor;conveying the polymerization product slurry through a first line comprising a continuous take-off valve to yield a mixture comprising a vapor phase, wherein the mixture exits the continuous take-off valve; andconveying the mixture through a second line comprising a flashline heater so that the mixture has a Froude number in a range from about 5 to about 100.2. The process of claim 1 , wherein a drop in pressure of the first line is less than a drop in pressure of the second line.3. The process of claim 1 , wherein a drop in pressure of the first line is greater than a drop in pressure of the second line.4. The process of claim 1 , wherein the Froude number of the mixture conveyed through the flashline heater is in a range of about 10 to about 60.5. The process of claim 1 , wherein the flashline heater comprises a plurality of segments.6. The process of claim 5 , wherein the conveying the mixture through the second line comprising the flashline heater comprises:conveying the mixture through at least one segment of the plurality of segments of the flashline heater so that the mixture has a Froude ...

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03-02-2022 дата публикации

POLYMERIC MATERIALS

Номер: US20220033532A1
Принадлежит:

Apparatus for undertaking a chemical reaction includes an elongate housing and a receptacle. The elongate housing may include a cooling means, and end fittings, which may include ports where fluids may be introduced and/or removed. In use of the apparatus, a chemical reaction product is formed within the receptacle. Subsequently the receptacle containing the chemical reaction product is withdrawn from the elongate housing. 127-. (canceled)28. An Apparatus for undertaking a polymerisation reaction to produce a drag reducing polymer , the apparatus comprising:(a) an elongate housing; and(b) an elongate receptacle within the housing, said receptacle being arranged to receive reagents for reaction in the apparatus to produce a drag reducing polymer.29. The apparatus according to claim 28 , wherein said receptacle comprises a plastic film material which has a thickness of at least 20 μm (preferably at least 50 μm) and a thickness of less than 2000 μm (preferably less than 1000 μm); and/or wherein the internal wall area of the receptacle is defined as the area of the receptacle which is arranged to contain material (e.g. polymer in use) claim 28 , wherein at least 50% (preferably about 100%) of the internal wall area is defined by a said plastic film material which consists of a single layer.30. The apparatus according to claim 29 , wherein said plastic material of said film comprises an optionally-substituted polyolefin polymer claim 29 , for example polyethylene.31. The apparatus according to claim 29 , wherein said receptacle includes a first end and a second end which are spaced apart along the elongate extent of the receptacle claim 29 , wherein said first end is a closed end and includes a sealed region claim 29 , wherein said receptacle is formed from lay-flat tubing.32. The apparatus according to claim 31 , wherein the length of the receptacle is the linear distance between said first end and said second end claim 31 , wherein the diameter of the receptacle is ...

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02-02-2017 дата публикации

REDUCTION OF FOULING IN HIGH PRESSURE REACTORS

Номер: US20170029533A1
Принадлежит: NOVA CHEMICALS (INTERNATIONAL) S.A.

The Application of equations of state to experimental and literature data permits the formation of a model and phase diagram(s) that show under what conditions polyethylene is likely to precipitate out of a high pressure solution of polyethylene in supercritical ethylene. This then permits a better definition to run a high pressure reactor to reduce the likelihood of phase separation, loss of cooling and potentially decomposition of the reactor contents. 1. A method to determine the curve of the liquid liquid equilibrium boundary as a function of molecular weight distribution (MWD) for a multitude of different products comprising from about 80 to about 100 wt. % of ethylene and about 0 up to about 20 weight % of one or more Calpha olefins having a molecular weight from about 8 ,000 to about 500 ,000 produced in super critical ethylene in a high pressure reactor at temperatures from about 80° C. to about 350° C. and pressures from about 100 MPa to about 350 MPa comprising:a) modeling experimental or literature data for the liquid liquid equilibrium using an equation of state model to describe the effects of the molecular weight and the polydispersity of the polyethylene on the liquid liquid equilibrium curveb) determining the composition-specific parameters of the model from a); and,c) applying an equation of state model selected from TPT1, TPT1-MSA and TPT1-RHNC to the temperature, pressure and composition conditions of the reaction to generate the liquid liquid equilibrium boundary and optionally the critical polymer concentration.2. The process according to wherein the reactor is a tubular reactor.3. A process to prepare a liquid polymer lean/liquid polymer rich and liquid liquid phase diagram for a reactor for polymerizing a system comprising a polymer having a weight average molecular weight from about 8 claim 1 ,000 to about 500 claim 1 ,000 comprising from about 80 to about 100 wt % of ethylene and about 0 to about 20 wt % of one or more Calpha olefins in ...

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04-02-2016 дата публикации

CONTINUOUS EMULSION POLYMERIZATION PROCESS AND INITIATION SYSTEM

Номер: US20160032023A1
Автор: Adams David
Принадлежит:

In a continuous emulsion polymerization process, at least one monomer, an aqueous phase, and at least two different redox initiators are added to a continuous polymerization reactor comprising a first zone and a second zone. At least one redox initiator is added to the first zone and at least one redox initiator is added to the second zone. 1. A continuous emulsion polymerization process comprising:adding at least one monomer, an aqueous phase, and at least two different redox initiators to a continuous tubular reactor comprising (1) a circulating loop section and (2) a secondary line section having one end connected to a discharge opening of the loop section and a polymer outlet at its other end; andpolymerizing the at least one monomer.2. The process of claim 1 , wherein each redox initiator comprises a reducing agent and an oxidizing agent.3. The process of claim 1 , wherein the at least two different redox initiators are added to the tubular reactor at different locations.4. The process of claim 2 , wherein at least one of the at least two different redox initiators is added to the circulating loop section of the tubular reactor.5. The process of claim 4 , wherein the reducing agent from at least one of the at least two different redox initiators is added to the secondary line section of the tubular reactor.6. The process of claim 4 , wherein oxidizing agent from at least one of the at least two different redox initiators is added to the secondary line section of the tubular reactor.7. The process of claim 2 , wherein at least one of the at least two different redox initiators is water soluble and at least one of the at least two different redox initiators is oil soluble.8. The process of claim 7 , wherein the water soluble initiator is added to the reactor upstream of where the oil soluble initiator is added.9. The process of claim 7 , wherein the oxidizing agent from the oil soluble redox initiator is added to the circulating loop section of the tubular ...

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11-02-2016 дата публикации

APPARATUS FOR PRODUCING WATER-ABSORBENT RESIN

Номер: US20160039950A1
Принадлежит: Sumitomo Seika Chemicals Co., Ltd.

In an apparatus for producing the water-absorbent resin, gas heated by the polymerization heat accompanied by a polymerization reaction in a reactor main body flows through a first pipe into a heat exchanging structure, and a cooled fluid obtained by the cooling flows through a second pipe into the reactor main body. In the apparatus, a first pipe temperature adjusting portion adjusts a temperature of the first pipe to fall within a predetermined temperature range, and a polymerization reactor temperature adjusting portion adjusts a temperature of an upper portion of the reactor main body to fall within a predetermined temperature range. 1. An apparatus for producing a water-absorbent resin , comprising: a reactor main body in which the water soluble ethylenically unsaturated monomer and the liquid medium is contained and an upper portion of which is left for a gaseous phase portion, and', 'a gas discharging portion which is connected to the reactor main body and discharges gas of the gaseous phase portion from the reactor main body;, 'a polymerization reactor in which a water-absorbent resin is produced by polymerization reaction on a water soluble ethylenically unsaturated monomer in a liquid medium, the polymerization reactor including'}a first channel portion having a first channel which is connected to the gas discharging portion and through which the gas discharged from the reactor main body by the gas discharging portion flows;a first channel portion temperature adjusting portion which adjusts a temperature of the first channel portion to fall within a predetermined temperature range in which the gas flowing through the first channel of the first channel portion is not condensed; a cooler main body which is connected to the first channel portion, into which the gas flowing through the first channel of the first channel portion flows, and which cools inflow gas, and', 'a cooled fluid discharging portion which is connected to the cooler main body and discharges ...

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01-05-2014 дата публикации

Pressure Management for Slurry Polymerization

Номер: US20140121334A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

Processes and systems for the production for pressure management of a polymerization product flowing from a loop polymerization reactor to a separation vessel in a slurry polymerization system are disclosed herein. For example, a process comprises withdrawing the polymerization product from a loop polymerization reactor, and conveying the withdrawn polymerization product to a separation vessel via a first pressure differential and a second pressure differential. The withdrawn polymerization product may flow through the first pressure differential before flowing through the second pressure differential, and the first pressure differential may be less than the second pressure differential. 1. A process for pressure management of a polymerization product in slurry polymerization , the process comprising:withdrawing the polymerization product from a loop polymerization reactor; andconveying the withdrawn polymerization product to a separation vessel via a first pressure differential and a second pressure differential, wherein the withdrawn polymerization product flows through the first pressure differential before flowing through the second pressure differential, wherein the first pressure differential is less than the second pressure differential.2. The process of claim 1 , wherein the first pressure differential has a drop in pressure between about 5% to about 50% of a total pressure differential between the loop polymerization reactor and the separation vessel claim 1 , wherein the second pressure differential has a drop in pressure between about 50% to about 95% of the total pressure differential between the loop polymerization reactor and the separation vessel.3. The process of claim 2 , wherein the drop in pressure of the first pressure differential is greater than 40% and less than 50% of the total pressure differential claim 2 , wherein the drop in pressure of the second pressure differential is greater than 50% and less than 60% of the total pressure ...

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22-02-2018 дата публикации

POLYMERIZATION REACTOR

Номер: US20180050318A1
Принадлежит: LG CHEM, LTD.

The present invention relates to a polymerization reactor. The polymerization reactor according to one aspect of the present invention comprises: a housing including a supply part for supplying a reactant; a tube which is provided inside the housing and extends along the height direction of the housing; a first impeller including a blade which spirally surrounds the tube along the height direction of the housing; a second impeller which is provided inside the housing in order to enable the reactant to flow into the tube; and a partition wall which is provided to surround the second impeller along the circumferential direction. 1. A polymerization reactor comprisinga housing including a supply part for supplying a reactant;a tube which is provided inside the housing and extends along the height direction of the housing;a first impeller including a blade which spirally surrounds the tube along the height direction of the housing;a second impeller which is provided inside the housing in order to enable the reactant to flow into the tube; anda partition wall which is provided to surround the second impeller along the circumferential direction.2. The polymerization reactor according to claim 1 , whereinthe second impeller is provided in a lower region of the housing, andthe supply part is provided in the lower region of the housing such that the reactant is fed into the partition wall.3. The polymerization reactor according to claim 2 , whereinthe farther the partition wall is from the tube, it is provided to have the higher diameter.4. The polymerization reactor according to claim 3 , whereinthe partition wall is provided such that an edge having a maximum diameter is spaced from an inner peripheral surface of the housing.5. The polymerization reactor according to claim 3 , whereinthe partition wall is provided such that its minimum diameter is equal to the diameter of the tube.6. The polymerization reactor according to claim 3 , whereinthe partition wall is provided ...

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03-03-2016 дата публикации

SLURRY PHASE POLYMERISATION PROCESS

Номер: US20160060369A1
Принадлежит:

A process comprising polymerizing in a loop reactor an olefin monomer optionally together with an olefin commoner in the presence of a polymerisation catalyst in a diluent to produce a slurry comprising solid particulate olefin polymer and the diluent wherein the Froude number is maintained at or below 20 is disclosed. 121-. (canceled)22. A process comprising polymerizing in a loop reactor an olefin monomer optionally together with an olefin comonomer in the presence of a polymerization catalyst in a diluent to produce a slurry comprising solid particulate olefin polymer and the diluent wherein the Froude number is maintained at or below 20 , wherein the loop reactor has an internal diameter of over 500 millimeters , wherein the solids concentration of the slurry in the loop reactor is above 20 vol % and wherein the loop reactor is one of two or more reactors connected in series and being used to produce a multimodal polymer , and at least one of the following applies:i) hydrogen is maintained at a low (or zero) concentration in the reactor(s) manufacturing the high molecular weight components and hydrogen is maintained at a high concentration in the reactor(s) manufacturing the low molecular weight components,ii) there is being produced a polymer with molecular weight less than 50 kDaltons,iii) there is being produced a polymer with molecular weight greater than 200 kDaltons,iv) there is being produced a polymer with a melt index below 0.1,v) there is being produced a polymer with a melt index above 50.23. A process as claimed in wherein the Froude number is in the range 2 to 15.24. A process as claimed in wherein the Froude number is in the range 3 to 10.25. A process as claimed in wherein the solids concentration of the slurry in the loop reactor is above 30 vol %.26. A process as claimed in wherein the solids concentration of the slurry in the loop reactor is in the range 40-60 wt % based on the total weight of the slurry.27. A process as claimed in wherein the ...

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12-06-2014 дата публикации

Method for Transforming a Single Reactor Line

Номер: US20140163182A1
Принадлежит: TOTAL RESEARCH & TECHNOLOGY FELUY

The present invention discloses a method for transforming a single reactor line into a double reactor line wherein the existing single reactor line is equipped with a flash tank for separating the solid polymer product from the flash vapour and wherein the vapour is sent to a system of at least two separating columns allowing the separation of its constituents into monomer, diluent and comonomer. 18-. (canceled)9. A method for transforming a single reactor line into a double reactor line comprising:adding a second single reactor line in front of a first existing single reactor line, wherein the second single reactor line is smaller than or of the same size as the first existing single reactor line; or rearranging connections between the legs in order to obtain a first reactor line and a second reactor line, wherein the first reactor line is smaller than or of the same size as the second reactor line;', 'adding a pump to the first reactor line, the second reactor line or combinations thereof; and', 'adding a continuous transfer line to transport polymer from the first reactor line to the second reactor line;, 'transforming the first existing single reactor line into a double reactor line, wherein the first existing single reactor line comprises at least 6 legs, and wherein the first existing single reactor line is transformed bywherein the first existing single reactor line comprises two or more settling legs configured to sequentially discharge settled polymer slurry.10. The method of claim 9 , wherein the transforming the first existing single reactor line into the double reactor line is performed claim 9 , and wherein the first reactor line has a smaller capacity than that of the second reactor line.11. The method of claim 9 , wherein the adding the second single reactor line in front of the first existing single reactor line is performed.12. The method of claim 9 , wherein polymer product exiting the first reactor line is sent to the second reactor line through a ...

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19-06-2014 дата публикации

METHOD FOR RECOVERING POLYMER AND APPARATUS THEREFOR

Номер: US20140171611A1
Принадлежит: Borealis AG

Process and apparatus for recovering polymer from a a gas phase reactor having a distribution plate via an outlet vessel comprising at least one apparatus for the breakup of polymeric agglomerates, the apparatus further comprising a feed pipe connecting the gas phase reactor and the outlet vessel a return gas line connecting the gas phase reactor and the outlet vessel, means for varying the flow rate through the return gas line from the outlet vessel to the gas phase reactor, and means for varying the outlet rate of polymer product from the outlet vessel. 1. (canceled)2. (canceled)3. (canceled)4. (canceled)5. (canceled)6. (canceled)7. (canceled)8. (canceled)9. (canceled)10. (canceled)11. (canceled)12. (canceled)13. (canceled)14. (canceled)15. (canceled)16. (canceled)17. (canceled)183312514. A process for recovering polymer from a gas phase reactor () , the gas phase reactor () having a distribution plate and being connected to an outlet vessel () via a feed pipe () and a return gas line () , the outlet vessel () comprising at least one apparatus for the breakup of polymeric agglomerates () , [{'b': 3', '2', '1, 'continuously discharging polymeric material from the gas phase reactor () via the feed pipe () to the outlet vessel (),'}, {'b': '4', 'passing the polymeric material into the at least one apparatus for breakup of polymeric agglomerates (),'}, {'b': '1', 'recovering polymer from the outlet vessel (), whereby'}, {'b': 3', '2', '5', '1', '3', '1, 'the bed level height in the gas phase reactor () and the flow through the feed pipe () are controlled by controlling the flow rate through the return gas line () from the outlet vessel () to the gas phase reactor (), and/or by controlling the outlet rate of polymer product from the outlet vessel ().'}], 'the process comprising19312. Process according to claim 18 , whereby the gas phase reactor () and the outlet vessel () are connected by a connecting passage including the feed pipe () claim 18 , wherein the connecting ...

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09-04-2015 дата публикации

FLUIDIZED BED POLYMERIZATION REACTOR AND PROCESS FOR PREPARING POLYMER

Номер: US20150099854A1
Принадлежит:

The invention provides a fluidized bed polymerization reactor, including: a column, in which a liquid distributor and a gas distributor above the liquid distributor are arranged, so that the reaction zone being divided into a first zone and a second zone through the gas distributor; and a circulating unit for circulating the gas material originated from the top zone of the column into the bottom zone thereof in a form of gas-liquid mixture. The gas-liquid mixture is undergone a gas-liquid separation in the bottom zone, the gas phase portion obtained being fed to the gas distributor and then into the second zone while the liquid phase portion obtained being entered into the first zone through the liquid distributor, so that the temperature in the first zone is lower than that in the second zone. Therefore, polymer with a molecular weight distributed in a relatively wide range can be obtained. The invention further provides a method for preparing polymer. 124-. (canceled)25. A fluidized bed polymerization reactor , including:{'b': 1', '2', '8', '11', '12, 'a column (), in which a liquid distributor () and a gas distributor () above the liquid distributor are arranged, wherein liquid reactant is fed into a bottom zone in the column under the liquid distributor, and enters into a reaction zone above the liquid distributor after passing through the liquid distributor, the reaction zone being divided into a first zone () under the gas distributor and a second zone () above the gas distributor; and'}{'b': '20', 'a circulating unit () for circulating the gas material originated from the top zone of the column into the bottom zone thereof in a form of gas-liquid mixture,'}wherein the gas-liquid mixture is undergone a gas-liquid separation in the bottom zone, the gas phase portion obtained being fed to the gas distributor and then into the second zone while the liquid phase portion obtained being entered into the first zone through the liquid distributor, so that the ...

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10-07-2014 дата публикации

METHODS FOR PROCESSING AND INTERPRETING SIGNALS FROM STATIC AND ACOUSTIC PROBES IN FLUIDIZED BED REACTOR SYSTEMS

Номер: US20140194582A1

Provided is a method for operating a gas-phase, fluidized-bed reactor. The method has the steps of (a) receiving a signal from a probe in contact with the interior of the reactor or a process component in communication with the reactor, wherein the signal is derived from a physical property or condition within the reactor or the process component; (b) modifying the signal to create a modified signal; and (c) adjusting one or more operating parameters of the reactor in response to the modified signal if the physical property or condition is different than a desired value. There is also a method for reducing fouling in a distributor plate of a gas-phase, fluidized-bed reactor with a recycle line. 1. A method for operating a gas-phase , fluidized-bed reactor , comprising:(a) receiving a signal from a probe in contact with the interior of the reactor or a process component in communication with the reactor, wherein the signal is derived from a physical property or condition within the reactor or the process component;(b) modifying the signal to create a modified signal; and(c) adjusting one or more operating parameters of the reactor in response to the modified signal if the physical property or condition is different than a desired value.2. The method of claim 1 , wherein the probe is one or more acoustic probes.3. The method of claim 1 , wherein the probe is one or more static probes.4. The method of claim 1 , wherein the probe is one or more coated static probes.5. The method of claim 1 , wherein the probe is a combination of one or more acoustic probes and one or more static probes.6. The method of claim 3 , wherein the signal from the one or more static probes is derived from a physical property or condition selected from the group consisting of fluctuating or changing electric field claim 3 , presence of transient surface active species claim 3 , bubble size claim 3 , bubble transit time claim 3 , and sign of passing individual charged particles.7. The method of ...

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10-07-2014 дата публикации

SYSTEM AND METHOD FOR CLOSED RELIEF OF A POLYOLEFIN LOOP REACTOR SYSTEM

Номер: US20140194583A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

A reactor system including an enclosed pressure relief system and/or a control system. The enclosed pressure relief system including a slurry separation system communicatively coupled with a pressure relief valve coupled to a loop reactor such that activation of the pressure relief valve results in discharge of a slurry from the loop reactor to the slurry separation system, wherein the slurry separation system is capable of separating solid and liquid components from gas components of the slurry and transmitting the gas components to a flare via a flare header. 1. A system , comprising:a loop reactor comprising a settling leg or a continuous take-off;a pressure relief valve coupled to the loop reactor; anda flash chamber configured to receive a discharge stream from the settling leg or the continuous take-off of the loop reactor, wherein the flash chamber is communicatively coupled with the pressure relief valve such that activation of the pressure relief valve results in a discharge of a slurry from the loop reactor to the flash chamber.2. The system of claim 1 , wherein the flash chamber is configured to separate solid and liquid components from gas components of the slurry and transmit the gas components to a flare via a flare header.3. The system of claim 2 , comprising an accumulator coupled to a bottom of the flash chamber to facilitate gravity feed of the solid and liquid components from the flash chamber to the accumulator.4. The system of claim 1 , wherein the flash chamber is configured to separate solid and liquid components from gas components of the slurry and transmit the gas components to a fractionation system claim 1 , and wherein the fractionation system is configured to transmit at least a portion of the gas components to a flare via a flare header.5. The system of claim 1 , comprising a control system configured to employ a plurality of interlocks to control reaction conditions of the loop reactor.6. The system of claim 1 , wherein the pressure ...

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07-05-2015 дата публикации

CHAIN TRANSFER AGENT REMOVAL BETWEEN POLYOLEFIN POLYMERIZATION REACTORS

Номер: US20150126693A1
Принадлежит:

A system and method for polymerizing olefin in the presence of a chain transfer agent in a first reactor to form a first polyolefin, discharging from the first reactor a transfer shiny having the first polyolefin and the chain transfer agent, and processing the transfer slurry in a separator to remove chain transfer agent and to provide a fluff slurry having the first polyolefin and a lower content of chain transfer agent than in the transfer slurry. The system and method provide for feeding the fluff slurry to a second reactor, polymerizing olefin in the second reactor to form a second polyolefin, and discharging from the second reactor a slurry having the second polyolefin. 1. A polyolefin reactor system comprising:a first polymerization reactor configured to polymerize olefin monomer in the presence of a chain transfer agent, and to discharge continuously a transfer slurry comprising a first polyolefin and the chain transfer agent;a separation system configured to receive the transfer slurry and to discharge a recycle stream comprising the chain transfer agent, and to discharge continuously a fluff slurry comprising the first polyolefin; anda second polymerization reactor configured to receive the fluff slurry from the separation system and to discharge a product slurry comprising a second polyolefin.2. The polyolefin reactor system of claim 1 , wherein the first polyolefin is continuously transferred from the first polymerization reactor claim 1 , through the separation system and to the second polymerization reactor.3. The polyolefin reactor system of claim 13 , wherein a greater first loop polymerization reactor pressure provides motive force to drive the transfer slurry from the first polymerization reactor and through the separation system.4. The polyolefin reactor system of claim 13 , wherein a first loop polymerization reactor pressure provides motive force to drive the transfer slurry from the first polymerization reactor and through the separation system ...

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25-08-2022 дата публикации

REACTION CONFIGURATION AND PROCEDURE FOR POLYMERS PRODUTION

Номер: US20220267482A1
Принадлежит: Versalis S.p.A.

There is a procedure for polymerisation in solution for the production of polymers. The procedure has the following steps: (A) continuously feeding one or more monomers, one or more solvents in a quantity comprised between 70% and 90% by weight with respect to the reagent mixture, and a catalytic system, to a first stirred reaction volume, wherein a single mixing cell is formed, in which the polymerisation begins, until a conversion is attained that varies from 20% to 70% with respect to the final conversion achieved and (B) proceeding the polymerisation in at least one second stirred reaction volume connected in series to the first reaction volume, in which two or more mixing cells are formed, at the outlet of which the final conversion of the monomer is attained. In the first reaction volume, the average residence time of the reagent mixture varies within an interval ranging from 10% to 25% with respect to the average residence time of the entire reaction volume. 2. The procedure according to claim 1 , wherein claim 1 , in the first reaction volume claim 1 , the specific stirring power is greater than the specific stirring power of the volumes subsequent to the first.3. The procedure according to claim 2 , wherein claim 2 , in the first reaction volume claim 2 , the specific stirring power is greater than 2 kW/m.4. The procedure according to claim 3 , wherein claim 3 , in the reaction volumes subsequent to the first volume the specific stirring power is comprised between 1 kW/mand 2 kW/m.5. The procedure according to claim 1 , wherein the average residence time of the entire reaction volume is typically comprised between 1 hour and 2 hours.6. The polymerisation procedure for the production of polymers according to claim 1 , wherein the average residence time of the monomer in the first reaction volume varies from 15% to 20% of the total residence time of the entire reaction volume.7. The polymerisation procedure for the production of polymers according to claim 1 ...

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14-05-2015 дата публикации

Methods of Controlling Dual Catalyst Olefin Polymerizations With An Alcohol Compound

Номер: US20150133612A1
Принадлежит:

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. 120-. (canceled)21. A method of controlling a polymerization reaction in a polymerization reactor system , the method comprising:{'sub': 3', '10, '(i) contacting a dual catalyst system with ethylene and a C-Calpha-olefin comonomer in the polymerization reactor system under polymerization conditions to produce an ethylene copolymer,'}wherein the dual catalyst system comprises a first metallocene catalyst component, a second metallocene catalyst component, an activator, and a co-catalyst;wherein the polymerization reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof; and(ii) introducing an amount of an alcohol compound into the polymerization reactor system to (I) reduce a melt index parameter of the ethylene copolymer; (II) increase a molecular weight parameter of the ethylene copolymer selected from Mw, Mz, or both; or (III) reduce a melt index parameter of the ethylene copolymer and increase a molecular weight parameter of the ethylene copolymer selected from Mw, Mz, or both.22. The method of claim 21 , wherein the alcohol compound comprises a Cto Cmono alcohol.23. The method of claim 21 , wherein the alcohol compound comprises ethylene glycol claim 21 , propylene glycol claim 21 , or both.24. The method of claim 21 , wherein the polymerization reactor system comprises two or more reactors.25. The method of claim 21 , wherein the activator comprises an aluminoxane compound claim 21 , an organoboron or organoborate compound claim 21 , an ionizing ionic compound claim 21 , or any combination thereof.26. The method of claim 21 , wherein:the polymerization reactor system comprises a loop slurry reactor;the alcohol compound comprises methanol, ethanol, propanol, butanol, ...

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14-05-2015 дата публикации

Process and Plant for Manufacturing Polyethylene-Diene-Copolymers

Номер: US20150133616A1
Принадлежит:

The present invention provides a process for manufacturing polyethylene-diene-copolymer conducted in a plant including at least one compressor unit, at least one preheater unit downstream of the compressor unit and at least one reactor, in particular a reactor, downstream of the compressor unit and the preheater unit. The process comprising the steps of (a) feeding a first feed stream comprising ethylene into the at least one compressor unit and subsequently into the at least one preheater unit, and (b1) feeding a second feed stream including at least one diene comonomer to the first feed stream leaving the at least preheater unit, and feeding the combined feed streams including ethylene and the at least one diene comonomer to the at least one reactor, and/or (b2) feeding a second feed stream including at least one diene comonomer to the at least one reactor at at least one location along the reactor. 1. A process for manufacturing polyethylene-diene copolymer conducted in a plant comprising at least one compressor unit , at least one preheater unit downstream of the compressor unit , and at least one reactor downstream of the compressor unit and the preheater unit ,the process comprising the steps of:a) feeding a first feed stream comprising ethylene into the at least one compressor unit and subsequently into the preheater unit, andb1) feeding a second feed stream comprising at least one diene comonomer to the first feed stream leaving the preheater unit, and feeding the combined feed streams comprising ethylene and the at least one diene comonomer to the at least one reactor, orb2) feeding a second feed stream comprising at least one diene comonomer to the at least one reactor at at least one location along the reactor.2. The process according to claim 1 , wherein the ethylene of the first feed stream is fresh ethylene claim 1 , ethylene recycled from the reactor without any further purification and/or ethylene recycled from the reactor which underwent gas ...

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21-05-2015 дата публикации

OLEFIN POLYMERIZER, POLYOLEFIN PRODUCTION SYSTEM, AND PROCESS FOR PRODUCING POLYOLEFIN

Номер: US20150141589A1
Автор: SATO Hideki
Принадлежит: Sumitomo Chemical Company, Limited

An olefin polymerization reactor comprising a tubular portion that extends in a vertical direction; a tapered portion disposed inside the tubular portion, an inside diameter of the tapered portion decreasing downwardly, and including a vertically penetrating orifice at a bottom end thereof; a tubular lower deflector disposed above the orifice of the tapered portion, an outside diameter of the tubular lower deflector increasing downwardly, a bottom end thereof being located away from an inner wall of the tubular portion, and including a vertically penetrating orifice at a top end thereof; and an upper deflector disposed above the orifice of the lower deflector, an outside diameter of the upper deflector increasing downwardly, a top end thereof being closed, a bottom end thereof being located away from the inner wall of the tubular portion, and an outside diameter at the bottom end being equal to or greater than an inside diameter of the orifice of the lower deflector. 1. An olefin polymerization reactor comprising:a tubular portion that extends in a vertical direction;a tapered portion disposed inside the tubular portion, an inside diameter of the tapered portion decreasing downwardly, and comprising a vertically penetrating orifice at a bottom end thereof;a tubular lower deflector disposed above the orifice of the tapered portion, an outside diameter of the tubular lower deflector increasing downwardly and a bottom end thereof being located away from an inner wall of the tubular portion, and comprising a vertically penetrating orifice at a top end thereof; andan upper deflector disposed above the orifice of the lower deflector, an outside diameter of the upper deflector increasing downwardly, a top end thereof being closed, a bottom end thereof being located away from the inner wall of the tubular portion, and an outside diameter at the bottom end being equal to or greater than an inside diameter of the orifice of the lower deflector.2. The polymerization reactor ...

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28-05-2015 дата публикации

SYSTEM AND METHOD FOR RAPID TRANSITIONING OF POLYOLEFIN PROCESSES FROM ONE PRODUCT TO ANOTHER

Номер: US20150147234A1
Принадлежит: Ineos USA, LLC

A gas-phase polyolefin reactor system for rapidly transitioning from one polyolefin product to another is disclosed. The reactor system comprises a control valve, a high-flow valve, a polyolefin reactor, a flow meter, a totalizer and an empirical model. During a transition, the empirical model predicts a required amount based upon an initial concentration and a selected ending concentration, the flow meter measures a flow rate, the totalizer determines a totalized amount when the flow rate of the first stream reaches the required amount based upon the measured flow rate and outputs the totalized amount to the empirical model, and the empirical model compares the required amount to the totalized amount and determines a transition endpoint. A method of rapidly transitioning the reactor system from one polyolefin product to another is also disclosed. 125-. (canceled)26) A gas-phase polyolefin reactor system , comprising:a) a control valve, wherein a first stream is connected to an input end of the control valve and to an input end of a high-flow valve and a second stream is connected to an output end of the control valve and the high-flow valve, wherein the second stream is connected to a third stream, wherein the third stream is connected to an input of a gas-phase polyolefin reactor;b) wherein the first, second and third streams comprise a reaction component, wherein an empirical model predicts a required amount of a reaction component based upon an initial concentration and a selected ending concentration, and wherein a flow meter measures a flow rate of the first stream near the input end of the high-flow valve and outputs the measured flow rate to a totalizer.27) The system of claim 26 , wherein an on-line analyzer measures the initial concentration of the reaction component in the third stream upstream from the gas-phase polyolefin reactor.28) The system of claim 26 , wherein the totalizer determines a totalized amount when the flow rate of the first stream ...

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28-05-2015 дата публикации

SYSTEM AND METHOD FOR RAPID TRANSITIONING OF POLYOLEFIN PROCESSES FROM ONE PRODUCT TO ANOTHER

Номер: US20150148506A1
Принадлежит: Ineos USA, LLC

A gas-phase polyolefin reactor system for rapidly transitioning from one polyolefin product to another is disclosed. The reactor system comprises a control valve, a high-flow valve, a polyolefin reactor, a flow meter, a totalizer and an empirical model. During a transition, the empirical model predicts a required amount based upon an initial concentration and a selected ending concentration, the flow meter measures a flow rate, the totalizer determines a totalized amount when the flow rate of the first stream reaches the required amount based upon the measured flow rate and outputs the totalized amount to the empirical model, and the empirical model compares the required amount to the totalized amount and determines a transition endpoint. A method of rapidly transitioning the reactor system from one polyolefin product to another is also disclosed. 112.-. (canceled)13. A method of transitioning a gas-phase polyolefin reactor system , comprising the steps of: 'i) a control valve, wherein a first stream is connected to an input end of the control valve and to an input end of a high-flow valve and a second stream is connected to an output end of the control valve and the high-flow valve, wherein the second stream is connected to a third stream, wherein the third stream is connected to an input of the gas-phase polyolefin reactor;', 'a) providing a gas-phase polyolefin reactor system comprisingb) selecting an ending reactant component concentration;c) obtaining a starting reactant concentration;d) predicting a required amount of reactant component with an empirical model based upon the starting reactant component concentration and the selected ending reactant component concentration;e) measuring a flow rate of the first stream near the input end of the high-flow valve to obtain a measured flow rate of the first stream; andf) estimating a transition endpoint using the empirical model and a totalizer based upon the required amount of reactant component and the measured ...

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24-06-2021 дата публикации

Polymerization Processes

Номер: US20210189023A1
Принадлежит:

In a gas phase fluidized bed polymerization process for the production of polyolefin polymers, such as polyethylene polymers or polypropylene polymers, loss of ethylene or propylene accompanying inert gas purging is reduced by passing an ethylene- or propylene-containing purge stream through a vent column to contact a hydrocarbon liquid flowing through the vent column contercurrent to the purge stream whereby unreacted ethylene or propylene in the purge stream portion is dissolved in the hydrocarbon liquid to produce an ethylene- or propylene-enriched liquid stream and an ethylene- or propylene-depleted gaseous stream. The ethylene- or propylene-enriched liquid stream is then recycled to the fluidized bed reactor, while at least part of the ethylene- or propylene-depleted gaseous stream is purged. 1. A gas phase fluidized bed polymerization process for the production of polyethylene polymers or polypropylene polymers , the process comprising:(a1) supplying at least one particulate catalyst to at least one fluidized bed reaction zone using at least one inert carrier gas;(b1) continuously supplying at least one feed stream comprising ethylene or propylene to the at least one fluidized bed reaction zone operating under polymerization conditions effective to produce the polyethylene polymers or polypropylene polymers;(c1) withdrawing from the at least one fluidized bed reaction zone at least a portion of the polyethylene polymers or polypropylene polymers and at least one gaseous recycle stream comprising the at least one inert carrier gas and unreacted ethylene or propylene;(d1) compressing and cooling the at least one gaseous recycle stream to produce a compressed and cooled recycle stream;(e1) returning at least a first portion of the compressed and cooled at least one recycle stream to the fluidized bed reactor;(f1) withdrawing at least a second portion of the compressed and cooled recycle stream through at least one vent column to contact a hydrocarbon liquid ...

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16-06-2016 дата публикации

Methods for processing and interpreting signals from static and acoustic probes in fluidized bed reactors

Номер: US20160168278A1
Принадлежит: ExxonMobil Research and Engineering Co

Provided is a method for operating a gas-phase, fluidized-bed reactor. The method has the steps of (a) receiving a signal from a probe in contact with the interior of the reactor or a process component in communication with the reactor, wherein the signal is derived from a physical property or condition within the reactor or the process component; (b) modifying the signal to create a modified signal; and (c) adjusting one or more operating parameters of the reactor in response to the modified signal if the physical property or condition is different than a desired value. There is also a method for reducing fouling in a distributor plate of a gas-phase, fluidized-bed reactor with a recycle line.

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25-06-2015 дата публикации

Double Loop Technology

Номер: US20150175720A1
Принадлежит:

The present invention relates to an apparatus and process for polymerizing olefins. One embodiment comprises polymerizing at least one monomer in a first loop reactor in the presence of a catalyst to produce a first polyolefin fraction. A portion of the first polyolefin fraction is transferred to a second loop reactor, connected in series with the first loop reactor. The process further comprises polymerizing in the second loop reactor at least one monomer in the presence of a catalyst to produce a second polyolefin fraction in addition to the first polyolefin fraction. The combination of the first and second polyolefin fractions can produce a polymer resin fluff having bimodal molecular weight distribution. 123-. (canceled)24. A process comprising:polymerizing olefin monomers in the presence of an anti-fouling agent and a chromium-type catalyst, a late Transition Metal type catalyst, or a Ziegler Natta catalyst;{'sub': 'w', 'claim-text': [{'sub': 2', '2', 'k, 'one or more blocks —(CHCHO)—, wherein each k ranges from 1 to 50; and'}, {'sub': 2', 'n, 'one or more blocks —(CH—CH(R)—O)—, wherein each R comprises an alkyl group having from 1 to 6 carbon atoms and each n ranges from 1 to 50, wherein the anti-fouling polymer is terminated by R′ and R″ end groups, wherein R′ is OH or an alkoxy having from 1 to 6 carbon atoms and R″ is H or an alkyl having from 1 to 6 carbon atoms.'}], 'wherein the anti-fouling agent comprises an anti-fouling polymer having an average molecular weight (M) of greater than 1000 daltons and containing25. The process of claim 24 , wherein R is methyl.26. The process of claim 24 , wherein the anti-fouling agent is liquid at room temperature.27. The process of claim 24 , wherein the anti-fouling polymer has a molecular weight (M) of at least about 2000.28. The process of claim 24 , wherein the ends of the anti-fouling polymer are hydrophilic.29. The process of claim 24 , wherein the anti-fouling agent comprises a block copolymer having general ...

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06-06-2019 дата публикации

HIGH-PRESSURE POLYMERIZATION PROCESS OF ETHYLENICALLY UNSATURATED MONOMERS CARRED OUT IN A POLYMERIZATION REACTOR INSTALLED WITHIN A PROTECTIVE ENCLOSURE

Номер: US20190169318A1
Принадлежит: BASELL POLYOLEFINE GMBH

A process for polymerizing or copolymerizing ethylenically unsaturated monomers at pressures in the range of from 110 MPa to 500 MPa in a production line comprising a continuously operated polymerization reactor which is installed within a protective enclosure, wherein the production line is monitored with respect to an occurrence of a leakage of monomers or of reaction mixture and a water based deluge system, which provides droplets of a diameter in a range from 25 μm to 20 mm to the enclosed area, is automatically started with a minimum flow rate of 10 L/min per mof enclosed area when a leakage of monomers or of reaction mixture is detected. 1. A process for polymerizing or copolymerizing one or more ethylenically unsaturated monomers at temperatures from 100° C. to 350° C. and pressures in the range of from 110 MPa to 500 MPa in a production line comprising a continuously operated polymerization reactor which is installed within a protective enclosure , monitoring the production line with respect to an occurrence of a leakage of monomers or of reaction mixture, and', {'sup': '2', 'automatically starting a water based deluge system, which provides droplets of a diameter in a range from 25 μm to 20 mm to the enclosed area when a leakage of monomers or of reaction mixture is detected, and the droplets are provided with a minimum flow rate of 10 L/min per mof enclosed area.'}], 'the process comprising'}2. The process of claim 1 , wherein the droplets are provided to at least 10% of the enclosed area.3. The process of claim 1 , wherein the water based deluge system operates by providing water.4. The process of claim 1 , wherein the water based deluge system operates by providing a solution of radical capturing salts.5. The process of claim 1 , wherein the polymerization is carried out in a production line in which the monomers are brought to the polymerization pressure by one or more compressors in a sequence of compression stages in which the compressed gas mixture ...

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18-09-2014 дата публикации

POLYOLEFIN PRODUCTION WITH DIFFERENT DILUENTS IN MULTIPLE POLYMERIZATION REACTORS

Номер: US20140275450A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY, LP

A system and method for producing polyolefin, including a polyolefin reactor system having: a first reactor to produce a first reactor discharge stream having a first polyolefin and a first diluent; and a second reactor to receive at least a portion of the first reactor discharge stream and to produce a second reactor discharge stream having a second polyolefin and a second diluent, wherein the second diluent is different than the first diluent. 1. A polyolefin reactor system comprising:a first reactor configured to produce a first reactor discharge stream comprising a first polyolefin and a first diluent composition; anda second reactor configured to receive at least a portion of the first reactor discharge stream and to produce a second reactor discharge stream comprising a second polyolefin and a second diluent composition, wherein the second diluent composition is different than the first diluent composition.2. The polyolefin reactor system of claim 1 , wherein the first diluent composition and the second diluent composition comprise a different Hildebrand solubility parameter value.3. The polyolefin reactor system of claim 1 , wherein the first diluent composition and second diluent composition comprise a different boiling point.4. The polyolefin reactor system of claim 1 , wherein the first diluent composition and the second diluent composition comprise a different heat capacity.5. The polyolefin reactor system of claim 1 , wherein the first reactor discharge stream is fed to a separator to remove at least a portion of the first diluent composition to form a first diluent recycle stream.6. The polyolefin reactor system of claim 4 , wherein the separator is a hydrocyclone or a wash column.7. A polyolefin reactor system comprising:a first reactor configured to receive a first diluent and to produce a first reactor discharge comprising the first diluent and a first polyolefin;a separator configured to receive at least a portion of the first reactor discharge and ...

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23-07-2015 дата публикации

Monomer/Diluent Recovery

Номер: US20150203601A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

The disclosure includes a polymerization process and an olefin polymerization system. A polymerization product is produced, a vapor phase is recovered from the polymerization product, the vapor phase is fractionated in a first column to yield a fraction stream, and the fraction stream is fractionated in a second column. A first stream of the second column, which comprises a diluent, can be recycled to a first polymerization reactor. A second stream of the second column, which comprises olefin monomer, diluent, and hydrogen, can be recycled to a second polymerization reactor. Comonomer may be recycled from the first column to the first polymerization reactor, the second polymerization reactor, or both. 1. A polymerization process comprising:producing a polymerization product;recovering a vapor phase from the polymerization product;fractionating the vapor phase in a first column to yield a fraction stream;fractionating the fraction stream in a second column;emitting a first stream and a second stream from the second column, wherein the first stream comprises a diluent, wherein the second stream comprises an olefin monomer, the diluent, and hydrogen;recycling at least a portion of the diluent of the first stream to a first polymerization reactor; andrecycling at least a portion of the diluent, at least a portion of the olefin monomer, and at least a portion of the hydrogen of the second stream to a second polymerization reactor.2. The process of claim 1 , wherein producing a polymerization product comprises:polymerizing the olefin monomer, and optionally an olefin comonomer, in the presence of the diluent to yield a first component of a solid polymer of the polymerization product in a first polymerization reactor; andpolymerizing the olefin monomer, and optionally the olefin comonomer, in the presence of the diluent to yield a second component of the solid polymer of the polymerization product in a second polymerization reactor.3. The process of claim 2 , wherein the ...

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02-10-2014 дата публикации

Catalyst Compositions for the Polymerization of Olefins

Номер: US20140296453A1
Принадлежит:

Catalyst compositions containing N,N-bis[2-hydroxidebenzyl]amine transition metal compounds are disclosed. Methods for making these transition metal compounds and for using such compounds in catalyst compositions for the polymerization of olefins also are provided. 117-. (canceled)19. The process of claim 18 , wherein the process is conducted in a batch reactor claim 18 , slurry reactor claim 18 , gas-phase reactor claim 18 , solution reactor claim 18 , high pressure reactor claim 18 , tubular reactor claim 18 , autoclave reactor claim 18 , or a combination thereof.20. The process of claim 18 , wherein the olefin monomer comprises ethylene or propylene.21. The process of claim 18 , wherein the olefin monomer comprises ethylene claim 18 , and the olefin comonomer comprises 1-butene claim 18 , 1-hexene claim 18 , 1-octene claim 18 , or a mixture thereof.22. The process of claim 18 , wherein the olefin polymer has a Mgreater than about 1 claim 18 ,000 claim 18 ,000 g/mol.23. The process of claim 18 , wherein:{'sup': 1', '2, 'sub': 1', '18, 'Xand Xindependently are a halide or a Cto Chydrocarbyl group;'}{'sup': B', 'C, 'sub': 1', '18', '1', '18, 'each Rand Rindependently is a halide, a Cto Chydrocarbyl group, or a Cto Chydrocarbylsilyl group, wherein p and q independently are 0, 1, or 2;'}{'sup': 'A', 'sub': 1', '18, 'Ris a Cto Chydrocarbyl group;'}the activator-support comprises a fluorided solid oxide, a sulfated solid oxide, or a combination thereof; andthe olefin monomer comprises ethylene or propylene.24. The process of claim 23 , wherein:the catalyst composition comprises a co-catalyst; and{'sub': 'w', 'the olefin polymer has a Min a range from about 2,000,000 to about 7,000,000 g/mol.'}25. The process of claim 23 , wherein:M is Zr or Hf;{'sup': 1', '2, 'Xand Xindependently are a halide, methyl, benzyl, or phenyl;'}{'sup': B', 'C, 'sub': 1', '5, 'each Rand Rindependently is a Cto Calkyl group;'}the process is conducted in a slurry reactor, gas-phase reactor, ...

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28-07-2016 дата публикации

UNIFIED COOLING IN MULTIPLE POLYOLEFIN POLYMERIZATION REACTORS

Номер: US20160215073A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

A system and method for a polyolefin reactor temperature control system having a first reactor temperature control path, a second reactor temperature control path, and a shared temperature control path. The shared temperature control path is configured to combine and process coolant return streams, and to provide coolant supply for the first reactor temperature control path and the second reactor temperature control path. 166-. (canceled)67. A reactor system comprising:a first polyolefin reactor configured to receive at least one feedstock, and at least one catalyst;a second polyolefin reactor configured to receive at least a portion of reactor discharge from the first polyolefin reactor; provide coolant supply to the first polyolefin reactor through a first cooler and a first bypass line disposed operationally in parallel to the first cooler;', 'provide coolant supply to the second polyolefin reactor through a second cooler and a second bypass line disposed operationally in parallel to the second cooler; and', 'receive coolant return from the first polyolefin reactor and coolant return from the second polyolefin reactor; and, 'a reactor temperature control system comprising a coolant pump configured toat least one polymer discharge on the second polyolefin reactor.68. The reactor system of claim 67 , wherein the at least one polymer discharge on the second polyolefin reactor is chosen from at least one of a continuous take-off (CTO) with a modulating valve claim 67 , a continuous take-off without a modulating valve claim 67 , a settling leg or a pulsating valve.69. The reactor system of claim 67 , wherein the polymer discharge on the second polyolefin reactor is chosen from a continuous take-off with a modulating valve or a continuous take-off with an isolation valve.70. The reactor system of claim 67 , wherein the continuous take off controls discharge of polymer product from the second reactor thereby controlling the pressure in the second reactor; andwherein the ...

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26-08-2021 дата публикации

Method of Producing Ethylene-Carboxylic Acid Compolymer

Номер: US20210261695A1
Принадлежит:

In a method of producing an ethylene-carboxylic acid copolymer, a monomer solution containing a carboxylic acid monomer is supplied from a discharging unit. The carboxylic acid monomer is copolymerized with an ethylene-based monomer. A coefficient of friction between the discharging unit and the monomer solution is maintained as 0.3 or less. 1. A method of producing an ethylene-carboxylic acid copolymer , comprising:supplying a monomer solution containing a carboxylic acid monomer from a discharging unit; andcopolymerizing the carboxylic acid monomer with an ethylene-based monomer,wherein a coefficient of friction between the discharging unit and the monomer solution is maintained as 0.3 or less.2. The method of claim 1 , wherein the coefficient of friction between the discharging unit and the monomer solution is maintained as 0.1 or less.3. The method of claim 1 , wherein the discharging unit comprises a piston and a packing unit surrounding the piston.4. The method of claim 3 , wherein the coefficient of friction between a surface of the piston and the monomer solution claim 3 , and the coefficient of friction between the packing unit and the monomer solution are all maintained as 0.3 or less.5. The method of claim 3 , wherein the piston and the packing unit each has a surface roughness (Ra) of less than 75 nm.6. The method of claim 3 , wherein the piston and the packing unit each has a surface roughness (Ra) of 2 nm or less.7. The method of claim 1 , wherein a temperature in the discharging unit is 85° C. or less.8. The method of claim 1 , wherein a temperature in the discharging unit is from 20° C. to 60° C.9. The method of claim 1 , further comprising supplying a lubricating composition into the discharging unit.10. The method of claim 9 , wherein an amount of dissolved oxygen in the lubricating composition is 10 ppm or less.11. The method of claim 9 , wherein the lubricating composition includes a base oil and a phenothiazine-based polymerization inhibitor ...

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30-08-2018 дата публикации

Methods of Relieving a Condition of Over-Pressure in a Vessel, Pressure Relief Assemblies, and Related Separator Vessels

Номер: US20180244810A1
Принадлежит:

A method and pressure relief assembly for relieving a condition of over-pressure in a vessel are provided. In addition, a separator vessel suitable for operation in a process for polymerizing one or more olefins is provided. 1. A method of relieving a condition of over-pressure in a vessel having a burst pressure and a vessel gas outlet , the method comprising:communicating in parallel a plurality of rupture discs with the vessel gas outlet;operatively pairing a first pair of rupture discs amongst the plurality of rupture discs by:providing a first rupture disc with a capacity to rupture at a predetermined lowest level of over-pressure;providing a second rupture disc with a capacity to rupture at a predetermined intermediate level of over-pressure;locating the first and second rupture discs opposite of each other symmetrically with respect to an axis of the vessel gas outlet; andoperatively pairing a second pair of rupture discs amongst the plurality of rupture discs by: locating the third and fourth discs opposite of each other symmetrically with respect to the axis;', 'whereby thrust induced moments during a relief of an over-pressurized gas from the vessel through one or more of the rupture discs are abated., 'providing a third and a fourth rupture disc with a capacity to rupture at a common predetermined higher level of over-pressure, the higher level of over-pressure being higher than the intermediate pressure and lower than the burst pressure of the vessel; and'}2. The method of claim 1 , further comprising providing the plurality of rupture discs with a common size.3. The method of claim 1 , further comprising communicating the plurality of rupture discs to a stack through a plurality of tubular bodies.4. The method of claim 3 , further comprising extending distal end portions of the plurality of tubular bodies into a base portion of the stack symmetrically with respect to the axis of the vessel gas outlet.5. The method of claim 1 , further comprising abating ...

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27-08-2020 дата публикации

CONTINUOUS AND MODULAR PROCESS FOR PRODUCING WATER-REDISPERSIBLE POLYMER POWDER COMPOSITIONS

Номер: US20200270374A1
Принадлежит:

The invention relates to a method for producing polymer powder compositions which are redispersible in water and which are based on polymerisates of one or more ethylenically unsaturated monomers. In a first step, an aqueous polymerisate dispersion is produced by means of a radically initiated polymerization of one or more ethylenically unsaturated monomers in an aqueous medium, said polymerisate dispersion being convened into the polymer powder composition which is redispersible in water by means of a diving process. The invention is characterized in that the polymerization and the drying process are each carried out in a continuous manner, and the polymerization and the diving process are carried out in separate interconnected modules. 1. A method for producing polymer powder compositions which are redispersible in water and which are based on polymers of one or more ethylenically unsaturated monomers , comprising:producing an aqueous polymer dispersion by radically initiated polymerization of one or more ethylenically unsaturated mononmers in an aqueous medium;converting the aqueous polymer dispersion to the polymer powder composition, which is redispersible in water, by a drying process, wherein the polymerization and the drying process are each carried out continuously; andconducting the polymerization and the drying process in separate interconnected modules.2. The method of claim 1 , wherein the production is effected by the emulsion polymerization process in the presence of at least one protective colloid claim 1 , optionally in combination with emulsifiers.3. The method of claim 2 , wherein claim 2 , after completion of the polymerization and prior to the drying process claim 2 , no further protective colloids are added to the aqueous polymer dispersion.4. A modular apparatus for producing polymer powder compositions which are redispersible in water in a continuous process as claimed in claim 1 , wherein the continuous process for the production of polymer ...

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05-11-2015 дата публикации

CONTINUOUS EMULSION POLYMERIZATION REACTOR AND PIGGING SYSTEM

Номер: US20150315301A1
Автор: Adams David
Принадлежит:

The invention relates to continuous polymerization apparatus comprising a tubular reactor with a continuous loop section (), a secondary line section () and a pigging system () that allows for cleaning of both sections of the reactor in a single continuous pass without manual removal of the pig. 1. A continuous emulsion polymerization apparatus comprising:a tubular reactor comprising (1) a circulating loop section and (2) a secondary line section having one end connected to a discharge opening of the loop section and a polymer outlet at its other end;one or more inlets though which a polymerizable monomer charge can be supplied to the tubular reactor;a pump for continuously circulating the monomer charge within the circulating loop section under conditions to effect polymerization thereof;a pig for cleaning the tubular reactor;a pig receiving station which accommodates the pig between cleaning operations; andflow control devices operable to connect the pig receiving station to the tubular reactor so that during a cleaning operation the pig leaves the pig receiving station and passes through and cleans both the circulating loop section and the secondary line section of the reactor.2. The polymerization apparatus according to claim 1 , wherein the pig does not pass through the pump during cleaning operations.3. The polymerization apparatus according to claim 1 , wherein the tubular reactor is in fluid communication with a suction side of the pump through an orifice in the wall of the tubular reactor.4. The polymerization apparatus according to claim 3 , wherein the size of the orifice is smaller than the size of the pig.5. The polymerization apparatus according to claim 3 , wherein the size of the orifice increases in a downstream direction of the tubular reactor.6. The polymerization apparatus according to claim 1 , wherein a discharge side of the pump is in fluid communication with the circulating loop section by way of a first flow control device and with the pig ...

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08-12-2016 дата публикации

GAS PHASE POLYMERIZATION PROCESS

Номер: US20160355613A1
Принадлежит:

An olefin polymerization process comprising polymerizing olefins in gas phase in a fluidized bed in the presence of an olefin polymerization catalyst in a polymerization reactor having a vertical body; a generally conical downwards tapering bottom zone; a generally cylindrical middle zone having a height to diameter ratio L/D of at least 4, above and connected to said bottom zone; and a generally conical upwards tapering top zone above and connected to said middle zone wherein (i) fluidization gas is introduced to the bottom zone of the reactor from where it passes upwards through the reactor; (ii) the fluidization gas is withdrawn from the top zone of the reactor, filtered, compressed, cooled and returned into the bottom zone of the reactor; (iii) a fluidized bed is formed within the reactor where the growing polymer particles are suspended in the upwards rising gas stream; and (iv) there is no fluidization grid in the reactor; characterized in that the gas velocity is maintained in the reactor such that Nis within the range of from 2.5 to 7. 2. The process according to wherein is within the range of from 2.5 to 5.3. The process according to wherein the ratio L/D is from 4 to 15.4. The process according to wherein the ratio L/D is from 5 to 10.5. The process according to comprising the step of removing polymer from the fluidization gas which has been withdrawn from the top zone of the reactor before the compression and cooling steps.6. The process according to wherein the polymer removed from the fluidization gas is recovered and passed to further processing.7. The process according to wherein the polymer removed from the fluidization gas is returned to the polymerization reactor.8. The process according to wherein polymer is withdrawn from the reactor through an outlet located in the middle zone.9. The process according to wherein the polymer is withdrawn from the reactor continuously.10. The process according to wherein polymer or polymer agglomerates are ...

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17-12-2015 дата публикации

Olefin Polymerization Process With Continuous Transfer

Номер: US20150361186A1
Принадлежит:

A process for the preparation of a polyolefin in at least two slurry loop reactors including a first loop reactor connected in series with a second loop reactor includes introducing olefin reactants, diluents and polymerization catalyst into the first loop reactor while circulating. The process includes polymerizing the olefin reactants to produce a polyolefin slurry, withdrawing the polyolefin slurry from the first loop reactor, and introducing withdrawn articles into the second loop reactor by means of settling legs. Each settling leg has an inlet connected to the first loop reactor and an outlet connected to the second loop reactor by means of a transfer line. At least one settling leg is continuously open allowing continuous transfer of solid olefin polymer particles from the first to the second loop reactor. The process includes controlling the continuous transfer of solid olefin polymer particles by the at least one continuously open settling leg. 115-. (canceled)16. A process for the preparation of a polyolefin in at least two slurry loop reactors comprising a first loop reactor connected in series with a second loop reactor , the process comprising the steps of:introducing one or more olefin reactants, diluents and polymerization catalyst into said first loop reactor, and while circulating said olefin reactants, diluents and polymerization catalyst in said first loop reactor;polymerizing said one or more olefin reactants to produce a polyolefin slurry comprising liquid diluent and solid olefin polymer particles;withdrawing polyolefin slurry comprising solid olefin polymer particles and diluent from said first loop reactor and introducing the withdrawn solid olefin polymer particles into the second loop reactor by means of one or more settling legs provided on said first loop reactor, wherein each settling leg has an inlet connected to the first loop reactor and an outlet connected to the second loop reactor by means of a transfer line;characterized in that ...

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24-12-2015 дата публикации

Heat Transfer in a Polymerization Reactor

Номер: US20150367319A1
Принадлежит:

A process comprises polymerizing an olefin monomer in a loop reactor in the presence of a catalyst and a diluent, and producing a slurry comprising solid particulate olefin polymer and diluent. The Biot number is maintained at or below about 3.0 within the loop reactor during the polymerizing process. The slurry in the loop reactor forms a slurry film having a film coefficient along an inner surface of the reactor wall, and the film coefficient is less than about 500 BTU·hr·ft·° F.. 1. A process comprising:polymerizing an olefin monomer in a loop reactor in the presence of a catalyst and a diluent; and{'sup': −1', '−2', '−1, 'producing a slurry comprising solid particulate olefin polymer and diluent, wherein the Biot number is maintained at or below about 3.0 within the loop reactor during the polymerizing, wherein the slurry in the loop reactor forms a slurry film having a film coefficient along an inner surface of a reactor wall, and wherein the film coefficient is less than about 500 BTU·hr·ft·° F..'}2. The process of claim 1 , wherein the slurry comprises a solids concentration in the range of about 25 wt % to about 70 wt %.3. The process of claim 1 , wherein the slurry comprises a solids concentration greater than about 50 wt %.4. The process of claim 1 , wherein the loop reactor comprises a reactor wall having a thickness and a thermal conductivity.5. The process of claim 4 , wherein a ratio of the film coefficient to the thermal conductivity is in a range of from about 8.0 ftto about 50 ft.6. The process of claim 4 , wherein a ratio of the film coefficient to the thickness is in a range of from about 1 claim 4 ,400 BTU·hr·ft·° F.to about 240 claim 4 ,000 BTU·hr·ft·° F..7. The process of claim 4 , wherein a ratio of the thermal conductivity to the thickness is in a range of from about 100 BTU·hr·ft·° F.to about 10 claim 4 ,000 BTU·hr·ft·° F..8. The process of claim 4 , wherein the reactor wall comprises a steel selected from the group consisting of: A106 Gr 8 ...

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03-07-2014 дата публикации

Methods for processing and interpreting signals from static and acoustic probes in fluidized bed reactor systems

Номер: WO2014106039A2

Provided is a method for operating a gas-phase, fluidized-bed reactor. The method has the steps of (a) receiving a signal from a probe in contact with the interior of the reactor or a process component in communication with the reactor, wherein the signal is derived from a physical property or condition within the reactor or the process component; (b) modifying the signal to create a modified signal; and (c) adjusting one or more operating parameters of the reactor in response to the modified signal if the physical property or condition is different than a desired value. There is also a method for reducing fouling in a distributor plate of a gas-phase, fluidized-bed reactor with a recycle line.

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03-05-2016 дата публикации

Methods for processing and interpreting signals from static and acoustic probes in fluidized bed reactor systems

Номер: US9328177B2
Принадлежит: ExxonMobil Research and Engineering Co

Provided is a method for operating a gas-phase, fluidized-bed reactor. The method has the steps of (a) receiving a signal from a probe in contact with the interior of the reactor or a process component in communication with the reactor, wherein the signal is derived from a physical property or condition within the reactor or the process component; (b) modifying the signal to create a modified signal; and (c) adjusting one or more operating parameters of the reactor in response to the modified signal if the physical property or condition is different than a desired value. There is also a method for reducing fouling in a distributor plate of a gas-phase, fluidized-bed reactor with a recycle line.

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03-05-2022 дата публикации

气相烯烃聚合方法

Номер: CN111356703B
Принадлежит: ExxonMobil Chemical Patents Inc

在生产聚烯烃聚合物,例如聚乙烯聚合物或聚丙烯聚合物的气相流化床聚合方法中,通过使含乙烯或丙烯的吹扫料流流经排气塔以接触与吹扫料流逆流流经排气塔的烃液体,减少伴随惰性气体吹扫而损失的乙烯或丙烯,于是吹扫料流部分内未反应的乙烯或丙烯溶解在烃液体中,产生富含乙烯或丙烯的液体料流和贫含乙烯或丙烯的气态料流。富含乙烯或丙烯的液体料流然后再循环到流化床反应器中,同时吹扫至少一部分贫含乙烯或丙烯的气态料流。

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14-09-2021 дата публикации

Polymerization processes

Номер: US11117980B2
Принадлежит: ExxonMobil Chemical Patents Inc

In a gas phase fluidized bed polymerization process for the production of polyolefin polymers, such as polyethylene polymers or polypropylene polymers, loss of ethylene or propylene accompanying inert gas purging is reduced by passing an ethylene- or propylene-containing purge stream through a vent column to contact a hydrocarbon liquid flowing through the vent column contercurrent to the purge stream whereby unreacted ethylene or propylene in the purge stream portion is dissolved in the hydrocarbon liquid to produce an ethylene- or propylene-enriched liquid stream and an ethylene- or propylene-depleted gaseous stream. The ethylene- or propylene-enriched liquid stream is then recycled to the fluidized bed reactor, while at least part of the ethylene- or propylene-depleted gaseous stream is purged.

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07-03-2019 дата публикации

Carbon dioxide as a catalyst quench agent in solution polymerization, and products made therefrom

Номер: WO2019045878A1
Принадлежит: ExxonMobil Chemical Patents Inc.

A method for making a polymer, having the steps of (a) polymerizing one or more monomers in the presence of a solvent and a catalyst to form a reaction product; (b) removing an effluent from the reaction product, where the effluent comprises an active catalyst and one or more unreacted monomers; (c) combining a quench, comprising carbon dioxide, with the effluent to form a quenched polymer stream, having a carboxyl metal complex; and (d) recovering a polymer from the quenched polymer stream.

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14-09-2021 дата публикации

Carbon dioxide as a catalyst quench agent in solution polymerization, and products made therefrom

Номер: US11117983B2
Принадлежит: ExxonMobil Chemical Patents Inc

A method for making a polymer, having the steps of (a) polymerizing one or more monomers in the presence of a solvent and a catalyst to form a reaction product; (b) removing an effluent from the reaction product, where the effluent comprises an active catalyst and one or more unreacted monomers; (c) combining a quench, comprising carbon dioxide, with the effluent to form a quenched polymer stream, having a carboxyl metal complex; and (d) recovering a polymer from the quenched polymer stream.

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03-11-2016 дата публикации

Homogeneous polymerization process using evaporative cooling

Номер: WO2016175962A1
Принадлежит: ExxonMobil Chemical Patents Inc.

This invention relates to a continuous homogeneous solution phase polymerization process comprising contacting, in an evaporative reactor system at a temperature of 50°C or more and a pressure of 100 kPa or more, a catalyst system, optionally, a hydrocarbon diluent, optionally, scavenger, and one or more monomer(s) to form a homogeneous polymerization medium, where the polymer product is dissolved in the reaction medium at 10 wt% or more (based upon the weight of the polymer present in the effluent at the exit of the reactor) and the catalyst system is dissolved in the reaction medium, and where the catalyst system comprises an activator and a coordination catalyst precursor compound and where all or part of the polymerization medium is evaporated during the polymerization.

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12-09-2014 дата публикации

Methods for processing and interpreting signals from static and acoustic probes in fluidized bed reactor systems

Номер: WO2014106039A3

Provided is a method for operating a gas-phase, fluidized-bed reactor. The method has the steps of (a) receiving a signal from a probe in contact with the interior of the reactor or a process component in communication with the reactor, wherein the signal is derived from a physical property or condition within the reactor or the process component; (b) modifying the signal to create a modified signal; and (c) adjusting one or more operating parameters of the reactor in response to the modified signal if the physical property or condition is different than a desired value. There is also a method for reducing fouling in a distributor plate of a gas-phase, fluidized-bed reactor with a recycle line.

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06-07-2021 дата публикации

processo de polimerização de olefinas

Номер: BR112016019209B1
Принадлежит: Borealis AG

PROCESSO DE POLIMERIZAÇÃO DE OLEFINAS. A presente invenção refere-se a um processo de polimerização de olefinas que compreende a polimerização de olefinas em fase gasosa num leito fluidizado na presença de um catalisador de polimerização de olefinas em um reator de polimerização que possui um corpo vertical; uma zona inferior geralmente cônica afunilada para baixo; uma zona média geralmente cilíndrica com uma razão da altura para o diâmetro L/D de pelo menos 4, acima e conectada à referida zona inferior; e uma zona superior geralmente cônica afunilada para cima acima e conectada à referida zona média em que (i) o gás de fluidização é introduzido à zona inferior do reator a partir de onde ele passa para cima através do reator; (ii) o gás de fluidização é retirado da zona superior do reator, filtrado, comprimido, arrefecido e devolvido para a zona inferior do reator; (iii) um leito fluidizado é formado no interior do reator em que as partículas de polímero em crescimento são suspensas no fluxo de gás ascendente; e (iv) não há nenhuma grelha de fluidização no reator; caracterizado pelo fato de que a velocidade do gás é mantida no reator de tal modo que NBr está dentro (...).

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26-01-2018 дата публикации

用于聚氯乙烯种子法糊树脂的生产装置及其生产工艺

Номер: CN105622813B
Автор: 李学斌, 汤守强, 陈淑艳

本发明涉及一种聚氯乙烯糊糊树脂的领域,特别是一种用于聚氯乙烯种子法糊树脂的生产装置及其生产工艺。制备罐分别通过管路与聚合反应釜和种子聚合反应釜的顶端连接,种子反应釜和聚合反应釜的底端分别与废水收集槽连接;种子反应釜通过种子储罐与聚合反应釜顶端连接;废水收集槽通过汽提塔与聚合反应釜连接并构成循环回路,聚合反应釜底端与卸料槽和脱除塔连接,卸料槽的出口管路与消泡机构连接,消泡机构与汽提塔的管路汇合后与气柜连接;脱除塔与干燥塔连接,干燥塔通过袋滤器与成品料仓连接。通过该装置进行的生产工艺,与现有技术相比,回收过程中无需添加化学消泡剂,污水达到连续化处理,大幅度提高生产能力,减少劳动强度,降低生产成本。

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21-11-2016 дата публикации

Apparatus for polymerizing vinyl chloride monomer and polymerization method of vinyl chloride monomer

Номер: KR101678262B1
Принадлежит: 주식회사 엘지화학

본 발명은 중합반응 후, 중합 반응기로부터 회수되는 미반응 염화비닐 단량체를 단독으로 또는 순수 염화비닐 단량체와 함께 중합 반응기로 재공급하여 염화비닐 중합체를 제조함에 있어서, 상기 미반응 염화비닐 단량체를 상기 중합 반응기로 재공급하기 전에 상기 미반응 염화비닐 단량체 중에 포함될 수 있는 비응축성 가스를 제거하는 것에 의하여 수득되는 염화비닐 중합체의 품질과 생산성을 향상시킬 수 있는 염화비닐 단량체의 중합장치 및 염화비닐 단량체의 중합방법에 관한 것으로서, 상기 장치는 염화비닐 단량체의 중합반응이 수행되는 중합 반응기와; 중합 반응기에서 회수되어 상기 중합 반응기로 재공급되는 미반응 염화비닐 단량체로부터 비응축성 가스를 제거하기 위한 분리기;를 포함함을 특징으로 한다. In the present invention, in the production of a vinyl chloride polymer by re-feeding unreacted vinyl chloride monomer recovered from a polymerization reactor alone or together with a pure vinyl chloride monomer to a polymerization reactor after the polymerization reaction, the unreacted vinyl chloride monomer is polymerized Which can improve the quality and productivity of the vinyl chloride polymer obtained by removing the non-condensable gas which can be contained in the unreacted vinyl chloride monomer before being re-supplied to the reactor, and a polymerization apparatus of a vinyl chloride monomer The apparatus comprising: a polymerization reactor in which a polymerization reaction of a vinyl chloride monomer is carried out; And a separator for removing the non-condensable gas from the unreacted vinyl chloride monomer recovered in the polymerization reactor and re-supplied to the polymerization reactor.

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03-09-1976 дата публикации

COOLING PROCESS OF A POLYMERIZATION REACTOR

Номер: FR2300096A1
Автор: [UNK]
Принадлежит: Chemische Werke Huels AG

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02-11-2016 дата публикации

Gas phase polymerization process

Номер: EP2913345B1
Принадлежит: Borealis AG

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23-05-2019 дата публикации

Gas-phase olefin polymerization process

Номер: WO2019099134A1
Принадлежит: ExxonMobil Chemical Patents Inc.

In a gas phase fluidized bed polymerization process for the production of polyolefin polymers, such as polyethylene polymers or polypropylene polymers, loss of ethylene or propylene accompanying inert gas purging is reduced by passing an ethylene- or propylene- containing purge stream through a vent column to contact a hydrocarbon liquid flowing through the vent column contercurrent to the purge stream whereby unreacted ethylene or propylene in the purge stream portion is dissolved in the hydrocarbon liquid to produce an ethylene- or propylene- enriched liquid stream and an ethylene- or propylene- depleted gaseous stream. The ethylene- or propylene- enriched liquid stream is then recycled to the fluidized bed reactor, while at least part of the ethylene- or propylene- depleted gaseous stream is purged.

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02-09-2015 дата публикации

Gas phase polymerization process

Номер: EP2913345A1
Принадлежит: Borealis AG

An olefin polymerization process comprising polymerizing olefins in gas phase in a fluidized bed in the presence of an olefin polymerization catalyst in a polymerization reactor having a vertical body; a generally conical downwards tapering bottom zone; a generally cylindrical middle zone having a height to diameter ratio L/D of at least 4, above and connected to said bottom zone; and a generally conical upwards tapering top zone above and connected to said middle zone wherein (i) fluidization gas is introduced to the bottom zone of the reactor from where it passes upwards through the reactor; (ii) the fluidization gas is withdrawn from the top zone of the reactor, filtered, compressed , cooled and returned into the bottom zone of the reactor; (iii) a fluidized bed is formed within the reactor where the growing polymer particles are suspended in the upwards rising gas stream; and (iv) there is no fluidization grid in the reactor; characterized in that the gas velocity is maintained in the reactor such that N Br is within the range of from 2.5 to 7.

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05-02-2021 дата публикации

适于烯烃共聚的物料混合方法及混合装置和烯烃共聚方法

Номер: CN108610447B

本发明涉及烯烃聚合领域,具体地,涉及一种适于烯烃共聚的物料混合方法及混合装置和烯烃共聚方法。本发明的适于烯烃共聚的物料混合方法包括:1)将第一物料与第二物料混合,得到第一混合物;2)将第三物料与第四物料混合,得到第二混合物;3)将第一混合物与第二混合物混合;任选地,在步骤2)或步骤3)引入第五物料;其中,所述第一物料和第二物料不同且选自α‑烯烃,所述第三物料为氢气,所述第四物料为有机溶剂,所述第五物料为二烯烃。通过本发明的混合方法及混合装置,能够显著改善互不相溶气体和液体的混合效果,将该方法用于乙丙橡胶共聚时,能够使氢气在混合物料中的含量保持稳定,从而显著减少聚合过程中产生的凝胶。

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30-06-2020 дата публикации

气相烯烃聚合方法

Номер: CN111356703A
Принадлежит: ExxonMobil Chemical Patents Inc

在生产聚烯烃聚合物,例如聚乙烯聚合物或聚丙烯聚合物的气相流化床聚合方法中,通过使含乙烯或丙烯的吹扫料流流经排气塔以接触与吹扫料流逆流流经排气塔的烃液体,减少伴随惰性气体吹扫而损失的乙烯或丙烯,于是吹扫料流部分内未反应的乙烯或丙烯溶解在烃液体中,产生富含乙烯或丙烯的液体料流和贫含乙烯或丙烯的气态料流。富含乙烯或丙烯的液体料流然后再循环到流化床反应器中,同时吹扫至少一部分贫含乙烯或丙烯的气态料流。

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30-05-2014 дата публикации

Polyolefin production with multiple polymerization reactors

Номер: WO2014081684A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

A polyolefin production system including: a first reactor configured to produce a first discharge slurry having a first polyolefin; a second reactor configured to produce a second discharge slurry having a second polyolefin; and a post-reactor treatment zone having at least a separation vessel configured to receive the second discharge slurry or both the first discharge slurry and the second discharge slurry.

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14-02-2018 дата публикации

Polyolefins production in multi-reactor polymerization system

Номер: RU2644897C2

FIELD: chemistry. SUBSTANCE: system comprises the first reactor configured to obtain a product leaving the first reactor and containing a first polyolefin, the second reactor configured to obtain a product leaving the second reactor and containing the second polyolefin, a post-reactor treatment zone configured to receive products, leaving the first and second reactors. The first and second reactors are arranged to allow the product leaving the first reactor to be transferred to the second reactor and, alternatively, bypassing the second reactor and feeding to the post-reactor treatment zone. The first and second polyolefins are contacted for the first time in the post-reactor treatment zone. At that, the post-reactor treatment zone contains a blowing-off column. The first and second polyolefins directed thereto come in contact for the first time there, a tank, a feeding extruder. The first and second polyolefins directed thereto come in contact for the first time in the tank, and an extruder. The first and second polyolefins directed thereto are first contacted at the extruder inlet and mixed in the extruder. EFFECT: invention provides an effective production of polyolefins, improving product quality, reducing the production costs. 11 cl, 25 dwg, 36 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 644 897 C2 (51) МПК B01J 19/24 (2006.01) C08F 2/01 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК B01J 19/24 (2017.08); C08F 2/01 (2017.08) (21)(22) Заявка: 2015118452, 19.11.2013 (24) Дата начала отсчета срока действия патента: Дата регистрации: 14.02.2018 20.11.2012 US 13/682,336 (45) Опубликовано: 14.02.2018 Бюл. № 5 (73) Патентообладатель(и): ШЕВРОН ФИЛЛИПС КЕМИКАЛ КОМПАНИ ЭлПи (US) (85) Дата начала рассмотрения заявки PCT на национальной фазе: 22.06.2015 (56) Список документов, цитированных в отчете о поиске: US 2011/0288247 А1, 24.11.2011. EP (43) Дата публикации заявки: 10.01.2017 Бюл. № 1 1564224 A1, 17.08. ...

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31-07-2014 дата публикации

Olefin polymerization process with continuous transfer

Номер: WO2014114646A1
Принадлежит: TOTAL RESEARCH & TECHNOLOGY FELUY

The present invention relates to a process for the preparation of a polyolefin in at least two slurry loop reactors comprising a first loop reactor connected in series with a second loop reactor, comprising the steps of: - introducing one or more olefin reactants, diluents and polymerization catalyst into said first loop reactor, and while circulating said olefin reactants, diluents and polymerization catalyst in said first loop reactor; - polymerizing said one or more olefin reactants to produce a polyolefin slurry comprising liquid diluent and solid olefin polymer particles; - withdrawing polyolefin slurry comprising solid olefin polymer particles and diluent from said first reactor and introducing the withdrawn particles into the second loop reactor, by means of one or more settling legs provided on said first reactor, wherein each settling leg has an inlet connected to the first reactor and an outlet connected to the second reactor by means of a transfer line, - wherein at least one settling leg is continuously open allowing continuous transfer of solid olefin polymer particles from said first loop reactor to said second loop reactor, and wherein the process further comprises the step of controlling the continuous transfer of solid olefin polymer particles from said first loop reactor to said second loop reactor by at least one continuously open settling leg.

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02-01-2018 дата публикации

具有连续输送的烯烃聚合工艺

Номер: CN104955852B
Принадлежит: Total Petrochemicals Research Feluy SA

本发明涉及在包含与第二环管反应器串联连接的第一环管反应器的至少两个淤浆环管反应器中制备聚烯烃的工艺,其包含如下步骤:‑将一种或多种烯烃反应物、稀释剂和聚合催化剂引入到所述第一环管反应器中,并且同时使所述烯烃反应物、稀释剂和聚合催化剂在所述第一环管反应器中循环;‑使所述一种或多种烯烃反应物聚合以产生包含液体稀释剂和固体烯烃聚合物颗粒的聚烯烃淤浆;‑从所述第一反应器排出包含固体烯烃聚合物颗粒和稀释剂的聚烯烃淤浆和通过设置在所述第一反应器上的一个或多个沉降腿将所排出的颗粒引入到所述第二环管反应器中,其中各沉降腿具有连接至所述第一反应器的入口和通过输送管线连接至所述第二反应器的出口,其中,至少一个沉降腿是连续打开的,容许固体烯烃聚合物颗粒从所述第一环管反应器到所述第二环管反应器的连续输送,和其中所述工艺进一步包含通过至少一个连续打开的沉降腿控制固体烯烃聚合物颗粒从所述第一环管反应器到所述第二环管反应器的连续输送的步骤。

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26-05-2020 дата публикации

OLEFINS POLYMERIZATION PROCESS WITH CONTINUOUS DISCHARGE

Номер: BR112015016302B1
Принадлежит: TOTAL RESEARCH & TECHNOLOGY FELUY

resumo “processo de polimerização de olefinas com descarga contínua” a presente invenção refere-se a um processo para a preparação de uma poliolefina em pelo menos dois reatores de circuitos fechados de suspensão que compreende um primeiro reator de circuito fechado ligado em série com um segundo reator de circuito fechado, compreendendo os passos de: - a introdução de um ou mais reagentes de olefina, diluentes e catalisador de polimerização no referido primeira reator de circuito fechado e enquanto os referidos reagentes de olefina circulam, diluentes e catalisador de polimerização no referido primeiro reator de circuito fechado; - a polimerização do referido um ou mais reagentes de olefina para produzir uma suspensão de poliolefina que compreende diluente líquido e partículas de polímero de olefina sólida; - a retirada da suspensão de poliolefina que compreende partículas de polímero de olefina sólida e diluente a partir do referido primeiro reator e a introdução das partículas retiradas para o segundo reator em circuito fechado, por meio de uma ou mais pernas de decantação proporcionada no referido primeiro reator, em que cada perna decantação tem uma entrada ligada ao primeiro reator e uma saída ligada com o segundo reator por meio de uma linha de transferência, em que pelo menos uma perna de decantação é continuamente aberta permitindo a transferência contínua de partículas de polímero de olefina sólidas a partir do referido primeiro reator de circuito fechado para o referido segundo reator de circuito fechado, e em que o processo compreende ainda o passo de controlar a transferência contínua de partículas de polímero de olefina sólidas a partir do referido primeiro reator de circuito fechado para o referido segundo reator de circuito fechado por pelo menos uma perna de decantação continuamente aberta. abstract "continuous discharge olefin polymerization process" The present invention relates to a process for preparing a polyolefin in at least two ...

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30-04-2020 дата публикации

Olefin polymerization process with continuous transfer

Номер: EA035131B1

The present invention relates to a process for the preparation of a polyolefin in at least two slurry loop reactors comprising a first loop reactor connected in series with a second loop reactor, comprising the following steps: introducing one or more olefin reactants, diluents and polymerization catalyst into said first loop reactor, and while circulating said olefin reactants, diluents and polymerization catalyst in said first loop reactor; polymerizing said one or more olefin reactants to produce a polyolefin slurry comprising liquid diluent and solid olefin polymer particles; withdrawing polyolefin slurry comprising solid olefin polymer particles and diluent from said first reactor and introducing the withdrawn particles into the second loop reactor, by means of one or more settling legs provided on said first reactor, wherein each settling leg has an inlet connected to the first reactor and an outlet connected to the second reactor by means of a transfer line, wherein at least one settling leg is continuously open allowing continuous transfer of solid olefin polymer particles from said first loop reactor to said second loop reactor, and wherein the process further comprises the step of controlling the continuous transfer of solid olefin polymer particles from said first loop reactor to said second loop reactor by at least one continuously open settling leg.

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30-09-2015 дата публикации

具有连续输送的烯烃聚合工艺

Номер: CN104955852A
Принадлежит: Total Petrochemicals Research Feluy SA

本发明涉及在包含与第二环管反应器串联连接的第一环管反应器的至少两个淤浆环管反应器中制备聚烯烃的工艺,其包含如下步骤:-将一种或多种烯烃反应物、稀释剂和聚合催化剂引入到所述第一环管反应器中,并且同时使所述烯烃反应物、稀释剂和聚合催化剂在所述第一环管反应器中循环;-使所述一种或多种烯烃反应物聚合以产生包含液体稀释剂和固体烯烃聚合物颗粒的聚烯烃淤浆;-从所述第一反应器排出包含固体烯烃聚合物颗粒和稀释剂的聚烯烃淤浆和通过设置在所述第一反应器上的一个或多个沉降腿将所排出的颗粒引入到所述第二环管反应器中,其中各沉降腿具有连接至所述第一反应器的入口和通过输送管线连接至所述第二反应器的出口,其中,至少一个沉降腿是连续打开的,容许固体烯烃聚合物颗粒从所述第一环管反应器到所述第二环管反应器的连续输送,和其中所述工艺进一步包含通过至少一个连续打开的沉降腿控制固体烯烃聚合物颗粒从所述第一环管反应器到所述第二环管反应器的连续输送的步骤。

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30-11-2015 дата публикации

POLYMERIZATION PROCESS OF OLEFINS WITH CONTINUOUS TRANSMISSION

Номер: EA201591029A1

Изобретение относится к процессу получения полиолефина по крайней мере в двух суспензионных петлевых реакторах, в которые входит первый петлевой реактор, соединенный последовательно со вторым петлевым реактором, состоящему из следующих шагов: введение одного или нескольких олефиновых реагентов, разбавителей и катализатора полимеризации в указанный первый петлевой реактор, при этом обеспечивая циркуляцию указанных олефиновых реагентов, разбавителей и катализатора полимеризации в указанном первом петлевом реакторе; полимеризирование указанных одних или нескольких олефиновых реагентов для получения полиолефиновой суспензии, в которую входит жидкий разбавитель и твердые олефиновые частицы полимера; извлечение полиолефиновой суспензии, в которую входят твердые олефиновые частицы полимера и разбавитель из указанного первого реактора; и введение извлеченных частиц во второй петлевой реактор посредством одного или нескольких осадительных стояков, установленных на указанном первом реакторе, где каждый осадительный стояк имеет вход, присоединенный к первому реактору, и выход, присоединенный ко второму реактору посредством линии передачи, где по крайней мере один осадительный стояк постоянно открыт, позволяя непрерывно передавать твердые олефиновые частицы полимера из указанного первого петлевого реактора в указанный второй петлевой реактор, и где процесс, к тому же, включает этап контролирования непрерывной передачи твердых олефиновых частиц полимера из указанного первого петлевого реактора в указанный второй петлевой реактор по крайней мере через один постоянно открытый осадительный стояк. The invention relates to a process for producing a polyolefin in at least two slurry loop reactors that include a first loop reactor connected in series with a second loop reactor consisting of the following steps: introducing one or more olefin reactants, diluents and polymerization catalyst into said first loop reactor while circulating said olefin reactants, diluents and polymerization ...

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23-09-2015 дата публикации

Olefin polymerization process with continuous transfer

Номер: EP2920214A1
Принадлежит: Total Research and Technology Feluy SA

The present invention relates to a process for the preparation of a polyolefin in at least two slurry loop reactors comprising a first loop reactor connected in series with a second loop reactor, comprising the steps of: - introducing one or more olefin reactants, diluents and polymerization catalyst into said first loop reactor, and while circulating said olefin reactants, diluents and polymerization catalyst in said first loop reactor; - polymerizing said one or more olefin reactants to produce a polyolefin slurry comprising liquid diluent and solid olefin polymer particles; - withdrawing polyolefin slurry comprising solid olefin polymer particles and diluent from said first reactor and introducing the withdrawn particles into the second loop reactor, by means of one or more settling legs provided on said first reactor, wherein each settling leg has an inlet connected to the first reactor and an outlet connected to the second reactor by means of a transfer line, - wherein at least one settling leg is continuously open allowing continuous transfer of solid olefin polymer particles from said first loop reactor to said second loop reactor, and wherein the process further comprises the step of controlling the continuous transfer of solid olefin polymer particles from said first loop reactor to said second loop reactor by at least one continuously open settling leg.

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11-07-2017 дата публикации

continuous discharge olefin polymerization process

Номер: BR112015016302A2
Принадлежит: Total Res & Technology Feluy

resumo “processo de polimerização de olefinas com descarga contínua” a presente invenção refere-se a um processo para a preparação de uma poliolefina em pelo menos dois reatores de circuitos fechados de suspensão que compreende um primeiro reator de circuito fechado ligado em série com um segundo reator de circuito fechado, compreendendo os passos de: - a introdução de um ou mais reagentes de olefina, diluentes e catalisador de polimerização no referido primeira reator de circuito fechado e enquanto os referidos reagentes de olefina circulam, diluentes e catalisador de polimerização no referido primeiro reator de circuito fechado; - a polimerização do referido um ou mais reagentes de olefina para produzir uma suspensão de poliolefina que compreende diluente líquido e partículas de polímero de olefina sólida; - a retirada da suspensão de poliolefina que compreende partículas de polímero de olefina sólida e diluente a partir do referido primeiro reator e a introdução das partículas retiradas para o segundo reator em circuito fechado, por meio de uma ou mais pernas de decantação proporcionada no referido primeiro reator, em que cada perna decantação tem uma entrada ligada ao primeiro reator e uma saída ligada com o segundo reator por meio de uma linha de transferência, em que pelo menos uma perna de decantação é continuamente aberta permitindo a transferência contínua de partículas de polímero de olefina sólidas a partir do referido primeiro reator de circuito fechado para o referido segundo reator de circuito fechado, e em que o processo compreende ainda o passo de controlar a transferência contínua de partículas de polímero de olefina sólidas a partir do referido primeiro reator de circuito fechado para o referido segundo reator de circuito fechado por pelo menos uma perna de decantação continuamente aberta. abstract "continuous discharge olefin polymerization process" The present invention relates to a process for preparing a polyolefin in at least two ...

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30-09-2015 дата публикации

Polyolefin production with multiple polymerization reactors

Номер: EP2922627A1

A polyolefin production system including: a first reactor configured to produce a first discharge slurry having a first polyolefin; a second reactor configured to produce a second discharge slurry having a second polyolefin; and a post-reactor treatment zone having at least a separation vessel configured to receive the second discharge slurry or both the first discharge slurry and the second discharge slurry.

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29-08-2011 дата публикации

Method for producing polypropylene random copolymer

Номер: KR101060012B1
Принадлежит: 주식회사 효성

본 발명은 폴리프로필렌 랜덤 공중합체의 제조방법을 제공하며, 특히 프로필렌과 공단량체로서 올레핀을 2단의 기상 연속 중합 반응기를 이용한 바이모달(bimodal) 중합 방법에 의하여 폴리프로필렌 랜덤 공중합체를 제조하는 방법을 제공한다. The present invention provides a method for preparing a polypropylene random copolymer, and in particular, a method for producing a polypropylene random copolymer by bimodal polymerization using propylene and a olefin as a comonomer in a two-stage gas phase continuous polymerization reactor. To provide. 본 발명에 따른 바이모달 방식의 기상 중합법을 사용하여 제조된 폴리프로필렌 랜덤 공중합체는 내압성, 가공성 및 충격성 등의 일반 물성이 우수하여 급수, 급탕 또는 난방용 내압 파이프를 우수한 생산성으로 제조하는데 활용될 수 있다. Polypropylene random copolymer prepared using the bimodal gas phase polymerization method according to the present invention is excellent in general physical properties such as pressure resistance, processability and impact resistance can be utilized to produce pressure-resistant pipes for water supply, hot water supply or heating with excellent productivity. have. 폴리프로필렌 랜덤 공중합체, 올레핀, 기상 반응기, 2단 중합법, 바이모달, 내압성, 내압 파이프, 가공성 Polypropylene random copolymers, olefins, gas phase reactors, two stage polymerization, bimodal, pressure resistance, pressure resistant pipes, processability

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25-07-2007 дата публикации

制备低分子量聚合物的装置和方法

Номер: CN101005890A
Принадлежит: EI Du Pont de Nemours and Co

本发明涉及一种用于进行连续聚合反应制备具有可调聚合物性能的聚合物的环流式反应器,包括包含至少两个带有插入的管节的管弯曲的三维管状回路,管弯曲的弯曲角大于30°,两个管弯曲间的距离至少为管直径的三倍,管弯曲和管节沿着与连续排列的管弯曲的弯曲方向相反的方向排列。

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15-07-2016 дата публикации

Catalyst supply device

Номер: KR101640133B1
Автор: 김신영, 김재호, 임성수
Принадлежит: 롯데케미칼 주식회사

촉매 투입장치가 개시된다. 개시된 촉매 투입장치는 촉매를 저장하는 촉매 저장부와, 촉매 저장부와 연결되게 설치되며 촉매 저장부로부터 공급되는 촉매를 배출로를 통하여 반응기에 정량으로 투입하는 촉매 계량부를 포함하는 것으로서, 촉매 계량부에 구동부를 통해 회전 가능하게 설치되며 회전 둘레방향을 따라 적어도 하나의 장착홈이 형성되어 있는 구형의 밸브 바디와, 소정 용량의 촉매를 수용하는 수용홈을 지니며 밸브 바디의 장착홈에 탈 부착 가능하게 설치되는 촉매 수용부재를 포함할 수 있다. A catalyst charging device is disclosed. The disclosed catalyst charging apparatus includes a catalyst storage unit for storing a catalyst and a catalyst metering unit connected to the catalyst storage unit and supplying a catalyst supplied from the catalyst storage unit to the reactor through a discharge path in a predetermined amount. A valve body rotatably installed through the driving unit and having at least one mounting groove formed along the circumferential direction of rotation, and a receiving groove for receiving a catalyst of a predetermined capacity, The catalyst-containing member may be a catalyst-containing member.

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23-10-2018 дата публикации

利用微反应器由丙烯酰胺制备聚丙烯酰胺的方法

Номер: CN108690155A
Автор: 商敏静, 宋扬, 苏远海
Принадлежит: Shanghai Jiaotong University

一种利用微反应器由丙烯酰胺制备聚丙烯酰胺的方法,通过将单体丙烯酰胺水溶液和引发剂水溶液分别从T型微混合器的两个不同入口端输入,混合后进入反应管道内进行聚合反应,经提纯干燥后,得到粉末状的聚丙酰胺。本方案使充分反应所需时间缩短到20min以内,反应温度为20℃~100℃,产品分散指数为3.0~4.5,数均分子量在15000~100000范围内可调,具有良好的推广前景。

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10-09-2020 дата публикации

Polymerization process

Номер: WO2020178010A1
Принадлежит: Borealis AG

The disclosure relates to a polymerization process, comprising providing a monomer stream, the monomer stream comprising an alpha-olefin monomer; providing a comonomer stream, the comonomer stream comprising at least one alpha-olefin comonomer; providing a hydrocarbon solvent stream, the hydrocarbon solvent stream comprising a hydrocarbon solvent capable of dissolving the alpha-olefin monomer and the alpha-olefin comonomer in polymerization conditions; providing an activated catalyst stream, the activated catalyst stream comprising activated polymerization catalyst; passing the monomer stream having a temperature in the range of greater than -30 °C to less than 10 °C into a polymerization reactor; passing the comonomer stream having a temperature in the range of greater than -30 °C to less than 10 °C into the polymerization reactor; passing the hydrocarbon solvent stream having a temperature in the range of greater than -30 °C to less than 10 °C into the polymerization reactor; passing the activated catalyst stream into the polymerization reactor; contacting the monomer stream, the comonomer stream, the hydrocarbon solvent stream and the activated catalyst stream in a polymerization reactor to form a reaction mixture comprising an alpha-olefin polymer; withdrawing a first product stream from the polymerization reactor, the first product stream comprising hydrocarbon solvent and alpha-olefin polymer dissolved in the hydrocarbon solvent; and a separation step for separating a second product stream and a third product stream from the first product stream, wherein the second product stream comprises majority of the alpha-olefin polymer present in the first product stream.

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16-05-2018 дата публикации

Olefin polymerization process in a gas-phase reactor comprising a riser unit and a downcomer

Номер: EP3321288A1
Принадлежит: BASELL POLYOLEFINE GMBH

A process for preparing an olefin polymer comprising polymerizing one or more olefins in a gas-phase polymerization reactor comprising a riser unit, in which growing polymer particles flow upwards under fluidization, fast fluidization or transport conditions, and a downcomer, in which growing polymer particles flow downward in a densified form, wherein the hold-up of polymer particles in the downcomer is from 55 wt.% to 80 wt.% of the total hold-up of polymer particles in the gas-phase polymerization reactor.

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09-12-2010 дата публикации

Preparation method of random copolymers of polypropylene

Номер: WO2010140745A1
Принадлежит: HYOSUNG CORPORATION

The preparation method of polypropylene random copolymer is disclosed, which is achieved by a bimodal polymerization method using a 2-stage continuous gas reactors for copolymerizing propylene and alpha olefin as comonomer. The polypropylene random copolymer prepared by using a bimodal gas polymerization according to the present invention has excellent physical properties such as pipe pressure resistance, processability and impact resistance, which leads to manufacturing excellent hot and cold water pipes and fittings.

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30-03-2021 дата публикации

Pdva油漆聚合终点判定方法

Номер: CN109632572B

本发明涉及油漆技术领域,公开了一种PDVA油漆聚合终点判定方法,包括以下步骤:步骤一:将二乙烯基乙炔与二甲苯的聚合为PDVA油漆;步骤二:对二甲苯回收塔抽真空;步骤三:将二甲苯回收塔内的PDVA油漆依次引流到缓冲槽、再沸器、二甲苯回收塔内,形成PDVA油漆的大循环,且将二甲苯回收塔内的PDVA油漆依次引流到所述再沸器、二甲苯回收塔内,形成PDVA油漆小循环;PDVA油漆大循环、小循环时,对PDVA油漆加热浓缩;步骤四:对循环管道内的PDVA油漆进行密度监测,并通过油漆密度对照表与监测到的PDVA油漆密度进行对照;步骤五:将达标的PDVA油漆排出。本发明通过质量流量计对PDVA油漆的密度进行测量,避免安全事故的发生,同时增加测量的精确性。

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08-07-2010 дата публикации

Redox-initiated cationic polymerization using vapor-state reducing agents

Номер: WO2010077606A1
Автор: James V. Crivello
Принадлежит: RENSSELAER POLYTECHNIC INSTITUTE

The novel use of a two-component redox system for cationic photopolymerization reactions is presented in which the reducing agent is delivered as a vapor to a thin film monomer sample containing the oxidizing agent. Diaryliodonium, triarylsulfonium and S,S-Dialkyl-S-phenacylsulfonium salts undergo facile reduction by silanes bearing Si-H groups in the presence of a noble metal catalyst. This redox couple can be employed as a convenient initiator system for the cationic polymerizations of epoxides, oxetanes and vinyl ethers.

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23-02-2006 дата публикации

Device and method of producing low molecular polymers

Номер: WO2006020787A1
Принадлежит: E.I. DUPONT DE NEMOURS AND COMPANY

The invention relates to a loop reactor for carrying out continuous polymerization reactions for the production of polymers with adjustable polymer properties comprising a three-dimensional tubular loop comprising at least two tube bends with interposed tube segments, the tube bends having a curving angle of greater than 30°, and the distance between two tube bends being at least three times the tube diameter, the tube bends and the tube segments being arranged in a direction reversed to the curving direction of the tube bends arranging in succession.

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