Настройки

Укажите год
-

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

Подробнее
-

Мониторинг СМИ

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

Подробнее

Форма поиска

Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
Ведите корректный номера.
Ведите корректный номера.
Ведите корректный номера.
Ведите корректный номера.
Укажите год
Укажите год

Применить Всего найдено 7126. Отображено 100.
03-05-2012 дата публикации

Polyethylene Composition and Finished Products Made Thereof

Номер: US20120108766A1
Принадлежит: BASELL POLYOLEFINE GMBH

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

Подробнее
20-09-2012 дата публикации

Process for the polymerisation of olefins

Номер: US20120238714A1
Принадлежит: Ineos Commercial Services UK Ltd

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

Подробнее
08-11-2012 дата публикации

Bimodal polyethylene for injection stretch blow moulding applications

Номер: US20120282422A1
Принадлежит: Total Petrochemicals Research Feluy SA

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

Подробнее
10-01-2013 дата публикации

Lubricant component

Номер: US20130012659A1
Автор: Joel David Citron
Принадлежит: EI Du Pont de Nemours and Co

A lubricant component is a copolymer of ethylene and α-olefins made by forming a series of α-olefins by oligomerization of ethylene using an oligomerization catalyst, and then copolymerizing the α-olefins and ethylene using a transition metalcontaining polymerization catalyst. The copolymer, which often has a high Viscosity Index, may be used, for example, in a lubricant as the base oil or a viscosity index modifier. The polyolefin may also be a component of a lubricant additive, meant to be added to an already formulated lubricant to improve the lubricant's properties.

Подробнее
27-06-2013 дата публикации

Polypropylene-based terpolymers for films

Номер: US20130165612A1
Принадлежит: Basell Poliolefine Italia Srl

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

Подробнее
04-07-2013 дата публикации

Catalyst compositions for the polymerization of olefins

Номер: US20130172497A1
Принадлежит: Chevron Phillips Chemical Co LP

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.

Подробнее
06-02-2014 дата публикации

Sealing material of polypropylene with high melting temperature

Номер: US20140039124A1
Принадлежит: Borealis AG

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

Подробнее
04-01-2018 дата публикации

RUBBER COMPOSITION COMPRISING A SPECIFIC HYDROCARBONATED RESIN

Номер: US20180001702A1
Принадлежит:

A rubber composition is based on at least one diene elastomer, a reinforcing filler, a crosslinking system and a hydrocarbon-based resin. The hydrocarbon-based resin has a number-average molecular weight (Mn) of between 700 and 1000 g/mol, an average molecular weight Mz of greater than 6000 g/mol and a polydispersity index (PI) of greater than 2.4. 115.-. (canceled)16. A rubber composition comprising at least one diene elastomer , a reinforcing filler , a crosslinking system and a hydrocarbon-based resin ,wherein said hydrocarbon-based resin has a number-average molecular weight Mn of between 700 and 1000 g/mol, an average molecular weight Mz of greater than 6000 g/mol and a polydispersity index PI of greater than 2.4.17. The rubber composition according to claim 16 , wherein the at least one diene elastomer is selected from the group consisting of essentially unsaturated diene elastomers.18. The rubber composition according to claim 16 , wherein the at least one diene elastomer is selected from the group consisting of polybutadienes claim 16 , synthetic polyisoprenes claim 16 , natural rubber claim 16 , butadiene copolymers claim 16 , isoprene copolymers and mixtures thereof.19. The rubber composition according to claim 16 , wherein a predominant diene elastomer is selected from the group consisting of polybutadienes claim 16 , copolymers of butadiene and styrene claim 16 , and natural rubber.20. The rubber composition according to claim 16 , wherein the reinforcing filler is selected from the group consisting of silicas claim 16 , carbon blacks and mixtures thereof.21. The rubber composition according to claim 16 , wherein a content of reinforcing filler is within a range extending from 5 to 200 phr.22. The rubber composition according to claim 21 , wherein the content of reinforcing filler is within a range extending from 40 to 160 phr.23. The rubber composition according to claim 16 , wherein a content of the hydrocarbon-based resin is within a range extending ...

Подробнее
03-01-2019 дата публикации

Process for Preparing a Polyethylene in at Least One Continuously Stirred Tank Reactor

Номер: US20190002603A1
Принадлежит:

Processes for preparing a polyethylene in at least one continuously stirred tank reactor are described herein. The process may comprise the step of: polymerizing ethylene in the presence of at least one supported metallocene catalyst, a diluent, optionally one or more co-monomers, and optionally hydrogen, thereby obtaining the polyethylene, wherein the supported metallocene catalyst comprises a solid support, a co-catalyst and at least one metallocene, wherein the solid support has a surface area within the range of from 100 to 500 m2/g, and has a D50 value within the range of from 4 μm to 18 μm, with D50 being defined as the particle size for which fifty percent by weight of the particles has a size lower than the D50; and D50 being measured by laser diffraction analysis on a Malvern type analyzer. Polyethylene obtained by the disclosed process and articles comprising the polyethylene are also described. 115.-. (canceled)16. An article comprising a polyethylene resin prepared by a process in at least one continuously stirred tank reactor , the process comprising:polymerizing ethylene in the presence of at least one supported metallocene catalyst, a diluent, optionally one or more co-monomers, and optionally hydrogen, thereby obtaining the polyethylene resin,{'sup': '2', 'wherein the supported metallocene catalyst comprises a solid support, a co-catalyst and at least one metallocene, wherein the solid support has a surface area within the range of from 100 to 350 m/g, and has a D50 value within the range of from 4 μm to 18 μm, with D50 being defined as the particle size for which fifty percent by weight of the particles has a size lower than the D50; and D50 being measured by laser diffraction analysis on a Malvern type analyzer.'}17. The article according to claim 16 , wherein the polyethylene resin at the end of the process has a D50 of at least 100 and at most 400 μm; and Si content lower than 60 ppm by weight.18. The article according to claim 16 , wherein the ...

Подробнее
03-01-2019 дата публикации

METHODS FOR DYEING ULTRA-HIGH MOLECULAR WEIGHT POLYETHYLENE AND DYED ARTICLES MADE BY THE SAME

Номер: US20190002649A1
Принадлежит:

Dyed articles, such as sutures, and methods for making the same by treating with a supercritical liquid are disclosed. The articles may be made at least partially, if not entirely, from ultra-high molecular weight polyethylene (UHMWPE). The dye may be D&C Violet #2. 1. A method of dyeing an article comprising an ultra-high molecular weight polyethylene (UHMWPE) , comprising contacting the article with a supercritical liquid and D&C Violet #2.2. The method of claim 1 , further comprising applying a pressure from about 3 claim 1 ,600 psi to about 3 claim 1 ,800 psi.3. The method of claim 1 , further comprising applying a temperature from about 110° C. to about 130° C.4. The method of claim 3 , wherein the temperature is maintained for about 90 to about 180 minutes.5. The method of claim 4 , wherein the dyed article has a color contrast of at least about 90%.6. The method of claim 1 , wherein the article is a suture.7. A dyed article made by the process of . This application claims the benefit of U.S. Provisional Application No. 62/275,268, filed on Jan. 6, 2016, the entire contents of which are incorporated by reference herein in entirety.The invention relates to a process for dyeing an article comprising an ultra-high weight polyethylene, with D&C Violet #2. A supercritical liquid is applied to the article with the dye at a specified temperature and pressure to yield the desired dyed article.In a process known in the art, highly oriented ultra-high molecular weight polyethylene fibers are contacted with a dye bath at a temperature of 100-130° C. for 20-60 minutes, with the dye bath consisting of an aqueous dispersion of a finely ground mixture of specific dyes and surfactants whereupon the moulded article is washed and dried. For good dyeing results the fibers are preferably modified by means of a plasma or corona treatment prior to the dyeing operation. An important drawback of the known process is that the dyed fibers, particularly if they are not first modified by ...

Подробнее
03-01-2019 дата публикации

ELASTOMER MATERIAL FOR MEDICAL DEVICES AND ELASTOMER MOLDED BODY FOR MEDICAL DEVICES

Номер: US20190002682A1
Автор: TOMIZUKA Kazuhito
Принадлежит: OLYMPUS CORPORATION

This elastomer material for medical devices contains: a first fluorine-based elastomer that is a ternary copolymer comprising three kinds of monomers A, B and C; and a second fluorine-based elastomer that is a ternary copolymer comprising the monomers A and B and a monomer D which is different from any one of the monomers A, B and C. The monomer C and the monomer D have side chains that have structures different from each other. 1. An elastomer material for medical devices comprising:a first fluorine-based elastomer which is a ternary copolymer having three kinds of monomers A, B and C; anda second fluorine-based elastomer which is a ternary copolymer having the monomers A and B and a monomer D different from any one of the monomers A, B and C,wherein the monomer A is vinylidene fluoride, the monomer B is tetrafluoroethylene, the monomer C is hexafluoropropylene, and the monomer D is perfluoroalkyl vinyl ether.2. The elastomer material for medical devices according to claim 1 , wherein claim 1 ,when total content of the first fluorine-based elastomer and the second fluorine-based elastomer is 100 parts by weight, a crosslinking aid is contained in an amount of not more than 15 parts by weight and not zero.3. The elastomer material for medical devices according to claim 1 , wherein claim 1 ,when total content of the first fluorine-based elastomer and the second fluorine-based elastomer is 100 parts by weight, a filler is contained in an amount of not more than 50 parts by weight and not zero.4. The elastomer material for medical devices according to claim 1 , wherein claim 1 ,when total content of the first fluorine-based elastomer and the second fluorine-based elastomer is 100 parts by weight, a third fluorine-based elastomer whose number average molecular weight is 5000 or less and having no crosslinking reactive group is contained in an amount of not more than 50 parts by weight and not zero.5. An elastomer molded body for medical devices comprising:a first ...

Подробнее
05-01-2017 дата публикации

SEMICONDUCTOR ELEMENT AND INSULATING LAYER-FORMING COMPOSITION

Номер: US20170005266A1
Принадлежит: FUJIFILM Corporation

Provided is a semiconductor element having a semiconductor layer and an insulating layer adjacent to the semiconductor layer, in which the insulating layer is formed of a crosslinked product of a polymer compound having a repeating unit (IA) represented by the following General Formula (IA) and a repeating unit (IB) represented by the following General Formula (IB). 2. The semiconductor element according to claim 1 , wherein Lis represented by the following Formula (1a) claim 1 ,{'br': None, 'sup': 1a', '3a, '*-Ar-L** \u2003\u2003Formula (1a)'}{'sup': 3a', '1a', '1a', '2a, 'in Formula (1a), Lrepresents a single bond or a linking group, Arrepresents an aromatic ring, * indicates the bonding position of the carbon atom to which Rin the repeating unit (IA) is bonded, and ** indicates the bonding position of Lin the repeating unit (IA).'}3. The semiconductor element according to claim 2 , wherein Aris a benzene ring.6. The semiconductor element according to claim 1 , wherein the crosslinkable group X is an epoxy group claim 1 , an oxetanyl group claim 1 , a hydroxymethyl group claim 1 , an alkoxymethyl group claim 1 , a (meth)acryloyloxy group claim 1 , a styryl group claim 1 , or a vinyl group.7. The semiconductor element according to claim 1 , wherein the crosslinkable group X is a hydroxymethyl group or an alkoxymethyl group.8. The semiconductor element according to claim 1 , wherein the crosslinked product is a crosslinked product by a crosslinking reaction between the crosslinkable group X of the repeating unit (IA) and the repeating unit (IB).9. The semiconductor element according to claim 8 , wherein the crosslinked product has a crosslinked portion where a hydroxymethyl group or an alkoxymethyl group as a crosslinkable group is formed by a reaction.10. The semiconductor element according to claim 1 , wherein the semiconductor layer contains an organic semiconductor. This application is a Continuation of PCT International Application No. PCT/JP2015/058775 filed ...

Подробнее
02-01-2020 дата публикации

EDDER COMPOUND AND CAPACITOR THEREOF

Номер: US20200006000A1
Принадлежит:

A metadielectric composite oligomeric organic material according to the formula: 3. The metadielectric composite oligomeric organic material of wherein all resistive insulating groups are selected independently from the group consisting of non-aromatic carbocycles and non-aromatic heterocycles.4. The metadielectric composite oligomeric organic material of wherein each instance of A is independently selected from —NO claim 1 , —CHO (aldehyde) claim 1 , —CRO (keto group) claim 1 , —SOH (sulfonic acids) claim 1 , —SOR (sulfonates) claim 1 , SONH claim 1 , —SONHR claim 1 , —SONR′R″ (sulfonamides) claim 1 , —COOH (carboxylic acid) claim 1 , —COOR (esters claim 1 , from carboxylic acid side) claim 1 , —CONH claim 1 , CONHR claim 1 , CONR′R″ (amides claim 1 , from carboxylic acid side) claim 1 , —CF claim 1 , —CCl claim 1 , and —CN claim 1 , and{'sub': 2', '2', '6', '5, 'wherein each instance of D is independently selected from —NH, —NHR, —NR, —OH, OR (ethers), —NHCOR (amides, from amine side), —OCOR (esters, from alcohol side), alkyls, —CH, and vinyls, and'}wherein R and R′ and R″ are radicals independently selected from the list comprising hydrogen, alkyl (methyl, ethyl, isopropyl, tert-butyl, neopentyl, cyclohexyl etc.), allyl (˜CH2-CH═CH2), benzyl (—CH2C6H5) groups, phenyl (+substituted phenyl) and other aryl (aromatic) groups.6. The composite oligomeric organic material of wherein the insulating resistive groups are independently selected from the group consisting of saturated hydrocarbon claim 1 , saturated halogenated hydrocarbon claim 1 , partially halogenated hydrocarbon claim 1 , aryl chain claim 1 , and cycloalkyl claim 1 , and X—RR′R″; wherein X is selected from C claim 1 , O claim 1 , N claim 1 , and S claim 1 , and R claim 1 , R′ claim 1 , and R″ claim 1 , wherein R′ and R″ are absent when necessitated by the valence of X claim 1 , are independently selected from H and C claim 1 , wherein one or more of R claim 1 , R′ claim 1 , and R″ is C.7. The composite ...

Подробнее
11-01-2018 дата публикации

CATALYST SYSTEMS FOR OLEFIN POLYMERIZATION

Номер: US20180009958A1
Принадлежит: Dow Global Technologies LLC

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

Подробнее
11-01-2018 дата публикации

INK COMPOSITION INCLUDING A MODIFIED POLYMER OR COPOLYMER ADDITIVE

Номер: US20180010003A1
Принадлежит:

An ink composition includes water, a co-solvent, a colorant, and a modified polymer or copolymer additive. The modified polymer or copolymer additive is selected from the group consisting of i) a hydrolyzed poly(isobutylene-alt-maleic anhydride), ii) a hydrolyzed poly(maleic anhydride-alt-1-octadecene), and iii) a modified polymer or copolymer. The modified polymer or copolymer includes a repeating unit of a backbone chain, and a long chain pendant group attached to a carbon atom of the repeating unit. In the backbone chain, the long chain pendant group of the repeating unit is separated by fewer than 8 spacer carbon atoms from another long chain pendant group of an adjacent repeating unit. 1. An ink composition , comprising:water;a co-solvent;a colorant; and i) a hydrolyzed poly(isobutylene-alt-maleic anhydride);', 'ii) a hydrolyzed poly(maleic anhydride-alt-1-octadecene); and', a repeating unit of a backbone chain; and', 'a long chain pendant group attached to a carbon atom of the repeating unit;', 'wherein in the backbone chain, the long chain pendant group of the repeating unit is separated by fewer than 8 spacer carbon atoms from an other long chain pendant group of an adjacent repeating unit., 'iii) a modified polymer or copolymer including], 'a modified polymer or copolymer additive selected from the group consisting of2. The ink composition as defined in wherein the long chain pendant group includes an ethylene oxide group claim 1 , and wherein a ratio of a number of linear atoms in the long chain pendant group to spacer carbon atoms between equivalent chemical sites in the backbone chain is at least 25:3.3. The ink composition as defined in wherein the repeating unit is formed from a monomer or comonomer selected from the group consisting of maleic anhydride claim 1 , an acrylic monomer or comonomer claim 1 , a methacrylic monomer or comonomer claim 1 , an amine monomer or comonomer claim 1 , a vinyl alcohol monomer or comonomer claim 1 , an allyl alcohol ...

Подробнее
11-01-2018 дата публикации

ADHESIVE COMPOSITION

Номер: US20180010023A1
Принадлежит:

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

Подробнее
10-01-2019 дата публикации

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

Номер: US20190010256A1
Принадлежит:

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

Подробнее
10-01-2019 дата публикации

Ethylene based polymer composition suitable for use in extrusion coating

Номер: US20190010262A1
Принадлежит: SABIC Global Technologies BV

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

Подробнее
10-01-2019 дата публикации

PHOTOACTIVATABLE FOULING-RESISTANT COPOLYMERS

Номер: US20190010268A1
Принадлежит: Arrow International, Inc.

A photoactivatable fouling-resistant copolymer composed of a photoactivatable monomer and a hydrophilic monomer is disclosed. The photoactivatable monomer includes an aryl ketone derivative having one or more polar groups or alkyl groups. 156-. (canceled)57. A photoactivatable fouling-resistant copolymer comprising:(a) a photoactivatable monomer including an aryl ketone derivative having one or more polar groups or alkyl groups, and(b) a hydrophilic monomer.59. The copolymer of claim 57 , wherein the photoactivatable monomer is present in an amount of 0.1 to 70% by weight based on the total weight of the copolymer.60. The copolymer of claim 57 , wherein the hydrophilic monomer is present in an amount of 30 to 99.9% by weight based on the total weight of the copolymer.61. The copolymer of claim 57 , wherein the photoactivatable monomer comprises the one or more polar groups or alkyl groups.62. The copolymer of claim 57 , wherein the polar group of the photoactivatable monomer comprises at least one of carboxylic acid claim 57 , a sulfonate group claim 57 , a nitro group claim 57 , a hydroxyl claim 57 , carboxy claim 57 , amino claim 57 , amide claim 57 , phosphate or ether group.63. The copolymer of claim 57 , wherein the alkyl group of the photoactivatable monomer or the hydrophilic monomer comprises at least one of a methyl claim 57 , ethyl claim 57 , or propyl group.64. The copolymer of claim 57 , wherein the copolymer has a weight average molecular weight ranging from 5 claim 57 ,000 to 200 claim 57 ,000.65. The copolymer of claim 57 , wherein the photoactivatable monomer comprises at least one unsaturated group.66. The copolymer of claim 57 , wherein the hydrophilic monomer comprises at least one unsaturated group.67. The copolymer of claim 65 , wherein the unsaturated group is a methacrylate claim 65 , acrylate claim 65 , acrylamide claim 65 , vinyl group or mixtures thereof.69. The copolymer of claim 57 , wherein the hydrophilic monomer is a sulfobetaine ...

Подробнее
10-01-2019 дата публикации

Resin composition and application thereof

Номер: US20190010321A1
Принадлежит: Chi Mei Corp

A resin composition and an application thereof are provided, wherein the resin composition includes a thermoplastic elastomer, a styrene-based resin, a processing oil, and a filler. Based on 100 wt % of the resin composition, the content of the thermoplastic elastomer is 20 wt % to 55 wt %, the content of the styrene-based resin is 25 wt % to 55 wt %, the content of the processing oil is 6 wt % to 18 wt %, and the content of the filler is 5 wt % to 20 wt %. A printing material made by the resin composition has good adhesion with a substrate.

Подробнее
10-01-2019 дата публикации

POLYESTER RESIN COMPOSITION AND METHOD FOR PRODUCING SAME

Номер: US20190010325A1

Provided are: a polyester resin composition that exhibits excellent flame retardancy and melt thermal stability and also exhibits excellent laser markability; and a method for producing same. The present invention provides: a polyester resin composition containing 3 to 60 parts by mass of a brominated polyacrylate flame retardant (B) relative to 100 parts by mass of a thermoplastic polyester resin (A), this brominated polyacrylate flame retardant (B) having a Na element concentration of 5 to 4000 ppm, as measured by X-Ray fluorescence analysis; and a production method including washing the brominated polyacrylate flame retardant (B) with hot water having a temperature of 40° C. to 100° C., then drying the washed product, and then mixing the dried product with the thermoplastic polyester resin (A). 1. A polyester resin composition , comprising:(A) 100 parts by mass of a thermoplastic polyester resin (A); and(B) 3 to 60 parts by mass of a brominated polyacrylate flame retardant (B), relative to the 100 parts by mass of the thermoplastic polyester resin (A),wherein the brominated polyacrylate flame retardant (B) has a Na element concentration of 5 to 4000 ppm, as measured by X-Ray fluorescence analysis.2. The polyester resin composition according to claim 1 , wherein the brominated polyacrylate flame retardant (B) has a Na element concentration of 100 to 1500 ppm.3. The polyester resin composition according to claim 1 , wherein the brominated polyacrylate flame retardant (B) has a Mg ion concentration of 5 to 2000 ppm and an Al ion concentration of 5 to 3000 ppm claim 1 , as measured by TCP emission spectrometry.4. The polyester resin composition according to claim 1 , wherein the brominated polyacrylate flame retardant (B) is a pentabromobenzyl polyacrylate.5. The polyester resin composition according to claim 1 , wherein the brominated polyacrylate flame retardant (B) contains sodium bromide.6. The polyester resin composition according to claim 1 , further comprising ...

Подробнее
09-01-2020 дата публикации

Polymer Compositions With PBSA Plasticizer

Номер: US20200010628A1
Принадлежит: Danimer Bioplastics, Inc.

A polymeric composition is disclosed which includes from about 40 to about 99 weight percent of a first polymer and from about 1 to about 60 weight percent of polybutylene(succinate-co-adipate) (“PBSA”). Preferably the first polymer is selected from the group consisting of polyvinyl chloride, polylactic acid, polyhydroxy alkanoates, and mixtures thereof. A method for making the composition is also disclosed. 1. A polymeric composition comprising:from about 40 to about 99 weight percent of a first polymer which comprises polyhydroxy alkanoates; andfrom about 1 to about 60 weight percent of polybutylene(succinate-co-adipate) (“PBSA”).2. (canceled)3. The polymeric composition of claim 1 , wherein the PBSA has a weight average molecular weight from about 50 claim 1 ,000 to about 200 claim 1 ,000.4. The polymeric composition of claim 1 , wherein the PBSA has a weight average molecular weight from about 80 claim 1 ,000 to about 120 claim 1 ,000.5. The polymeric composition of claim 1 , wherein the PBSA has a viscosity from about 15 claim 1 ,000 to about 40 claim 1 ,000 centipoise at a temperature of about 215° C.6. The polymeric composition of claim 1 , wherein the PBSA has a melting point from about 20° C. to about 75° C.7. The polymeric composition of claim 1 , wherein the PBSA has a melting point from about 25° C. to about 40° C.8. The polymeric composition of claim 1 , wherein the PBSA comprises:from about 40 to about 60 mole percent moieties derived from 1,4-butanediol,from about 10 to about 50 mole percent moieties derived from succinic acid, andfrom about 10 to about 50 mole percent moieties derived from adipic acid.9. The polymeric composition of claim 1 , wherein the composition comprises from about 1 to about 10 weight percent of the PBSA.10. The polymeric composition of claim 1 , wherein the composition comprises from about 50 to about 60 weight percent of the PBSA.11. The polymeric composition of claim 1 , wherein the composition further comprises at least one ...

Подробнее
19-01-2017 дата публикации

Modified conjugated diene-based polymer, preparation method therefor, and rubber composition containing same

Номер: US20170015761A1
Принадлежит: LG Chem Ltd

Disclosed are a modified conjugated diene-based polymer represented by specific Chemical Formula, a method of preparing the same, and a rubber composition including the same.

Подробнее
19-01-2017 дата публикации

Process control for long chain branching control in polyethylene production

Номер: US20170015768A1
Принадлежит: Univation Technologies Llc

Polymerization process control methods for making polyethylene are provided. The process control methods include performing a polymerization reaction in a polymerization reactor to produce the polyethylene, where ethylene, and optionally one or more comonomers, in the polymerization reaction is catalyzed by an electron donor-free Ziegler-Natta catalyst and an alkyl aluminum co-catalyst. A melt flow ratio (I 21 /I 2 ) of the polyethylene removed from the polymerization reactor is measured and an amount of long chain branching (LCB) of the polyethylene from the polymerization reactor is controlled by adjusting a weight concentration of the alkyl aluminum co-catalyst present in the polymerization reactor. In addition, an electron donor-free Ziegler-Natta catalyst productivity of the polyethylene being produced in the polymerization reactor is measured from which the amount of LCB of the polyethylene from the polymerization reactor is determined using the measured electron donor-free Ziegler-Natta catalyst productivity and a predetermined relationship between the electron donor-free Ziegler-Natta catalyst productivity and the LCB.

Подробнее
18-01-2018 дата публикации

POLYOLEFIN FOR PREPARING FIBER AND FIBER COMPRISING THE SAME (As Amended)

Номер: US20180016370A1
Принадлежит:

The present invention relates to polyolefin powder for preparing fiber, and fiber comprising the same. According to the present invention, provided is polyolefin, which exhibits a high molecular weight range and narrow molecular weight distribution and in which the formation of a gel deteriorating the quality of fiber is reduced. Therefore, by using the polyolefin, the present invention exhibits molecular weight, density and narrow molecular weight distribution, which are equivalent to those of conventional polyolefin, but the number of gels having a large particle diameter is remarkably reduced, and therefore, the present invention can provide fiber having excellent tenacity and tensile strength half-life. 1. Polyolefin powder for preparing fiber:wherein a weight average molecular weight is 100,000 to 300,000 g/mol;wherein a molecular weight distribution is 2.0 to 3.2; and{'sup': '2', 'when the polyolefin powder is manufactured into a casting film at 190° C., the number of gels with a particle diameter of 250 μl or more is less than 2,000 per unit area (m).'}2. The polyolefin powder according to claim 1 , wherein a melt index (MI:190° C. claim 1 , 2.16 kg) is 0.1 to 2.0 g/10 min.3. The polyolefin powder according to claim 1 , wherein a density is 0.945 to 0.955 g/cm.4. The polyolefin powder according to claim 1 , wherein the polyolefin powder is prepared by the polymerization of olefin monomers in the presence of a single metallocene supported catalyst.5. A fiber comprising the polyolefin powder of .6. The fiber according to claim 5 , wherein a tenacity measured according to ASTM D 638 is 13 to 20 gf/denier.7. The fiber according to claim 5 , wherein a tensile strength half-life measured for UV by AATCC method #16 claim 5 , after measuring tensile strength according to ASTM D 638 claim 5 , is 250 to 350 hours.8. The fiber according to claim 5 , wherein the fiber is used as monofilament or multifilament products. This application claims the benefit of Korean Patent ...

Подробнее
18-01-2018 дата публикации

LOW DENSITY POLYETHYLENE COPOLYMER HAVING EXCELLENT FILM PROCESSABILITY AND TRANSPARENCY

Номер: US20180016372A1
Принадлежит: LG CHEM, LTD.

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

17-01-2019 дата публикации

TIRE UNDERTREAD

Номер: US20190016178A1
Принадлежит:

Rubber compositions that are particularly suitable for the undertread for a tire tread, such rubber compositions including a functionalized polybutadiene rubber and a second rubber component such as a styrene butadiene copolymer, natural rubber, another polybutadiene or other diene rubber or combinations thereof. Such rubber compositions are reinforced with a carbon black reinforcing filler that may be characterized as a low-surface area, high structure carbon black having a nitrogen surface area of between 15 m/g and 25 m/g and a COAN of between 65 ml/100 g and 85 ml/100 g. 1. A tread for a tire that comprises an undertread , the undertread formed from a rubber composition that is based upon a cross-linkable rubber composition , the cross-linkable composition comprising , per 100 parts by weight of rubber (phr):at least 20 phr of a functionalized polybutadiene rubber having a functional group that is capable of interacting with carbon black;between 0 phr and 80 phr of a second rubber component;{'sup': 2', '2, 'a low-surface area, high structure carbon black having a nitrogen surface area of between 15 m/g and 25 m/g and a COAN of between 65 ml/100 g and 85 ml/100 g; and'}a curing system.2. The tread of claim 1 , wherein the functionalized polybutadiene rubber is a tin coupled end-functionalized polybutadiene rubber.3. The tread of claim 2 , wherein the polybutadiene rubber is end-functionalized with an amine group.4. The tread of claim 1 , wherein the cross-linkable rubber composition comprises between 40 phr and 80 phr of the carbon black.5. The tread of claim 1 , wherein an OAN of the carbon black is between 100 ml/100 g and 150 ml/100 g.6. The tread of claim 5 , wherein an iodine number of the carbon black is between 10 mg/g and 25 mg/g.7. The tread of claim 6 , wherein the cross-linkable rubber composition comprises between 40 phr and 60 phr of the functionalized polybutadiene rubber.8. The tread of claim 1 , wherein the second rubber component is selected from ...

Подробнее
17-01-2019 дата публикации

GAS PHASE POLYMERISATION OF ETHYLENE

Номер: US20190016831A1
Принадлежит:

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

Подробнее
17-01-2019 дата публикации

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

Номер: US20190016832A1
Принадлежит: Braskem America, Inc.

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

Подробнее
17-01-2019 дата публикации

Process control for long chain branching control in polyethylene production

Номер: US20190016835A1
Принадлежит: Univation Technologies Llc

Polymerization process control methods for making polyethylene are provided. The process control methods include performing a polymerization reaction in a polymerization reactor to produce the polyethylene, where ethylene, and optionally one or more comonomers, in the polymerization reaction is catalyzed by an electron donor-free Ziegler-Natta catalyst and an alkyl aluminum co-catalyst. A melt flow ratio (I 21 /I 2 ) of the polyethylene removed from the polymerization reactor is measured and an amount of long chain branching (LCB) of the polyethylene from the polymerization reactor is controlled by adjusting a weight concentration of the alkyl aluminum co-catalyst present in the polymerization reactor. In addition, an electron donor-free Ziegler-Natta catalyst productivity of the polyethylene being produced in the polymerization reactor is measured from which the amount of LCB of the polyethylene from the polymerization reactor is determined using the measured electron donor-free Ziegler-Natta catalyst productivity and a predetermined relationship between the electron donor-free Ziegler-Nana catalyst productivity and the LCB.

Подробнее
24-01-2019 дата публикации

POLYOLEFIN ELASTOMER COMPOSITIONS AND METHODS OF MAKING THE SAME

Номер: US20190021441A1
Принадлежит: COOPER-STANDARD AUTOMOTIVE INC.

An elastomeric article is provided that includes a composition having a silane-crosslinked polyolefin elastomer with a density less than 0.90 g/cm. The elastomeric article can exhibit a compression set of from about 5.0% to about 35.0%, as measured according to ASTM D 395 (22 hrs @ 70° C.). The silane-crosslinked polyolefin elastomer can include a first polyolefin having a density less than 0.86 g/cm, a second polyolefin having a crystallinity less than 40%, a silane crosslinker, a grafting initiator, and a condensation catalyst. 1. A silane-crosslinked polyolefin elastomer blend comprising:{'sup': '3', 'a first polyolefin having a density less than 0.86 g/cm;'}a second polyolefin having a percent crystallinity less than 40%;a silane crosslinker,{'sup': '3', 'wherein the silane-crosslinked polyolefin elastomer blend exhibits a compression set of from about 5.0% to about 35.0%, as measured according to ASTM D 395 (22 hrs @ 70° C.) and wherein the silane-crosslinked polyolefin elastomer blend has a density less than 0.90 g/cm.'}2. The silane-crosslinked polyolefin elastomer blend of further comprising a microencapsulated foaming agent.3. The silane-crosslinked polyolefin elastomer blend of claim 1 , wherein the density is less than 0.70 g/cm.4. The silane-crosslinked polyolefin elastomer blend of further comprising a foaming agent.5. The silane-crosslinked polyolefin elastomer blend of claim 1 , wherein the density is less than 0.60 g/cm.6. The silane-crosslinked polyolefin elastomer blend of claim 1 , wherein the compression set is from about 15.0% to about 35.0% claim 1 , as measured according to ASTM D 395 (22 hrs @ 70° C.).7. The silane-crosslinked polyolefin elastomer blend of claim 1 , wherein the first polyolefin comprises an ethylene-octene copolymer from about 60 wt % to about 97 wt %.8. The silane-crosslinked polyolefin elastomer blend of claim 1 , wherein the second polyolefin comprises a polypropylene homopolymer from about 10 wt % to about 35 wt % and/or ...

Подробнее
26-01-2017 дата публикации

AMINOSILANE TERMINAL MODIFIER TO WHICH FUNCTIONAL GROUP HAS BEEN INTRODUCED, METHOD FOR PRODUCING TERMINAL-MODIFIED CONJUGATED DIENE POLYMER USING THE AMINOSILANE TERMINAL MODIFIER, AND TERMINAL-MODIFIED CONJUGATED DIENE POLYMER

Номер: US20170022297A1
Принадлежит: LG CHEM, LTD.

Disclosed are an end-modified conjugated diene-based polymer configured such that the end of a conjugated diene-based polymer is coupled with an aminosilane-based end modifier, and a method of preparing the same. 3. The end-modified conjugated diene-based polymer of claim 1 , wherein the end-modified conjugated diene-based polymer has a number average molecular weight (Mn) of 1 claim 1 ,000 to 2 claim 1 ,000 claim 1 ,000 g/mol.4. The end-modified conjugated diene-based polymer of claim 1 , wherein the end-modified conjugated diene-based polymer comprises 1 to 60 wt % of an aromatic vinyl monomer based on 100 wt % in total of a conjugated diene monomer and the aromatic vinyl monomer.7. The method of claim 5 , wherein the organometallic compound is used in an amount of 0.01 to 10 mmol based on 100 g in total of the monomer.8. The method of claim 5 , wherein a molar ratio of the organometallic compound and the compound represented by Chemical Formula 1 ranges from 1:0.1 to 1:10.9. The method of claim 5 , wherein the polymerizing in a) is performed with additional use of a polar additive.10. The method of claim 9 , wherein the polar additive is added in an amount of 0.001 to 10 g based on 1 mmol in total of the organometallic compound. This application claims the benefit of Korean Patent Application Nos. KR 10-2014-0186008, filed Dec. 22, 2014, and KR 10-2015-0104520, filed Jul. 23, 2015, which are hereby incorporated by reference in their entirety into this application.The present invention relates to a functionalized aminosilane-based end modifier, a method of preparing an end-modified conjugated diene-based polymer using the same, and an end-modified conjugated diene-based polymer prepared thereby.Recently, in the vehicle industry, the demand for the durability, stability and fuel economy of vehicles is continuously increasing, and much effort is directed to satisfying the demand.In particular, many attempts have been made to enhance the properties of rubber, as a ...

Подробнее
26-01-2017 дата публикации

Process for Forming Polyolefins

Номер: US20170022307A1
Принадлежит: Chevron Phillips Chemical Co LP

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

Подробнее
26-01-2017 дата публикации

Propylene-Based Impact Copolymers

Номер: US20170022308A1
Принадлежит:

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

Подробнее
25-01-2018 дата публикации

Modified liquid diene rubber and resin composition containing modified liquid diene rubber

Номер: US20180022835A1
Автор: Kei Hirata, Satoshi Motoda
Принадлежит: Kuraray Co Ltd

There are provided a modified liquid diene rubber that can be used for a curable resin composition and a resin composition containing the modified liquid diene rubber. The curable resin composition containing the modified liquid diene rubber has a much higher curing rate than that in the related art, and the resulting cured product has excellent mechanical properties, transparency, and heat resistance. Produced are a modified liquid diene rubber and a resin composition containing the modified liquid diene rubber. The modified liquid diene rubber includes a modifying group (p) partly containing a (meth)acryloyl group therein and a monomer unit (a1) derived from a conjugated diene compound. A carbon-carbon double bond derived from the conjugated diene compound has a hydrogenation rate of 30 to 95 mol %, and the modifying group (p) has a functional group equivalent weight of 700 to 20,000 g/eq.

Подробнее
25-01-2018 дата публикации

MULTI-REACTOR SLURRY POLYMERIZATION PROCESSES WITH HIGH ETHYLENE PURITY

Номер: US20180022842A1
Принадлежит: BASELL POLYOLEFINE GMBH

A slurry polymerization process for the preparation of polyethylene in a reactor cascade of two or more polymerization reactors including the steps of feeding to a polymerization reactor amounts of ethylene, of a Ziegler catalyst, of fresh aluminum alkyl and of a diluent; feeding the slurry product withdrawn from the polymerization reactor to a second polymerization reactor; and feeding additional amounts of ethylene and of diluent wherein the ethylene is first passed through an ethylene purification unit, which reduces at least the concentration of carbon monoxide, carbon dioxide, oxygen, acetylene and water contained in the ethylene, before it is fed to the two or more polymerization reactors of the reactor cascade. 2. The process of claim 1 , further comprising the steps of: (i) the second slurry product,', '(ii) a third amount of ethylene, and', '(iii) a third amount of diluent, '(g) to a third polymerization reactor, feeding a third set of components comprising'}h) contacting the third set of components in the third polymerization reactor at a reactor temperature from about 60° C. to about 95° C. and a reactor pressure from about 0.15 MPa to about 3 MPa, thereby forming an additional amount of polyethylene in the slurry product comprising particulate polyethylene and a suspension medium; and(i) withdrawing the third slurry product from the third polymerization reactor.3. (canceled)4. The process of claim 1 , wherein the ethylene fed to the polymerization reactors has a carbon monoxide concentration of at most about 0.09 ppm by volume.5. The process of claim 1 , wherein the ethylene fed to the polymerization reactors has a carbon dioxide concentration of at most about 0.9 ppm by volume.6. The process of claim 1 , wherein the ethylene fed to the polymerization reactors has an oxygen concentration of at most about 0.9 ppm by volume.7. The process of claim 1 , wherein the ethylene fed to the polymerization reactors has an acetylene concentration of at most about 2. ...

Подробнее
25-01-2018 дата публикации

POLYMERIC PIEZOELECTRIC FILM AND MANUFACTURING METHOD THEREOF

Номер: US20180022895A1
Принадлежит: Mitsui Chemicals, Inc.

A polymeric piezoelectric film, including a helical chiral polymer (A) having a weight average molecular weight of from 50,000 to 1,000,000 and optical activity, in which, in the film: a crystallinity given by a DSC method is from 20% to 80%; a standardized molecular orientation MORc is from 3.5 to 15.0 when a reference thickness measured by a microwave transmission-type molecular orientation meter is 50 μm; and when a direction parallel to a phase difference streak is a direction X, a direction perpendicular to the direction X and parallel to a main plane of a film is a direction Y, and the phase difference streak is evaluated by an evaluation method A, per a length of 1,000 mm in the direction Y, a number of phase difference streaks with an evaluation value of 60 or more is 0, and a sum of the evaluation values of phase difference streaks with an evaluation value of 20 or more is 1000 or less. 1. A polymeric piezoelectric film , comprising a helical chiral polymer (A) having a weight average molecular weight of from 50 ,000 to 1 ,000 ,000 and optical activity , wherein , in the film:a crystallinity given by a DSC method is from 20% to 80%;a standardized molecular orientation MORc is from 3.5 to 15.0 when a reference thickness measured by a microwave transmission-type molecular orientation meter is 50 μm; andwhen a direction parallel to a phase difference streak is a direction X, a direction perpendicular to the direction X and parallel to a main plane of a film is a direction Y, and the phase difference streak is evaluated by an evaluation method A, per a length of 1,000 mm in the direction Y, a number of phase difference streaks with an evaluation value of 60 or more is 0, and a sum of evaluation values of phase difference streaks with an evaluation value of 20 or more is 1000 or less, (a) with respect to the direction Y, acquiring in-plane phase difference data of a film at intervals of 0.143 mm to obtain an in-plane phase difference profile;', '(b) performing ...

Подробнее
24-01-2019 дата публикации

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

Номер: US20190022470A1
Принадлежит: ACUSHNET COMPANY

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

Подробнее
23-01-2020 дата публикации

Methods for Determining Transition Metal Compound Concentrations in Multicomponent Liquid Systems

Номер: US20200023331A1
Автор: BUCK Richard M., YANG Qing
Принадлежит:

Methods for simultaneously determining the concentrations of transition metal compounds in solutions containing two or more transition metal compounds are described. Polymerization reactor systems providing real-time monitoring and control of the concentrations of the transition metal components of a multicomponent catalyst system are disclosed, as well as methods for operating such polymerization reactor systems. 111-. (canceled)12. A polymerization reactor system comprising:(A) a reactor configured to contact a catalyst system with an olefin monomer and an optional olefin comonomer under polymerization reaction conditions to produce an olefin polymer;(B) a catalyst preparation vessel configured to contact a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst to form the catalyst system; and(C) an analytical system configured to determine a first concentration of the first transition metal compound and a second concentration of the second transition metal compound in a solution comprising the first transition metal compound and the second transition metal compound present within the polymerization reactor system; wherein:the polymerization reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof.13. The reactor system of claim 12 , wherein the analytical system comprises an ultraviolet-visible spectrometer.14. The reactor system of claim 13 , wherein the analytical system further comprises a filter assembly configured to filter a sample of the solution comprising the first transition metal compound and the second transition metal compound before analysis by the ultraviolet-visible spectrometer.15. The reactor system of claim 12 , wherein the reactor system further comprises (D) a controller configured to control a first flow rate of the first transition metal compound and/or a second flow rate of the second transition metal compound into the reactor based ...

Подробнее
24-01-2019 дата публикации

COPOLYMERS AND USES THEREOF

Номер: US20190023826A1
Принадлежит:

The invention relates to a specific copolymer obtainable by co-polymerizing at least the following monomers: —more than 80 wt % of at least one bicyclic (meth)acrylate ester, —0.05 to 15% w/w styrene, and—optionally other ethylenically unsaturated monomers, as well as to the way to synthesize them and the use of such polymers to modify the rheology of a liquid in which they are soluble. 1. A copolymer comprising:83-99.95 wt % of the bicyclic (meth)acrylate esters (a),0.05 to 12 wt % of styrene (b), and0 to 19 wt % of ethylenically unsaturated monomers that are not monomer (a) or (b),up to a total of 100 wt %, wherein the weight percentages of the monomer are based on the total weight of all the monomers.3. A copolymer according to claim 1 , wherein the copolymer is a random co-polymer.6. A copolymer according to claim 1 , comprising a total of bicyclic (meth)acrylate ester and styrene in an amount of 90 wt % of the total monomer claim 1 , or more.7. A copolymer according of claim 6 , comprising a total of bicyclic (meth)acrylate ester and styrene in an amount of 95 wt % or more.8. A copolymer according to claim 7 , wherein the copolymer is produced from isobornyl methacrylate and styrene.9. A copolymer according to claim 1 , having a cloud point in fuel of 12.5° C. or lower.10. A copolymer according to claim 1 , having an average weight average molecular weight of from 100 claim 1 ,000 to 50 claim 1 ,000 claim 1 ,000 D.11. Additive package for fuels comprising a copolymer of .12. Method for the preparation of a copolymer of comprising the step of radically polymerizing the specified monomers.13. Method for the preparation of an additives package for fuel claim 1 , comprising the step of making a solution comprising a copolymer of and one or more other fuel additives.14. Use of a polymer or additive package according to claim 1 , for modifying the rheology of a fluid claim 1 , by dissolving said polymer into said fluid claim 1 , whereby said fluid is not a fuel for ...

Подробнее
24-01-2019 дата публикации

METHOD FOR PRODUCING LOW MOLECULAR WEIGHT POLYTETRAFLUOROETHYLENE, LOW MOLECULAR WEIGHT POLYTETRAFLUOROETHYLENE, AND POWDER

Номер: US20190023856A1
Принадлежит: DAIKIN INDUSTRIES, LTD.

The invention provides a production method for producing low molecular weight polytetrafluoroethylene enabling easy removal of most of C8-C14 perfluorocarboxylic acids and salts thereof, which are unfortunately generated by irradiation, from the low molecular weight polytetrafluoroethylene. The method for producing low molecular weight polytetrafluoroethylene includes: (1) irradiating polytetrafluoroethylene to provide low molecular weight polytetrafluoroethylene having a melt viscosity of 1×10to 7×10Pa·s at 380° C.; (2) pulverizing the low molecular weight polytetrafluoroethylene; and (3) heating the low molecular weight polytetrafluoroethylene pulverized in the step (2). 1. A method for producing low molecular weight polytetrafluoroethylene , comprising:{'sup': 2', '5, '(1) irradiating polytetrafluoroethylene to provide low molecular weight polytetrafluoroethylene having a melt viscosity of 1×10to 7×10Pa·s at 380° C.;'}(2) pulverizing the low molecular weight polytetrafluoroethylene; and(3) heating the low molecular weight polytetrafluoroethylene pulverized in the step (2).2. The production method according to claim 1 ,wherein the heating is performed at a temperature of 50° C. to 300° C.3. The production method according to claim 1 ,wherein the heating is performed at a temperature of 50° C. to 200° C.4. The production method according to claim 1 ,wherein the polytetrafluoroethylene has a standard specific gravity of 2.130 to 2.230.5. The production method according to claim 1 ,wherein both the polytetrafluoroethylene and the low molecular weight polytetrafluoroethylene are in the form of powder.6. The production method according to claim 1 , further comprising:(4) heating the polytetrafluoroethylene up to a temperature that is not lower than the primary melting point thereof to provide a molded article before the step (1),{'sup': '3', 'the molded article having a specific gravity of 1.0 g/cmor higher.'}7. Low molecular weight polytetrafluoroethylene obtainable ...

Подробнее
24-01-2019 дата публикации

AN ETHYLENE/ALPHA-OLEFIN COPOLYMER COMPOSITION, AND ARTICLES COMPRISING THE SAME

Номер: US20190023883A1
Принадлежит: Dow Global Technologies LLC

An ethylene/alpha-olefin copolymer composition having a density from 0.935 to 0.955 g/cc; a ratio of weight average molecular weight to number average molecular weight, Mw/Mn, of from 3 to 10; a z-average molecular weight, Mz, from 200 kg/mol to 500 kg/mol; and a PENT value of greater than 500 hours at 80° C. and 2.4 MPa; wherein when the composition is formed into a monolayer pipe the pipe has a pipe hydrostatic strength of greater than 100 hours at 20° C. and 12.0 MPa. Also provided is a pipe or pipe fitting comprising the ethylene/alpha-olefin copolymer composition. 1. A pipe fabricated from an ethylene/alpha-olefin copolymer composition having:a) a density from 0.935 to 0.955 g/cc;b) a ratio of weight average molecular weight to number average molecular weight, Mw/Mn, of from 3 to 10;c) a z-average molecular weight, Mz, of from 200 kg/mol to 500 kg/mol; andd) a PENT value determined according to ASTM F1473-13 of greater than 500 hours at 80° C. and 2.4 MPa;wherein the pipe has a pipe hydrostatic strength, determined according to ISO 1167, of greater than 100 hours at 20° C. and 12.0 MPa as specified in EN 12201-2.2. The pipe of claim 1 , wherein the pipe further exhibits a pipe hydrostatic strength claim 1 , determined according to ISO 1167 claim 1 , of at least 1 claim 1 ,000 hours at 95° C. and 3.6 MPa as specified in ISO 22391-2.3. The pipe of claim 1 , wherein the composition further exhibits a zero shear viscosity ratio claim 1 , ZSVR claim 1 , of from 1.5 to 20.4. The pipe of claim 1 , wherein the composition further exhibits a dynamic viscosity claim 1 , η* claim 1 , at 100 rad/sec and 190° C. of less than 2 claim 1 ,000 Pa-s.5. The pipe of claim 1 , wherein the composition further exhibits a dynamic viscosity claim 1 , η* claim 1 , at 0.1 rad/sec and 190° C. from 10 claim 1 ,000 to 70 claim 1 ,000 Pa-s.6. The pipe of claim 1 , wherein the composition has a density from 0.940 to 0.952 g/cc.7. The pipe of claim 1 , wherein the composition has a ratio of ...

Подробнее
24-01-2019 дата публикации

RESIN COMPOSITION AND MOLDED ARTICLE

Номер: US20190023887A1
Автор: Tanaka Ryo
Принадлежит: FUJI XEROX CO.,LTD.

A resin composition includes a cellulose ester compound and a styrene-acrylonitrile resin having a weight average molecular weight of 50,000 or greater and 200,000 or less. 1. A resin composition comprising:a cellulose ester compound; anda styrene-acrylonitrile resin having a weight average molecular weight of 50,000 or greater to 200,000 or less.2. The resin composition according to claim 1 ,wherein a ratio of a total mass of the styrene-acrylonitrile resin with respect to a total of a total mass of the cellulose ester compound and the total mass of the styrene-acrylonitrile resin is 0.05 or greater to 0.35 or less.3. The resin composition according to claim 1 ,wherein a ratio of a total mass of the styrene-acrylonitrile resin with respect to a total of a total mass of the cellulose ester compound and the total mass of the styrene-acrylonitrile resin is 0.10 or greater to 0.30 or less.4. The resin composition according to claim 1 ,wherein the cellulose ester compound includes at least one selected from the group consisting of cellulose acetate propionate and cellulose acetate butyrate.5. The resin composition according to claim 1 , further comprising:a thermoplastic elastomer having a constituent unit derived from a (meth)acrylic acid ester compound.6. The resin composition according to claim 5 ,wherein the thermoplastic elastomer has a core-shell structure having a core part and a shell layer.7. The resin composition according to claim 5 ,wherein the thermoplastic elastomer includes a constituent unit derived from an olefin compound.8. The resin composition according to claim 7 ,wherein the constituent unit derived from an olefin compound is a constituent unit derived from at least one compound selected from the group consisting of ethylene, α-olefin, and butadiene.9. The resin composition according to claim 5 ,wherein a ratio of a total mass of the thermoplastic elastomer with respect to a total of a total mass of the cellulose ester compound and a total mass of ...

Подробнее
24-01-2019 дата публикации

THERMOPLASTIC COMPOSITIONS CONTAINING ACRYLIC COPOLYMERS AS MELT STRENGTH AND CLARITY PROCESS AIDS

Номер: US20190023889A1
Автор: PETR Michael T.
Принадлежит:

Provided are thermoplastic polymer composition comprising (a) a polyvinyl halide, and (b) an acrylic copolymer comprising 70 to 100 weight % of a first polymeric stage, based on the total weight of the acrylic copolymer, comprising polymerized units derived from at least 85 weight % of one or more C-Calkyl methacrylate monomers and C-Calkyl acrylate monomers, based on the total weight of monomers in the first polymeric stage, wherein the first polymeric stage has a calculated Tof 70° C. or less, and wherein the acrylic copolymer has a molecular weight of greater than 1.5×10g/mol. 1. A thermoplastic polymer composition comprising:(a) a polyvinyl halide; and{'sub': 1', '6', '1', '3', 'g, 'sup': '6', '(b) an acrylic copolymer comprising 70 to 100 weight % of a first polymeric stage, based on the total weight of the acrylic copolymer, comprising polymerized units derived from at least 85 weight % of one or more C-Calkyl methacrylate monomers and C-Calkyl acrylate monomers, based on the total weight of monomers in the first polymeric stage, wherein the first polymeric stage has a calculated Tof 70° C. or less, and wherein the acrylic copolymer has a molecular weight of 1.5×10g/mol or more.'}2. The thermoplastic polymer composition of claim 1 , wherein the first polymeric stage comprises (i) 35 to 75 weight % of methyl methacrylate monomers claim 1 , and (ii) 25 to 65 weight % of one or more C-Calkyl methacrylate monomers and C-Calkyl acrylate monomers claim 1 , based on the total weight of monomers in the first polymeric stage.3. The thermoplastic polymer composition of claim 2 , wherein the C-Calkyl methacrylate monomers and C-Calkyl acrylate monomers of the first polymeric stage comprise one or more of butyl methacrylate and ethyl acrylate.4. The thermoplastic polymer composition of claim 1 , wherein the acrylic copolymer further comprises a second polymeric stage comprising polymerized units derived from one or more C-Calkyl (meth)acrylate monomers.5. The ...

Подробнее
24-01-2019 дата публикации

METHOD OF PREPARING ABS-BASED GRAFT COPOLYMER HAVING IMPROVED IMPACT STRENGTH AND METHOD OF MANUFACTURING ABS-BASED INJECTION-MOLDED ARTICLE INCLUDING THE SAME

Номер: US20190023894A1
Принадлежит:

The present invention relates to a method of preparing an ABS-based graft copolymer having improved impact strength and an ABS-based injection-molded article including the same. More particularly, the present invention provides an ABS-based copolymer resin having improved impact strength by optimizing structures of large-diameter diene-based rubber latex particles and a matrix structure between ABS-based copolymer particles and a SAN resin through introduction of a multimeric acid of an unsaturated fatty acid or a metal salt thereof as an emulsifier in a large-diameter diene-based rubber latex polymerization step and an ABS graft polymerization step. 1. A method of preparing an ABS-based graft copolymer having improved impact strength , the method comprising:a) a step of polymerizing 100 parts by weight of a conjugated diene-based monomer, 0.5 to 5 parts by weight of an emulsifier, and 0.01 to 6 parts by weight of a water-soluble polymerization initiator; b) a step of adding 0.01 to 5 parts by weight of an emulsifier thereto when a polymerization conversion rate is 60 to 85%, after step a); c) a step of terminating polymerization when a polymerization conversion rate is 90 to 99% to obtain a large-diameter diene-based rubber latex; and d) a step of graft-polymerizing 100 parts by weight of a monomer mixture comprising 40 to 70% by weight (based on solids) of the large-diameter diene-based rubber latex, 15 to 35% by weight of an aromatic vinyl monomer, and 5 to 25% by weight of a vinyl cyan monomer with 0.01 to 3 parts by weight of an emulsifier, 0.01 to 3 parts by weight of an initiator, and 0.001 to 1 part by weight of an oxidation-reduction catalyst,wherein the emulsifiers of steps a) and d) are a multimeric acid of an unsaturated fatty acid or a metal salt thereof.2. The method according to claim 1 , wherein the unsaturated fatty acid is a straight-chain claim 1 , branched-chain claim 1 , or cyclic unsaturated fatty acid having 8 to 22 carbon atoms.3. The method ...

Подробнее
25-01-2018 дата публикации

POLYMER AND POSITIVE RESIST COMPOSITION

Номер: US20180024430A1
Автор: Hoshino Manabu
Принадлежит: ZEON CORPORATION

Provided are a polymer that can be favorably used as a positive resist having a low film reduction rate in a state of low irradiation with ionizing radiation or the like and a positive resist composition that can favorably form a high-resolution pattern. The polymer includes an α-methylstyrene unit and a methyl α-chloroacrylate unit, and the proportion of components having a molecular weight of less than 6,000 in the polymer is no greater than 0.5%. The positive resist composition contains the aforementioned polymer and a solvent. 1. A polymer comprising an α-methylstyrene unit and a methyl α-chloroacrylate unit , whereina proportion of components having a molecular weight of less than 6,000 is no greater than 0.5%.2. The polymer according to claim 1 , whereina proportion of components having a molecular weight of less than 10,000 is no greater than 0.5%.3. The polymer according to claim 1 , whereina proportion of components having a molecular weight of greater than 80,000 is at least 15%.4. The polymer according to claim 1 , having a weight average molecular weight (Mw) of at least 55 claim 1 ,000.5. A positive resist composition comprising the polymer according to and a solvent. The present disclosure relates to a polymer and a positive resist composition, and in particular relates to a polymer that is suitable for use as a positive resist and a positive resist composition that contains this polymer.Polymers that display increased solubility in a developer after undergoing main chain scission through irradiation with ionizing radiation, such as an electron beam, or short-wavelength light, such as ultraviolet light, are conventionally used as main chain scission-type positive resists in fields such as semiconductor production. (Hereinafter, the term “ionizing radiation or the like” is used to refer collectively to ionizing radiation and short-wavelength light.)PTL 1 discloses one example of a main chain scission-type positive resist having high sensitivity. The ...

Подробнее
25-01-2018 дата публикации

POLYMER AND POSITIVE RESIST COMPOSITION

Номер: US20180024432A1
Автор: Hoshino Manabu
Принадлежит: ZEON CORPORATION

Provided are a polymer that can be favorably used as a positive resist having a low film reduction rate under low irradiation, a high y value, and high sensitivity, and a positive resist composition that can efficiently form a high-resolution pattern. The polymer includes an a-methylstyrene unit and a methyl α-chloroacrylate unit, and has a molecular weight distribution (Mw/Mn) of less than 1.48. In the polymer, the proportion of components having a molecular weight of less than 6,000 is no greater than 0.5% and the proportion of components having a molecular weight of greater than 80,000 is no greater than 6.0%. The positive resist composition contains the aforementioned polymer and a solvent. 1. A polymer comprising an α-methylstyrene unit and a methyl α-chloroacrylate unit , whereinthe polymer has a molecular weight distribution (Mw/Mn) of less than 1.48,a proportion of components having a molecular weight of less than 6,000 is no greater than 0.5%, anda proportion of components having a molecular weight of greater than 80,000 is no greater than 6.0%.2. The polymer according to claim 1 , whereina proportion of components having a molecular weight of less than 10,000 is no greater than 0.8%.3. The polymer according to claim claim 1 , having a weight average molecular weight (Mw) of at least 30 claim 1 ,000.4. The polymer according to claim 1 , whereina proportion of components having a molecular weight of greater than 100,000 is at least 0.5%.5. A positive resist composition comprising the polymer according to and a solvent. The present disclosure relates to a polymer and a positive resist composition, and in particular relates to a polymer that is suitable for use as a positive resist and a positive resist composition that contains this polymer.Polymers that display increased solubility in a developer after undergoing main chain scission through irradiation with ionizing radiation, such as an electron beam, or short-wavelength light, such as ultraviolet light, ...

Подробнее
24-01-2019 дата публикации

AQUEOUS POLYMER DISPERSIONS, A METHOD FOR THEIR PREPARATION AND THE USE THEREOF AS POUR-POINT DEPRESSANTS FOR CRUDE OIL, PETROLEUM, AND PETROLEUM PRODUCTS

Номер: US20190024011A1
Принадлежит:

The invention relates to aqueous polymer dispersions comprising at least one polymer obtainable by the reaction of at least one monomer M1 of the general formula HC═CH—C(O)OR (I), wherein R is an unbranched alkyl chain comprising from 18 to 22 carbon atoms, and optionally at least one monomer M2. The invention relates moreover to a method for the preparing of such aqueous polymer dispersion and the use thereof as pour point depressant for crude oil, petroleum, and petroleum products. 115.-. (canceled)16. An aqueous polymer dispersion comprising [ {'br': None, 'sub': '2', 'HC═CH—C(O)OR\u2003\u2003(I)'}, '50 to 100% by weight of at least one monomer M1 of the general formula (I)'}, 'wherein R is an unbranched alkyl chain comprising from 18 to 22 carbon atoms; and', '0 to 50% by weight of at least one monomer M2, which is different from monomer M1;, 'a) 10 to 55% by weight based on the dispersion of at least one polymer P obtainable by the reaction of reactive monomers M, wherein the reactive monomers M comprise'}wherein the amounts of the monomers M1 and M2 are each based on the total amount of all reactive monomers M used in the reaction,{'sub': 'w', 'wherein the polymer P has a weight-average molecular weight Mof 20,000 to 150,000 g/mol according to DIN 55672-1:1995-02; and'}{'sub': '50', 'wherein the polymer P is present in the form of particles having an average particle size dof from 75 nm to 400 nm effected by Column Hydrodynamic Chromatography;'}b) 0 to 24.5% by weight based on the total amount of the aqueous polymer dispersion of at least one with water miscible solvent,c) 0 to 30% by weight based on the total amount of the aqueous polymer dispersion of at least one hydrophobic organic solvent, 15 to 30% by weight of acrylic acid, methacrylic acid, or a mixture thereof; and', '70 to 85% by weight of methyl methacrylate, n-butyl acrylate, 2-ethylhexyl acrylate, styrene, alpha-methyl styrene, or a mixture of two or more thereof, in polymerized form,', 'wherein ...

Подробнее
28-01-2021 дата публикации

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

Номер: US20210024660A1
Принадлежит:

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

Подробнее
31-01-2019 дата публикации

SHOE SOLES, COMPOSITIONS, AND METHODS OF MAKING THE SAME

Номер: US20190029361A1
Принадлежит: COOPER-STANDARD AUTOMOTIVE INC.

A shoe sole composition and method for making a shoe sole are provided. The shoe sole includes a composition comprising a foamed silane-crosslinked polyolefin elastomer having a density less than 0.50 g/cm. The shoe sole exhibits a compression set of from about 5.0% to about 20.0%, as measured according to ASTM D 395 (6 hrs @ 50° C.). The foamed silane-crosslinked polyolefin elastomer can be produced from a blend including a first polyolefin having a density less than 0.86 g/cm, a second polyolefin, having a crystallinity less than 40%, a silane crosslinker, a grafting initiator, a condensation catalyst, and a foaming agent. 1. A shoe midsole comprising:{'sup': '3', 'claim-text': [{'sup': '3', 'a first polyolefin having a density less than 0.86 g/cm,'}, 'a second polyolefin having a crystallinity less than 40%,', 'a silane crosslinker,', 'a grafting initiator,', 'a condensation catalyst, and', 'a foaming agent,, 'a foamed silane-crosslinked polyolefin elastomer having a density less than 0.50 g/cm, the foamed silane-crosslinked polyolefin elastomer comprisingwherein the shoe midsole exhibits a compression set of from about 1.0% to about 50.0%, as measured according to ASTM D 395 (48 hrs @ 50° C.).2. The shoe midsole of claim 1 , wherein the first polyolefin is an ethylene/α-olefin copolymer from about 60 wt % to about 97 wt %.3. The shoe midsole of claim 1 , wherein the second polyolefin is a polypropylene homopolymer and/or a poly(ethylene-co-propylene) claim 1 , the second polyolefin from about 10 wt % to about 35 wt %.4. The shoe midsole of claim 1 , wherein the silane crosslinker comprises a vinyltrialkoxy silane from about 1 wt % to about 4 wt %.5. The shoe midsole of claim 1 , wherein the grafting initiator comprises one or more halogen molecules claim 1 , azo compounds claim 1 , carboxylic peroxyacids claim 1 , peroxyesters claim 1 , peroxyketals claim 1 , and peroxides claim 1 , the grafting initiator from greater than 0.15 wt % to about 2 wt %.6. The shoe ...

Подробнее
01-02-2018 дата публикации

METHOD OF FORMING THERMORESPONSIVE POLYMERS

Номер: US20180030171A1
Автор: Delgado Paula, Palkar Amit
Принадлежит: Phillips 66 Company

A method of forming a thermoresponsive polymer. The method proceeds by mixing 2-(3-(4-methyl-6-oxo-1,6-dihydropyrimidin-2-yl)ureido)ethyl methacrylate and methacrylamide in the presence of a solvent form a monomer solution. An initiator is then added to the monomer solution to form a thermoresponsive polymer. 1. A method comprising:mixing 2-(3-(4-methyl-6-oxo-1,6-dihydropyrimidin-2-yl)ureido)ethyl methacrylate and methacrylamide in the presence of an organic solvent to form a monomer solution;adding an initiator to the monomer solution to form a thermoresponsive polymer.2. The method of claim 1 , wherein the organic solvent is selected from the group consisting of: dimethyl sulfoxide claim 1 , dimethyl formamide claim 1 , ethyl acetate claim 1 , methanol claim 1 , dioxane claim 1 , tetrahydrofuran claim 1 , acetone claim 1 , methylene chloride and toluene and combinations thereof.3. The method of claim 1 , wherein monomer solution is heated to a temperature greater than 50° C.4. The method of claim 1 , wherein monomer solution is heated to a temperature greater than 70° C.5. The method of claim 1 , wherein the initiator is an addition-type initiator.6. The method of claim 1 , wherein the initiator is selected from the group consisting of: azo initiators claim 1 , azobisisobutyronitriles claim 1 , peroxides claim 1 , persulfates and combinations thereof.7. The method of claim 1 , wherein the mixing of monomer solution occurs at an elevated temperature.8. The method of claim 7 , wherein the elevated temperature is greater than 50° C.9. The method of claim 1 , wherein the thermoresponsive polymer is purified in a polar solvent.10. The method of claim 1 , wherein the thermoresponsive polymer is water soluble.12. The method of claim 1 , wherein the thermoresponsive polymer has an average molecular weight greater than 50 claim 1 ,000.11. A method comprising:mixing from about 0.01 mol % to about 50 mol % 2-(3-(4-methyl-6-oxo-1,6-dihydropyrimidin-2-yl)ureido)ethyl ...

Подробнее
01-02-2018 дата публикации

Method of forming thermoresponsive polymers

Номер: US20180030172A1
Автор: Amit Palkar, Paula Delgado
Принадлежит: Phillips 66 Co

A method of forming a thermoresponsive polymer. The method begins by mixing in the presence of an organic solvent to form a monomer solution. An initiator is then added to the monomer solution to form a thermoresponsive polymer. In this method, R1 and R4 can be independently selected from the group consisting of H and alkyl groups; R2 and R3 can be independently selected from the group consisting of H, alkyl, olefinic, aromatic, heterocyclic, halogen, ammonium, nitroxides, nitrates, nitrite amides, amines, esters, ethers, carboxylic acids, acyl chlorides, alcohols, nitriles, phosphates, phosphonates, sulfates, sulfonates, sulfide, sulfite, thiol, and combinations thereof; Y can be selected from the group consisting of O, N and S; R5 and R6 can be independently selected from the group consisting of alkyl, olefinic, heterocyclic, halogens, ammonium, carboxylic, amines, esters, amides and combinations thereof; and X are methylene groups from about 0 to about 20 carbons.

Подробнее
01-02-2018 дата публикации

METHOD OF REDUCING DRAG IN A CONDUIT

Номер: US20180030178A1
Принадлежит:

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

Подробнее
01-02-2018 дата публикации

PRODUCTION METHOD OF ALPHA-OLEFIN LOW POLYMER AND PRODUCTION APPARATUS

Номер: US20180030181A1
Автор: Emoto Hiroki
Принадлежит:

The present invention relates to a method and an apparatus for producing an α-olefin low polymer by subjecting an α-olefin to low polymerization reaction in the presence of a catalyst in a liquid phase part within a reactor, and the present invention relates to a method and an apparatus for producing an α-olefin low polymer, such as 1-hexene, etc., by subjecting an α-olefin, such as ethylene, etc., to low polymerization reaction, in which the formation of a polymer on an upper tube plate surface of a shell and tube type heat exchanger that is used for heat removal is suppressed, thereby performing a continuous operation stably over a long period of time. 1. A method for producing an α-olefin low polymer by subjecting an α-olefin to low polymerization reaction in the presence of a catalyst , the method comprising:a step of withdrawing a gas of a gas phase part within a reactor, introducing the gas for cooling into a shell and tube type heat exchanger, and circulating and supplying an obtained condensed liquid into the reactor,wherein the heat exchanger includes jet nozzles for supplying atomized droplets between a gas supply port and a tube plate,{'sup': '3', 'the gas is supplied as a gas having a density of 20 kg/mor more at a gas flow rate of 1 m/s or more from the gas supply port, and'}{'sup': '2', 'the atomized droplets are supplied from the jet nozzles provided in five or more places per 1.00 mof an area of the tube plate.'}2. A method for producing an α-olefin low polymer by subjecting an α-olefin to low polymerization reaction in the presence of a catalyst within a reactor , the method comprising:a step of withdrawing a part of a gas of a gas phase part within a reactor, introducing the gas for cooling into a shell and tube type heat exchanger, and circulating and supplying an obtained condensed liquid into the reactor,wherein the heat exchanger includes: a cylindrical shell; an upper tube plate and a lower tube plate disposed on an upper end side and a lower ...

Подробнее
17-02-2022 дата публикации

Alkane-soluble non-metallocene precatalysts

Номер: US20220049032A1
Принадлежит: Dow Global Technologies LLC

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

Подробнее
30-01-2020 дата публикации

Polymerization Process

Номер: US20200031964A1
Автор: Pannell Richard B.
Принадлежит:

A process including contacting one or more monomers, at least one catalyst system, and a condensing agent including a majority of propane under polymerizable conditions to produce a polyolefin polymer is provided. 1. A polymerization process , the process comprising contacting one or more monomers , at least one catalyst system , and a condensing agent comprising a majority of propane under polymerizable conditions to produce a polyolefin polymer.2. The process of claim 1 , wherein the production rate of the polyolefin polymer is at least 5% greater than the same process polymerizing with a condensing agent consisting essentially of isopentane.3. The process of claim 1 , wherein the polyolefin density (ASTM D1505) is ≤0.912 g/cmand the space time yield is >14.0 lb/ft3/hr (224. kg/m/hr).4. The process of claim 1 , wherein the space time yield is >17.5 lb/ft3/hr (280. kg/m/hr)5. The process of claim 1 , wherein the production rate when producing a polyolefin polymer having density ≤0.912 g/cmis ≥80% of the production rate when producing a polyolefin polymer having a density ≥0.918 g/cm claim 1 , density measured by ASTM D1505.6. The process of claim 1 , wherein the reactor pressure is from 22 to 29 barg.7. The process of claim 1 , wherein the reactor pressure is from 26 to 29 barg.8. The process of claim 1 , wherein the condensing agent comprises ≥25 mol % propane.9. The process of claim 1 , wherein the condensing agent comprises a majority of propane.10. The process of claim 1 , wherein the condensing agent further comprises at least one C-Ccondensing agent.11. The process of claim 10 , wherein the at least one C-Ccondensing agent comprises n-butane claim 10 , isobutane claim 10 , n-pentane claim 10 , isopentane claim 10 , 2 claim 10 ,2-dimethylpropane claim 10 , n-hexane claim 10 , isohexane claim 10 , n-heptane claim 10 , n-octane claim 10 , or mixtures thereof.12. The process of claim 1 , wherein the mole ratio of the propane to the at least one C-Ccondensing ...

Подробнее
31-01-2019 дата публикации

MACROMOLECULAR CONJUGATES FOR VISUALIZATION AND SEPARATION OF PROTEINS AND CELLS

Номер: US20190033300A1
Принадлежит:

A macromolecular water-soluble conjugates based on synthetic copolymers to which at least one affinity tag, at least one imaging probe and at least one targeting ligand are bound via covalent bonds. The macromolecular conjugate may be used in identification, visualization, quantification or isolation of proteins and/or cells. 2. The method according to claim 1 , wherein the molecular weight of the conjugate is in the range of 1000 to 500000 g/mol.3. The method according to claim 1 , wherein the targeting ligand is a moiety capable of selectively binding to the target protein claim 1 , wherein the targeting ligand is selected from the group consisting of an inhibitor or substrate of the targeted enzyme claim 1 , an agonist or antagonist of the targeted receptor claim 1 , and a ligand of the target protein resin.4. The method according to claim 1 , wherein the targeting ligand may be attached to the synthetic copolymer via a linker claim 1 , a peptide claim 1 , a nucleic acid claim 1 , or an oligosaccharide.5. The method according to claim 1 , wherein the affinity tag is selected from biotin claim 1 , His-tag claim 1 , FLAG tag claim 1 , HA tag claim 1 , Strep-tag claim 1 , Avi-Tag claim 1 , GST-tag claim 1 , c-myc-tag claim 1 , V5-tag claim 1 , E-tag claim 1 , S-tag claim 1 , SBP-tag claim 1 , poly(Glu)-tag claim 1 , and calmodulin.6. The method according to claim 1 , wherein the imaging probe is selected from the group comprising fluorescent moieties claim 1 , radionuclides and metal complexes.7. The method according to claim 6 , wherein the imaging probe is selected from the group consisting of fluorophores with an excitation maximum in the range of 350 to 850 nm claim 6 , lanthanide complexes claim 6 , and radionuclide complexes Cu claim 6 , Ga claim 6 , F claim 6 , Tc claim 6 , I claim 6 , I claim 6 , I claim 6 , Co claim 6 , Ga claim 6 , Cu claim 6 , In claim 6 , Y.8. The method according to wherein the method of identification claim 1 , visualization claim 1 , ...

Подробнее
04-02-2021 дата публикации

Olefin polymerization activators

Номер: US20210032382A1
Принадлежит: Dow Global Technologies LLC

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

Подробнее
09-02-2017 дата публикации

PROCESS FOR MAKING A STABILIZED FABRICATED ARTICLE FROM POLYOLEFIN

Номер: US20170037160A1
Принадлежит:

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

Подробнее
09-02-2017 дата публикации

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

Номер: US20170037164A1
Принадлежит:

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

Подробнее
08-02-2018 дата публикации

METHOD FOR PREPARING POLYOLEFIN

Номер: US20180037676A1
Принадлежит:

The present invention provides a method for preparing a polyolefin having a broad molecular weight distribution. More specifically, the present invention provides a method for preparing a polyolefin having a broad molecular weight distribution and an ultra-high molecular weight in which an organometallic complex containing a specific Ti—Al complex structure is used as a molecular weight controller (i.e., molecular weight enhance) in the polymerization of an olefin monomer, thereby enabling both solution polymerization and slurry polymerization, particularly enabling the molecular weight distribution to be more readily and effectively controlled. 2. The method for preparing a polyolefin according to claim 1 , wherein at least one of Rto Rin the chemical formula 1 is an alkoxyalkyl having 1 to 10 carbon atoms.3. The method for preparing a polyolefin according to claim 1 , wherein at least one of Rto Rin the chemical formula 1 is an alkoxyalkyl having 8 to 10 carbon atoms.4. The method for preparing a polyolefin according to claim 1 , wherein claim 1 , in the chemical formula 1 claim 1 , Ris a branched alkylene group having 4 to 10 carbon atoms claim 1 , and Rand Rare each independently an alkyl group having 4 to 10 carbon atoms.5. The method for preparing a polyolefin according to claim 1 , wherein the compound of the chemical formula 1 is included in a molar ratio of 0.05 to 1 with respect to 1 mole of the transition metal contained in the metallocene compound.7. The method for preparing a polyolefin according to claim 1 , wherein the metallocene catalyst further includes a support selected from the group consisting of silica claim 1 , silica-alumina claim 1 , and silica-magnesia claim 1 , andan amount of hydroxyl group on the surface of the support is 0.1 to 10 mmol/g.8. The method for preparing a polyolefin according to claim 1 , wherein the metallocene catalyst includes a metallocene compound claim 1 , a cocatalyst claim 1 , and a metallocene supported catalyst in ...

Подробнее
09-02-2017 дата публикации

Aldehyde-Functionalized Polymers for Paper Strength and Dewatering

Номер: US20170037574A1
Принадлежит: ECOLAB USA INC.

Disclosed are compositions and methods useful in applications relating to papermaking. The compositions and methods of the present invention comprise aldehyde-functionalized polymers designed to impart high paper strength and enhance water removal during the papermaking process. The aldehyde-functionalized polymers are of relatively low molecular weight, and comprise amino and/or amide groups mono-reacted and di-reacted at a ratio of at least about 1.5 to 1. The low molecular weight polymers of the present invention have the same strength and dewatering performance as corresponding high molecular weight polymers. 1. A composition for treating the strength and press section dewatering of a paper sheet comprising one or more aldehyde-functionalized polymers comprising amino groups , amide groups , or a combination of amino and amide groups thereof , wherein (i) at least about 15 mole percent of the amino groups , amide groups , or both the amino and amide groups are functionalized with one or more aldehydes , (ii) the amino groups , amide groups , or both the amino and amide groups are mono-reacted and di-reacted at a ratio of at least about 1.5 to 1 , and (iii) the aldehyde-functionalized polymers have an average molecular weight of from about 10 ,000 g/mole to about 300 ,000 g/mole.2. The composition of claim 1 , wherein the amino groups claim 1 , amide groups claim 1 , or combination of the amino and amide groups thereof are mono-reacted and di-reacted at a ratio of at least about 3 to 1 and the aldehyde-functionalized polymers have an average molecular weight of from about 10 claim 1 ,000 g/mole to about 300 claim 1 ,000 g/mole.3. The composition of claim 1 , wherein the amino groups claim 1 , amide groups claim 1 , or combination of the amino and amide groups thereof are mono-reacted and di-reacted at a ratio of at least about 3 to 1 and the aldehyde-functionalized polymers have an average molecular weight of from about 10 claim 1 ,000 g/mole to about 100 claim 1 ...

Подробнее
09-02-2017 дата публикации

PVDF-TrFE Co-Polymer Having Improved Ferroelectric Properties, Methods of Making a PVDF-TrFE Co-Polymer Having Improved Ferroelectric Properties and Methods of Changing the End Group of a PVDF-TrFE Co-Polymer

Номер: US20170040156A1
Принадлежит: Thin Film Electronics ASA

A method of exchanging or transforming end groups in and/or improving the ferroelectric properties of a PVDF-TrFE co-polymer is disclosed. A bulky or chemically dissimilar end group, such as an iodine, sulfate, aldehyde or carboxylic acid end group, may be transformed to a hydrogen, fluorine or chlorine atom. A method of making a PVDF-TrFE co-polymer is disclosed, including polymerizing a mixture of VDF and TrFE using an initiator, and transforming a bulky or chemically dissimilar end group to a hydrogen, fluorine or chlorine atom. A PVDF-TrFE co-polymer or other fluorinated alkene polymer is also disclosed. The co-polymer may be used as a ferroelectric, electromechanical, piezoelectric or dielectric material in an electronic device. 1. A method of exchanging an end group of a polyvinylidene fluoride-trifluoroethylene (PVDF-TrFE) co-polymer , the end group comprising:exchanging an iodine or hydroxyl end group on a polyvinylidene fluoride-trifluoroethylene (PVDF-TrFE) co-polymer with hydrogen, fluorine or chlorine, andisolating or purifying the PVDF-TrFE co-polymer having the hydrogen, fluorine or chlorine end group.2. The method according to claim 1 , wherein the PVDF-TrFE co-polymer has the iodine end group claim 1 , and exchanging the iodine end group comprises reacting the PVDF-TrFE co-polymer having the iodine end group with a tin hydride complex.3. The method according to claim 1 , wherein the PVDF-TrFE co-polymer has the hydroxy end group claim 1 , and exchanging the hydroxy end group comprises reacting the PVDF-TrFE co-polymer having the hydroxy end group with a source of hydrogen claim 1 , fluorine or chlorine.4. The method according to claim 3 , wherein the PVDF-TrFE co-polymer has the hydroxy end group claim 3 , and exchanging the hydroxy end group comprises reacting the PVDF-TrFE co-polymer having the hydroxy end group with a source of hydrogen.5. The method according to claim 3 , further comprising converting a PVDF-TrFE claim 3 , co-polymer having a ...

Подробнее
07-02-2019 дата публикации

Pressure-Sensitive Adhesive, and Self-Adhesive Products and Composites Comprising the Latter

Номер: US20190040285A1
Принадлежит:

The invention relates to a block copolymer-containing pressure-sensitive adhesive comprising e) 52% by weight to 65% by weight, preferably 55% by weight to 62% by weight, of an elastomer component, f) 30% by weight to 45% by weight, preferably 35% by weight to 42% by weight, of at least one bonding resin, g) 0% by weight to 15% by weight, preferably to 10% by weight, of at least one softening resin and h) 0% by weight to 18% by weight, preferably to 10% by weight, of further additives, where the elastomer component (a) consists to an extent of at least 90% by weight of polyvinylaromatic-polybutadiene block copolymers, where the polyvinylaromatic-polybutadiene block copolymers include at least one type of diblock copolymer (a1) and at least one type of tri- or multiblock copolymer (a2), the at least one diblock copolymer (a1) has a vinylaromatic content of 15% by weight to 45% by weight, within the elastomer component (a) the proportion of tri- or multiblock copolymer (a2) is between 25% by weight and 50% by weight, preferably between 30% by weight and 45% by weight, the tri- or multiblock copolymer (a2) has a molar mass of at least 125 000 g/mol and a vinylaromatic content of 15% to 45% by weight, and one kind of the tri- or multiblock copolymer is preferably a multi-arm (radial) block copolymer. 1. A block copolymer-containing pressure-sensitive adhesive comprising:a) 52 wt % to 65 wt %, of an elastomer component,b) 30 wt % to 45 wt %, of at least one tackifier resin,c) 0 wt % to 15 wt %, of at least one plasticizing resin, and wherein the elastomer component (a) is at least 90 wt % of polyvinylaromatic-polybutadiene block copolymers, the polyvinylaromatic-polybutadiene block copolymers comprising at least one kind of a diblock copolymer (a1) and at least one kind of a triblock or multiblock copolymer (a2),', 'the at least one diblock copolymer (a1) has a vinylaromatic fraction of 15 wt % to 45 wt %, within the elastomer component (a) the fraction of triblock or ...

Подробнее
18-02-2016 дата публикации

Ziegler-natta catalyst for high temperature polymerization

Номер: US20160046745A1
Принадлежит: Nova Chemicals International SA

The various embodiments of the invention provide, a magnesium titanium polymerization procatalyst, methods for making and using the same.

Подробнее
15-02-2018 дата публикации

Process for Reducing the Light Oligomer Content of Polypropylene Oils

Номер: US20180044446A1
Принадлежит:

Disclosed herein are dual catalyst compositions containing an unbridged metallocene compound, a bridged metallocene compound, a chemically-treated solid oxide, and an optional co-catalyst. These catalyst compositions can be used for the oligomerization of propylene to produce an oligomer product. For example, a heavy propylene oligomer can be recovered from the oligomer product, and the heavy propylene oligomer can be characterized by a high flash point and viscosity index, and a low pour point. 1. An oligomerization process comprising: (i) catalyst component I comprising an unbridged zirconium or hafnium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group;', '(ii) catalyst component II comprising a single atom bridged, zirconium or hafnium based metallocene compound containing two cyclopentadienyl groups;', '(iii) a chemically-treated solid oxide; and', '(iv) optionally, a co-catalyst;, 'contacting an olefin feedstock comprising propylene with a catalyst composition comprisingto form an oligomer product under oligomerization conditions; andisolating a heavy propylene oligomer by removing unreacted propylene and at least a portion of light propylene oligomers from the oligomer product using one or more separation steps, wherein the heavy propylene oligomer is characterized by a pour point in a range from about 0 to about −55° C.2. The process of claim 1 , wherein the heavy propylene oligomer is characterized by:a flash point in a range from about 140 to about 300° C.; anda viscosity index in a range from about 75 to about 200.3. The process of claim 1 , wherein the heavy propylene oligomer is characterized by:a flash point in a range from about 140 to about 260° C.;a viscosity index in a range from about 80 to about 130; anda pour point in a range from about −5 to about −30° C.4. The process of claim 1 , wherein the heavy propylene oligomer is characterized by:a Mw in a range from about ...

Подробнее
15-02-2018 дата публикации

Propylene-Olefin Copolymers and Methods for Making the Same

Номер: US20180044514A1
Принадлежит: ExxonMobil Chemical Patents Inc

Provided is a composition having 70 wt % to 90 wt % of a first propylene-olefin copolymer component having an ethylene content of 15 to 21 wt %; and 10 wt % to 30 wt % of a second propylene-olefin copolymer component having an ethylene content of 6 to 10 wt %; wherein the weight average molecular weight of the first component is 250,000 to 1,780,000 g/mol higher than the weight average molecular weight of the second component; wherein the reactivity ratio product of the first component is less than 0.75; wherein the reactivity ratio product of the second component is greater than or equal to 0.75.

Подробнее
15-02-2018 дата публикации

CURABLE LIQUID DEVELOPER

Номер: US20180046105A1
Принадлежит:

Provided is a curable liquid developer having sufficient fixability while being a curable liquid developer containing a polymer material. The curable liquid developer includes: a cationic polymerizable liquid monomer including a vinyl ether monomer; and toner particles insoluble in the cationic polymerizable liquid monomer, in which the curable liquid developer further includes a polymerizable polyolefin including a polyolefin in a main chain thereof, the polymerizable polyolefin having a vinyl ether group at at least one terminal of the polyolefin. 1. A curable liquid developer , comprising:a cationic polymerizable liquid monomer including a vinyl ether monomer; andtoner particles insoluble in the cationic polymerizable liquid monomer, whereinthe curable liquid developer further comprises a polymerizable polyolefin comprising a polyolefin in a main chain thereof, at least one terminal of the polyolefin having a vinyl ether group.2. A curable liquid developer according to claim 1 , wherein the polymerizable polyolefin has vinyl ether groups at a plurality of terminals of the polyolefin.3. A curable liquid developer according to claim 1 , wherein the polymerizable polyolefin has a weight-average molecular weight of 900 to 10 claim 1 ,000.4. A curable liquid developer according to claim 3 , wherein the polymerizable polyolefin has a weight-average molecular weight of 1 claim 3 ,000 to 10 claim 3 ,000.5. A curable liquid developer according to claim 1 , wherein the polymerizable polyolefin has a structure derived from one of 1 claim 1 ,2-polybutadiene and 1 claim 1 ,4-polyisoprene claim 1 , and has hydrogen added to a double bond moiety except the vinyl ether group.67-. (canceled)8. A curable liquid developer according to claim 2 , wherein the polymerizable polyolefin has a weight-average molecular weight of 900 to 10 claim 2 ,000.9. A curable liquid developer according to claim 2 , wherein the polymerizable polyolefin has a weight-average molecular weight of 1 claim 2 ...

Подробнее
14-02-2019 дата публикации

ROOFING MEMBRANES, COMPOSITIONS, AND METHODS OF MAKING THE SAME

Номер: US20190045881A1
Принадлежит: COOPER-STANDARD AUTOMOTIVE INC.

A roofing membrane and a method of making the same is provided. The roofing membrane includes a top layer having a flame retardant and a first silane-crosslinked polyolefin elastomer with a density less than 0.90 g/cm; a scrim layer; and a bottom layer having a flame retardant and a second silane-crosslinked polyolefin elastomer with a density less than 0.90 g/cm. The top and bottom layers of the roofing membrane both exhibit a compression set of from about 5.0% to about 35.0%, as measured according to ASTM D 395 (22 hrs @ 70° C.). 1. A roofing membrane comprising:{'sup': '3', 'a top layer comprising a flame retardant and a first silane-crosslinked polyolefin elastomer having a density less than 1.45 g/cm;'}an optional scrim layer; and{'sup': '3', 'a bottom layer comprising a flame retardant and a second silane-crosslinked polyolefin elastomer having a density less than 1.45 g/cm.'}2. The roofing membrane of claim 1 , wherein the flame retardant comprises a magnesium hydroxide and/or an aluminum hydroxide from about 20 wt % to about 70 wt %.3. The roofing membrane of claim 1 , wherein the first and second silane-crosslinked polyolefin elastomers both exhibit a crystallinity of from about 5% to about 25%.4. The roofing membrane of claim 1 , wherein the first and second silane-crosslinked polyolefin elastomers have a glass transition temperature of from about −75° C. to about −25° C.5. The roofing membrane of claim 1 , wherein the first and second silane-crosslinked polyolefin elastomers each comprise a first polyolefin having a density less than 0.86 g/cm claim 1 , a second polyolefin claim 1 , a silane crosslinker claim 1 , a grafting initiator claim 1 , and a condensation catalyst.6. The roofing membrane of claim 5 , wherein the silane crosslinker comprises a vinyltrialkoxy silane from about 1 wt % to about 4 wt %.7. The roofing membrane of claim 5 , wherein the condensation catalyst comprises a sulfonic ester catalyst and/or a tin catalyst from about 1 wt % to ...

Подробнее
14-02-2019 дата публикации

RESIN COMPOSITION, METHOD FOR PRODUCING RESIN COMPOSITION, POWDERY MIXTURE, BIPOLAR PLATE FOR REDOX FLOW BATTERIES AND SEPARATOR FOR FUEL CELLS

Номер: US20190048108A1
Автор: KATANO Hideomi
Принадлежит: KATANOSENKAKU CO., LTD.

A resin composition containing carbon nanotubes as a component (A), an olefin based polymer that satisfies the following conditions (1) to (3) as a component (B), and a thermoplastic resin as a component (C), in which the blended amount of the component (A) is from 15 to 40% by mass with respect to 100% by mass of the total amount of the components (A) to (C), and the blended amount of the component (B) is from 0.5 to 2 times the blended amount of the component (A): (1) a weight average molecular weight (Mw) of from 35,000 to 150,000, (2) a molecular weight distribution (Mw/Mn) of 3 or less, and (3) a softening point of from 80 to 130° C. 1. A resin composition , comprising:(A) carbon nanotubes as a component (A);(B) an olefin based polymer as a component (B); and(C) a thermoplastic resin as a component (C),wherein:a blended amount of the component (A) is from 15 to 40% by mass with respect to 100% by mass of a total amount of the components (A) to (C); anda blended amount of the component (B) is from 0.5 to 2 times the blended amount of the component (A); andthe olefin based polymer (B) that satisfies the following conditions (1) to (3):(1) a weight average molecular weight (Mw) of from 35,000 to 150,000,(2) a molecular weight distribution (Mw/Mn) of 3 or less, and(3) a softening point of from 80 to 130° C.2. The resin composition according to claim 1 , further comprising:(D) a non-conductive inorganic filler as a component (D),wherein:a blended amount of the component (A) is from 5 to 35% by mass with respect to 100% by mass of a total amount of the components (A) to (D); anda blended amount of the component (D) is from 6 to 40% by mass with respect to 100% by mass of the total amount of the components (A) to (D).3. The resin composition according to claim 1 , wherein the component (C) is at least one selected from the group consisting of a polypropylene based resin claim 1 , a polymethylpentene based resin claim 1 , a syndiotactic polystyrene resin claim 1 , a ...

Подробнее
14-02-2019 дата публикации

METHOD OF PREPARING VINYL CHLORIDE-BASED POLYMER

Номер: US20190048110A1
Принадлежит:

The present invention relates to a method of preparing a vinyl chloride-based polymer, which includes inducing the nucleation of particles by adding a mercaptan-based chain transfer agent to a monomer composition including a vinyl chloride-based monomer and a preliminary polymerization initiator (preliminary polymerization); and preparing a polymer by mixing a vinyl chloride-based monomer and the particle nuclei and adding a main polymerization initiator (main polymerization). In the preparation method, a vinyl chloride-based polymer having a uniform molecular weight distribution and a desired number average molecular weight may be provided by controlling a degree of polymerization of a vinyl chloride-based polymer prepared in such a way that dispersibility is ensured by adjusting the point of time to add the mercaptan-based chain transfer agent to the point of time to reach a specific conversion rate of the preliminary polymerization. 1. A method of preparing a vinyl chloride-based polymer comprising:forming particle nuclei by adding a mercaptan-based chain transfer agent to a monomer composition including a vinyl chloride-based monomer and a preliminary polymerization initiator (preliminary polymerization); andpreparing a polymer by mixing a vinyl chloride-based monomer and the particle nuclei and adding a main polymerization initiator (main polymerization).3. The method of claim 2 , wherein the mercaptan-based chain transfer agent includes one or more selected from the group consisting of 2-mercaptoethanol claim 2 , 3-mercapto-1 claim 2 ,2-propanediol claim 2 , methyl mercaptodecanoate claim 2 , and dimethyl 9-mercaptooctadecyl-1 claim 2 ,18-dioate.4. The method of claim 1 , wherein the mercaptan-based chain transfer agent is added when a conversion rate of the preliminary polymerization is 3 to 8%.5. The method of claim 1 , wherein the mercaptan-based chain transfer agent is added in an amount of 0.01 to 0.1 parts by weight with respect to 100 parts by weight of ...

Подробнее
14-02-2019 дата публикации

FILMS, AND RELATED COMPOSITIONS AND METHODS OF MAKING

Номер: US20190048155A1
Принадлежит:

Disclosed in embodiments herein are monolayer or multilayer films. The films include at least one layer including a) a polyethylene polymer component comprising linear low density polyethylene; and b) a wax component comprising nonpolar, polyethylene wax, wherein the nonpolar, polyethylene wax has a density of 0.955 grams/cmor greater, and wherein the nonpolar, polyethylene wax is present in an amount of at least 3 percent by weight of the film. Also disclosed in embodiments herein are related compositions and methods of making monolayer or multilayer films. 1) A film comprising at least one layer , wherein the at least one layer comprises:a) a polyethylene polymer component comprising linear low density polyethylene; and{'sup': '3', 'b) a wax component comprising nonpolar, polyethylene wax, wherein the nonpolar, polyethylene wax has a density of 0.955 grams/cmor greater, and wherein the nonpolar, polyethylene wax is present in an amount from 10 to 30 percent by weight of the film.'}2) The film of claim 1 , wherein the polymer component comprises a blend of linear low density polyethylene and at least one polyethylene polymer chosen from low density polyethylene claim 1 , medium density polyethylene claim 1 , and high density polyethylene.3) (canceled)4) The film of claim 1 , wherein the nonpolar claim 1 , polyethylene wax has an acid value of 5 (mg KOH/g) or less as measured in accordance with ISO 2114 claim 1 , and/or wherein the nonpolar claim 1 , polyethylene wax has a saponification value of 5 (mg KOH/g) or less as measured in accordance with ISO 3681.5) The film of claim 1 , wherein the nonpolar claim 1 , polyethylene wax has a viscosity in the range from 100 to 30 claim 1 ,000 (mPa-s) as measured in accordance with DIN53019 at 140° C.6) The film of claim 1 , wherein the nonpolar claim 1 , polyethylene wax has a drop point in the range from 125° C. to 145° C. as measured in accordance with ASTM D 3954.7) The film of claim 1 , wherein the film has a 100% ...

Подробнее
14-02-2019 дата публикации

METHACRYLIC RESIN COMPOSITION AND INJECTION-MOLDED ARTICLE

Номер: US20190048181A1
Принадлежит: KURARAY CO., LTD.

A methacrylic resin composition comprising not less than 90% by mass of a methacrylic resin, wherein the methacrylic resin comprises 95 to 100% by mass of methyl methacrylate monomer units and 0 to 5% by mass of acrylate monomer units, the methacrylic resin has an Mw of 57000 to 90000, Mw representing a weight-average molecular weight, and a ratio Mw/Mn of not more than 1.9, Mn representing a number-average molecular weight, the methacrylic resin composition has an absolute value of a difference between YI4 and YI2 of not more than 3, YI4 representing a yellow index at an optical path length of 200 mm of an injection-molded article obtained at a cylinder temperature of 280° C. in a molding cycle of 4 minutes, YI2 representing a yellow index at an optical path length of 200 mm of an injection-molded article obtained at a cylinder temperature of 280° C. in a molding cycle of 2 minutes, and meets a relationship represented by Formula (B) and Formula (C): 2. An injection-molded article composed of the methacrylic resin composition according to .3. A board composed of the methacrylic resin composition according to and having a thickness of not more than 1 mm.4. A method for producing the methacrylic resin composition according to claim 1 , comprising bulk-polymerizing a monomer mixture comprising methyl methacrylate monomer and an acrylate monomer. The present invention relates to a methacrylic resin composition and an injection-molded article, and a production method thereof. More specifically, the present invention relates to a methacrylic resin composition that during heat forming, has excellent flowability and is less likely to be colored and an injection-molded article that has high heat resistance and high mechanical strength, and a production method thereof.Methacrylic resins have high transparency and are useful as the materials of molded articles used as optical members, lighting members, sign members, decoration members, and the like. There is a demand to ...

Подробнее
22-02-2018 дата публикации

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

Номер: US20180051110A1
Принадлежит:

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

Подробнее
23-02-2017 дата публикации

Polymer compositions comprising cross-linked polymers comprising boronic ester functions enabling exchange reactions, process for preparing them and their use

Номер: US20170051117A1

The object of the invention is a polymer compositions comprising cross-linked polymer comprising boronic ester functions enabling exchange reactions, as well as free monofunctional boronic esters. The compositions are obtained from the modification of a polymer by a functionalised boronic ester additive. This polymer can be pre-functionalised boronic ester or functionalised on addition of the said additive. In particular, the invention relates to a process enabling the behaviour of a polymer to be modified by addition of a functional additive, enabling a cross-linked network containing exchangeable boronic ester links to be formed.

Подробнее
23-02-2017 дата публикации

POLYMER COMPOSITIONS COMPRISING CROSS-LINKED POLYMERS COMPRISING BORONIC ESTER FUNCTIONS ENABLING EXCHANGE REACTIONS, PROCESS FOR PREPARING THEM AND THEIR USE

Номер: US20170051144A1

The object of the invention is a polymer compositions comprising cross-linked polymer comprising boronic ester functions enabling exchange reactions, as well as free monofunctional boronic esters. 115-. (canceled)19. A composition according to claim 18 , wherein mequals 2 claim 18 , GFPis polymerisable by polyaddition or by polycondensation.20. A composition according to claim 18 , wherein mequals 1 claim 18 , GFPis polymerisable by radical polymerisation claim 18 , by polymerisation by coordination claim 18 , or by ring-opening polymerisation.22. A composition according to claim 17 , wherein the cross-linking agent is a polymer that carries:pending boronic ester functional groups of formula (EB1) or (EB2), not containing polymerisable groups, linked to the polymer by at least one carbon atom of the dioxaborolane or dioxaborinane ring; orpending boronic ester functional groups of formula (EB1) or (EB2), not containing polymerisable groups, linked to the polymer by the boron atom of the dioxaborolane or dioxaborinane ring.23. A composition according to claim 17 , wherein the cross-linking agent is a monomer (b) boronic ester functional compound claim 17 , precursor to a thermoplastic polymer or thermoset claim 17 , comprising at least one boronic ester function per monomer and carrying at least one polymerisable group.26. A composition according to claim 23 , wherein the monomers (a) claim 23 , (b) and (c) include a single polymerisable group and the polymerisation is a radical polymerisation claim 23 , a polymerisation by coordination or a ring-opening polymerisation.27. A composition according to claim 23 , wherein the monomers (a) claim 23 , (b) and (c) include only two polymerisable groups and the polymerisation is a polyaddition or a polycondensation.28. A process comprising the copolymerisation of the following compounds:(a) Precursor monomers to thermoplastic polymers comprising at least one pending boronic ester group, said pending boronic ester group not ...

Подробнее
22-02-2018 дата публикации

BARRIER COMPOSITIONS

Номер: US20180051418A1
Автор: Hayes Peter, PROULX Robert
Принадлежит:

This disclosure relates to barrier compositions. The barrier composition can comprise a copolymer formed by polymerizing monomers comprising derived from a vinyl aromatic monomer and a second monomer selected from the group consisting of butadiene alkyl (meth)acrylates and mixtures thereof, and a solid grade oligomer. In some embodiments, the vinyl aromatic monomer and the second monomer are polymerized in the presence of the solid grade oligomer. Paper products and methods of making the paper products comprising the barrier composition are also described herein. The barrier compositions disclosed herein can be used to impart water, moisture, grease, oil, and/or oxygen resistance to the paper product. 1. A barrier composition comprising:a copolymer derived from a vinyl aromatic monomer and a second monomer selected from the group consisting of butadiene, alkyl (meth)acrylates, and mixtures thereof, anda solid grade oligomer, wherein the vinyl aromatic monomer and the second monomer are polymerized in the presence of the solid grade oligomer, anda pigment present in an amount of from 1% to 50% by weight of the barrier composition,wherein the solids in the barrier composition comprise 50% by weight or greater of the copolymer and solid grade oligomer.2. The barrier composition of claim 1 , wherein the vinyl aromatic monomer includes styrene claim 1 , alkylstyrenes claim 1 , or a combination thereof.3. The barrier composition of claim 1 , wherein the second monomer includes 2-ethylhexyl acrylate claim 1 , butyl acrylate claim 1 , ethyl acrylate claim 1 , methyl acrylate claim 1 , methyl methacrylate claim 1 , optionally a crosslinking monomer claim 1 , or a combination thereof.4. The barrier composition of claim 1 , wherein the solid grade oligomer is derived from monomers including monomers selected from the group consisting of styrene claim 1 , alkylstyrenes claim 1 , (meth)acrylic acids or salts or esters thereof claim 1 , alkoxy (meth)acrylates claim 1 , and ...

Подробнее
22-02-2018 дата публикации

MACROMOLECULAR CONJUGATES FOR VISUALIZATION AND SEPARATION OF PROTEINS AND CELLS

Номер: US20180052152A1
Принадлежит:

Macromolecular water-soluble conjugates based on synthetic copolymers to which at least one affinity tag, at least one imaging probe, and at least one targeting ligand are bound via covalent bonds. The macromolecular conjugate may be used in identification, visualization, quantification or isolation of proteins and/or cells. The targeting ligand may be attached to the synthetic copolymer via a flexible linker. 1: Synthetic macromolecular conjugate for selective interaction with proteins , characterized in that it contains a copolymer to which at least one affinity tag , at least one imaging probe and at least one targeting ligand are bound via covalent bonds.3: The macromolecular conjugate according to claim 1 , characterized in that the molecular weight of the conjugate is preferably in the range of 1000 to 500000 g/mol claim 1 , preferably in the range of 20000 to 150000 g/mol.4: The macromolecular conjugate according to claim 1 , characterized in that the targeting ligand is a moiety capable of selectively binding to the targeted protein or peptide sequence claim 1 , in particular the targeting ligand is selected from the group comprising an inhibitor or substrate of the targeted enzyme claim 1 , an agonist or antagonist of the targeted receptor claim 1 , a ligand of the targeted protein resin.5: The macromolecular conjugate according to claim 1 , characterized in that the targeting ligand may be attached to the synthetic copolymer via a flexible linker claim 1 , preferably via a flexible linker based on polyethylene glycol claim 1 , peptide claim 1 , preferably a peptide having a molecular weight from 100 to 5000 g/mol claim 1 , or nucleic acid claim 1 , preferably a nucleic acids comprising 1 to 40 nucleotides claim 1 , or oligosaccharide claim 1 , preferably an oligosaccharide containing 1 to 40 monosaccharides.6: The macromolecular conjugate according to claim 1 , characterized in that the affinity tag is selected from biotin claim 1 , His-tag claim 1 , FLAG ...

Подробнее
21-02-2019 дата публикации

KINETIC HYDRATE INHIBITORS FOR CONTROLLING GAS HYDRATE FORMATION IN WET GAS SYSTEMS

Номер: US20190055484A1
Принадлежит:

Polymers are provided for use in inhibiting gas hydrate formation and/or corrosion in hydrocarbon-containing fluids. The polymer comprises repeat units derived from a first monomer comprising N-[3-(dibutylamino)propyl]methacrylamide (DBAPAMA) or an alkyl, acetyl, acryloyl or benzyl quaternary salt thereof, N-[3-(diisobutyl)propyl]methacrylamide or an alkyl, acetyl, acryloyl or benzyl quaternary salt thereof, N-[3-(diisopentyl)propyl]methacrylamide or an alkyl, acetyl, acryloyl or benzyl quaternary salt thereof, or a combination thereof; and repeat units derived from a second monomer comprising acrylamide, N-alkylacrylamide, N-alkyl (alkyl)acrylamide, ((dialkylamino)alkyl)acrylamide or an alkyl or benzyl quaternary salt thereof, ((dialkylamino)alkyl)alkylacrylamide or an alkyl or benzyl quaternary salt thereof, acrylic acid, alkyl acrylate, N,N-(dialkylamino)alkyl acrylate or an alkyl or benzyl quaternary salt thereof, N,N-(dialkylamino)alkyl (alkyl)acrylate or an alkyl or benzyl quaternary salt thereof, hydroxyalkyl acrylate, hydroxyalkyl (alkyl)acrylate, acrylamido alkyl sulfonic acid or a salt thereof, a diallyl dialkyl quaternary ammonium salt, or a combination thereof. The second monomer does not comprise the first monomer. 1. A polymer comprising:repeat units derived from a first monomer comprising N-[3-(dibutylamino)propyl]methacrylamide (DBAPAMA) or an alkyl, acetyl, acryloyl or benzyl quaternary salt thereof, N-[3-(diisobutyl)propyl]methacrylamide or an alkyl, acetyl, acryloyl or benzyl quaternary salt thereof, N-[3-(diisopentyl)propyl]methacrylamide or an alkyl, acetyl, acryloyl or benzyl quaternary salt thereof, or a combination thereof; andrepeat units derived from a second monomer comprising acrylamide, N-alkylacrylamide, N-alkyl (alkyl)acrylamide, ((dialkylamino)alkyl)acrylamide or an alkyl or benzyl quaternary salt thereof, ((dialkylamino)alkyl)alkylacrylamide or an alkyl or benzyl quaternary salt thereof, acrylic acid, alkyl acrylate, N,N-( ...

Подробнее
01-03-2018 дата публикации

PROCESS FOR FORMING POLYOLEFINS

Номер: US20180057623A1
Принадлежит: CHEVRON PHILLIPS CHEMICAL COMPANY LP

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

Подробнее
01-03-2018 дата публикации

AMORPHOUS PROPYLENE-ETHYLENE COPOLYMERS

Номер: US20180057624A1
Принадлежит: EASTMAN CHEMICAL COMPANY

A low molecular weight copolymer is provided comprising propylene and ethylene, 1. A low molecular weight copolymer comprising propylene and ethylene ,wherein said low molecular weight copolymer has a softening point in the range of 90 to 140° C.,wherein said low molecular weight copolymer has a needle penetration that is equal to y, {'br': None, 'i': y≦−', 'x', 'x', 'x', 'x', 'x', 'x−, 'sup': 6', '5', '4', '3', '2, '0.000000262249+0.000172031278−0.046669720165+6.701746779438−537.286013331959+22,802.983472587400,204.018086126'}, 'wherein y is defined by the following formulawherein x in the above formula is the softening point of said low molecular weight copolymer,wherein said low molecular weight copolymer has a molecular weight polydispersity index of about 3 to about 25, a crystallinity of about 18% to about 30% measured by X-Ray diffraction, and a Brookfield viscosity in the range of about 1000 to about 4000 cp at 190° C. measured by ASTM D 3236.2. The low molecular weight copolymer of wherein said copolymer has a crystallinity content of about 20% to about 30%.3. The low molecular weight copolymer of wherein said copolymer has a weight average molecular weight of 25 claim 1 ,000 to 50 claim 1 ,000.4. The low molecular weight copolymer of wherein said copolymer has a weight average molecular weight of 30 claim 3 ,000 to 45 claim 3 ,000.5. The low molecular weight copolymer of wherein said copolymer has a molecular weight polydispersity index of about 8 to about 23.6. The low molecular weight copolymer of wherein said copolymer has a molecular weight polydispersity index of about 6 to about 15.7. The low molecular weight copolymer of wherein said number average molecular weight ranges from about 1 claim 1 ,000 to about 20 claim 1 ,000.8. The low molecular weight copolymer of wherein said Brookfield viscosity ranges from about 1 claim 1 ,500 to about 3 claim 1 ,000.9. The low molecular weight copolymer of wherein the storage modulus (G′) at 25° C. of said low ...

Подробнее
02-03-2017 дата публикации

POLYMER COMPOUND FOR A CONDUCTIVE POLYMER AND METHOD FOR PRODUCING SAME

Номер: US20170058059A1
Принадлежит: SHIN-ETSU CHEMICAL CO., LTD.

The present invention provides a polymer compound for a conductive polymer comprising one or more repeating units “a” shown by the formula (1), and having a weight-average molecular weight in the range of 1,000 to 500,000. There can be provided a polymer compound for a conductive polymer having a specific superacidic sulfo group which is soluble in an organic solvent, and suitably used for a fuel cell or a dopant for a conductive material. Field of the InventionThe present invention relates to a polymer compound for a conductive polymer and a method for producing the same.Description of the Related ArtA polymer containing a sulfo group has been used as a fuel cell or a dopant polymer for a conductive polymer. As a material for a fuel cell, vinylperfluoroalkyl ether sulfonic acid represented by Nafion (registered trademark) has been widely used, and as a dopant polymer for a conductive polymer, a polymer of vinylsulfonic acid or styrenesulfonic acid has been widely used (Patent Document 1).The vinylperfluoroalkyl ether sulfonic acid has chemically high stability and excellent durability, but the glass transition point thereof is low, so that there is a problem that when a fuel cell using it is exposed to high temperature, the polymer causes heat flow whereby ion conductivity thereof is lowered. A superacidic polymer having a sulfo group an α-position of which has been fluorinated is effective for enhancing the ion conductivity, but a material having high glass transition point and chemical stability with such a structure has not yet been found out.Also, a conductive polymer having a conjugated double bond such as a polythiophene, a polyaniline, a polypyrrole, etc., does not exhibit conductivity itself, but conductivity thereof is expressed by doping therein a strong acid such as sulfonic acid, etc. As the dopant, polystyrene sulfonic acid (PSS) has been most frequently used. This is because conductivity becomes the highest by doping PSS.PSS is a water-soluble resin, ...

Подробнее
02-03-2017 дата публикации

PROCESS FOR THE POLYMERISATION OF OLEFINS

Номер: US20170058064A1
Принадлежит:

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

Подробнее
02-03-2017 дата публикации

STAR POLYMERS AND COMPOSITIONS THEREOF

Номер: US20170058072A1
Принадлежит:

The invention provides a composition comprising: (a) a star polymer comprising: (i) a core portion comprising a polyvalent (meth) acrylic monomer, oligomer or polymer thereof or a polyvalent divinyl non-acrylic monomer, oligomer or polymer thereof; and (ii) at least two arms of polymerized alkyl (meth)acrylate ester; and (b) an oil of lubricating viscosity, wherein the core portion further comprises a functional group of formula (I): 1. (canceled)2. The composition of wherein the star polymer comprises greater than about 7 arms.3. The composition of wherein the star polymer comprises greater than about 10 arms.4. The composition of wherein the polyvalent (meth) acrylic monomer is an acrylic or methacrylic acid polyol or a condensation product of a polyamine.5. The composition of claim 4 , wherein the polyvalent unsaturated (meth) acrylic monomer is ethylene glycol diacrylate claim 4 , ethylene glycol dimethacrylate claim 4 , diethylene glycol diacrylate claim 4 , diethylene glycol dimethacrylate claim 4 , glycerol diacrylate claim 4 , glycerol triacrylate claim 4 , mannitol hexaacrylate claim 4 , 4-cyclohexanediol diacrylate claim 4 , 1 claim 4 ,4-benzenediol dimethacrylate claim 4 , pentaerythritol tetraacrylate claim 4 , 1 claim 4 ,3-propanediol diacrylate claim 4 , 1 claim 4 ,5-pentanediol dimethacrylate claim 4 , bis-acrylates and methacrylates of polyethylene glycols of molecular weight 200-4000 claim 4 , polycaprolactonediol diacrylate claim 4 , pentaerythritol triacrylate claim 4 , 1 claim 4 ,1 claim 4 ,1-trimethylolpropane triacrylate claim 4 , pentaerythritol diacrylate claim 4 , pentaerythritol triacrylate claim 4 , pentaerythritol tetraacrylate claim 4 , triethylene glycol diacrylate claim 4 , triethylene glycol dimethacrylate claim 4 , 1 claim 4 ,1 claim 4 ,1-trimethylolpropane trimethacrylate claim 4 , hexamethylenediol diacrylate or hexamethylenediol dimethacrylate or an alkylene bis-(meth)acrylamide.611-. (canceled)12. The composition of wherein the ...

Подробнее
02-03-2017 дата публикации

CONDUCTIVE POLYMER COMPOSITE AND SUBSTRATE

Номер: US20170058144A1
Принадлежит: SHIN-ETSU CHEMICAL CO., LTD.

The present invention provides a conductive polymer composite including: (A) a π-conjugated polymer, and (B) a dopant polymer which contains a repeating unit “a” shown by the following general formula (1) and having a weight-average molecular weight in the range of 1,000 to 500,000. There can be provided a conductive polymer composite which has excellent filterability and film-formability by spin coating, and can form a conductive film having high transparency and excellent flatness. 5. The conductive polymer composite according to claim 1 , wherein the component (B) is a block copolymer.6. The conductive polymer composite according to claim 2 , wherein the component (B) is a block copolymer.7. The conductive polymer composite according to claim 3 , wherein the component (B) is a block copolymer.8. The conductive polymer composite according to claim 4 , wherein the component (B) is a block copolymer.9. The conductive polymer composite according to claim 1 , wherein the component (A) is a polymer formed by polymerization of one or more precursor monomers selected from the group consisting of pyrrole claim 1 , thiophene claim 1 , selenophene claim 1 , tellurophene claim 1 , aniline claim 1 , a polycyclic aromatic compound claim 1 , and a derivative thereof.10. The conductive polymer composite according to claim 2 , wherein the component (A) is a polymer formed by polymerization of one or more precursor monomers selected from the group consisting of pyrrole claim 2 , thiophene claim 2 , selenophene claim 2 , tellurophene claim 2 , aniline claim 2 , a polycyclic aromatic compound claim 2 , and a derivative thereof.11. The conductive polymer composite according to claim 3 , wherein the component (A) is a polymer formed by polymerization of one or more precursor monomers selected from the group consisting of pyrrole claim 3 , thiophene claim 3 , selenophene claim 3 , tellurophene claim 3 , aniline claim 3 , a polycyclic aromatic compound claim 3 , and a derivative thereof ...

Подробнее
20-02-2020 дата публикации

Multimodal polyethylene pipe

Номер: US20200056023A1
Принадлежит: SCG Chemicals PCL, Thai Polyethylene Co Ltd

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

Подробнее
01-03-2018 дата публикации

CONDUCTIVE RESIN COMPOSITION AND ELECTRONIC CIRCUIT MEMBER USING THE SAME

Номер: US20180061519A1

The present invention relates to a conductive resin composition comprising, as essential components, a resin (A), a curing agent (B) reacting with the resin (A), and a conductive filler (C), wherein the resin (A) has a functional group, a functional group equivalent of 400 g/eq or more and 10,000 g/eq or less, a Tg (glass transition temperature) or a softening point of 40° C. or less, or an elastic modulus of less than 1.0 GPa at 30° C., and wherein the conductive filler (C) is made of a conductive material having a volume specific resistivity of 1×10Ω·cm or less at room temperature. 1. A conductive resin composition comprising , as essential components , a resin (A) , a curing agent (B) reacting with the resin (A) , and a conductive filler (C) , wherein the resin (A) has a functional group , a functional group equivalent of 400 g/eq or more and 10 ,000 g/eq or less , a Tg (glass transition temperature) or a softening point of 40° C. or less , or an elastic modulus of less than 1.0 GPa at 30° C. , and wherein the conductive filler (C) is made of a conductive material having a volume specific resistivity of 1×10Ω·cm or less at room temperature.2. The conductive resin composition according to claim 1 , wherein the resin (A) has a weight average molecular weight of 50 claim 1 ,000 or more.3. The conductive resin composition according to claim 1 , wherein the molecular structure of the resin (A) contains at least one selected from (meth)acrylic acid ester claim 1 , styrene claim 1 , and acrylonitrile as the component.4. The conductive resin composition according to claim 1 , wherein the conductive filler (C) has a flat shape claim 1 , and an aspect ratio of the thickness and the in-plane longitudinal direction is 10 or more.5. The conductive resin composition according to claim 1 , wherein the compounding ratio of the conductive filler (C) is from 40 to 95% by mass in terms of mass ratio to the total amount of the conductive resin composition.6. The conductive resin ...

Подробнее
28-02-2019 дата публикации

Pneumatic tire having tread with alkoxysilane-terminated polybutadiene

Номер: US20190062535A1
Принадлежит: Goodyear Tire and Rubber Co

The present invention is directed to a pneumatic tire comprising a tread, the tread comprising a rubber composition comprising a diene elastomer, silica, a blocked mercaptosilane, and a low molecular weight polybutadiene functionalized with an alkoxysilane functional group.

Подробнее
27-02-2020 дата публикации

Process for obtaining low volatile plastomers

Номер: US20200062876A1
Принадлежит: Borealis AG

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

Подробнее
27-02-2020 дата публикации

Process for Preparing High Melt Strength Polypropylene

Номер: US20200062880A1
Принадлежит:

The present invention relates to a polypropylene composition comprising a long chain branched polymer having high melt strength. The process for preparing the corresponding polypropylene having composition is provided comprising blending a propylene base polymer with a unsaturated polyfunctional poly(alkylsiloxane), a polyfunctional acrylate coagent, an initiator, additives such as stabilizer, acid neutralizer and antioxidants, and reactive extruding the blend to form a branched polymer composition bridged by siloxane units. 1. A method for producing a long chain branched polypropylene having high melt strength , comprising:dry blending at ambient temperature an extrusion feed, wherein the extrusion feed comprises a propylene base polymer, a branching agent, a polyfunctional acrylate, and an initiator; andreactive extruding the extrusion feed to form a long chain branched polypropylene having a melt flow rate of 0.1-25 g/10 min.2. The method of claim 1 , wherein the branching agent comprises an unsaturated polyfunctional poly(alkylsiloxane).3. The method of claim 1 , wherein the long chain branched polypropylene comprises a branched polymer bridged by siloxane units.4. The method of claim 1 , wherein the long chain branched polypropylene has a zero shear viscosity (η) of 500-200 claim 1 ,000 Pa*s.5. The method of claim 1 , wherein the dry blending is conducted at ambient temperature.6. The method of claim 2 , wherein the unsaturated polyfunctional poly(alkylsiloxane) is a vinyl terminated poly(alkylsiloxane) based homopolymer or copolymer with a molecular weight preferably in the range of 500-50 claim 2 ,000 g/mol or a vinyl content in the range of 0.01-20 wt %.7. The method of claim 6 , wherein the vinyl terminated poly(alkylsiloxane) based homopolymer or copolymer has a molecular weight in the range of 500-5 claim 6 ,000 g/mol or vinyl content in the range of 1-20 wt %.8. The method of claim 6 , wherein the vinyl terminated poly(alkylsiloxane) based homopolymer or ...

Подробнее
08-03-2018 дата публикации

PRODUCING POLYOLEFIN PRODUCTS

Номер: US20180066088A1
Принадлежит: UNIVATION TECHNOLOGIES, LLC

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

Подробнее
08-03-2018 дата публикации

VINYL CHLORIDE RESIN COMPOSITION FOR POWDER MOLDING, VINYL CHLORIDE RESIN MOLDED PRODUCT, AND LAMINATE

Номер: US20180066120A1
Автор: Nishimura Shota
Принадлежит: ZEON CORPORATION

Provided is a vinyl chloride resin composition for powder molding that can provide a molded product having low fluff adhesiveness. The vinyl chloride resin composition for powder molding contains a vinyl chloride resin (a) and a silicone oil (b) having a viscosity of at least 10 cs and no greater than 200×10cs. The content of the silicone oil (b) having a viscosity of at least 10 cs and no greater than 200×10cs is at least 0.1 parts by mass and no greater than 10 parts by mass per 100 parts by mass of the vinyl chloride resin (a). 1. A vinyl chloride resin composition for powder molding comprising:{'sup': '4', 'a vinyl chloride resin (a); and a silicone oil (b) having a viscosity of at least 10 cs and no greater than 200×10cs, wherein'}{'sup': '4', 'content of the silicone oil (b) having a viscosity of at least 10 cs and no greater than 200×10cs is at least 0.1 parts by mass and no greater than 10 parts by mass per 100 parts by mass of the vinyl chloride resin (a).'}2. The vinyl chloride resin composition for powder molding according to claim 1 , whereinthe vinyl chloride resin (a) includes vinyl chloride resin particles (a1) having an average degree of polymerization of at least 800 and no greater than 5,000, and vinyl chloride resin fine particles (a2) having an average degree of polymerization of at least 500 and no greater than 5,000,the vinyl chloride resin particles (a1) having an average degree of polymerization of at least 800 and no greater than 5,000 have a percentage content in the vinyl chloride resin (a) of at least 70 mass % and no greater than 100 mass %, andthe vinyl chloride resin fine particles (a2) having an average degree of polymerization of at least 500 and no greater than 5,000 have a percentage content in the vinyl chloride resin (a) of at least 0 mass % and no greater than 30 mass %.3. The vinyl chloride resin composition for powder molding according to claim 1 , further comprisinga plasticizer, whereincontent of the plasticizer is at least ...

Подробнее
07-03-2019 дата публикации

Sintered and Porous Articles Having Improved Flexural Strength

Номер: US20190070795A1
Принадлежит:

Polymer compositions containing polyethylene particles having a multi-modal molecular weight distribution are disclosed. The polymer compositions are well suited to producing porous substrates through a sintering process. Formulations made according to the present disclosure can produce porous substrates having improved flexibility demonstrated by an increased flexural strength while still retaining excellent pressure drop characteristics. 1. A polymer article comprising:a porous substrate comprising polyethylene particles sintered together, the polyethylene particles comprising polyethylene polymers having a multi-modal molecular weight distribution, at least 50% by weight of the polyethylene polymers having a molecular weight greater than about 3,500,000 g/mol and wherein less about 50% by weight of the polyethylene polymers having a molecular weight distribution of less than about 1,500,000 g/mol, the porous substrate having a mean pore size of from about 50 microns to about 300 microns when tested according to DIN Test 66133.2. A polymer article as defined in claim 1 , wherein the porous substrate has a flexural strength of greater than about 2 MPa.3. A polymer article as defined in claim 1 , wherein the porous substrate displays a pressure drop of less than about 10 mbar.4. A polymer article as defined in claim 1 , wherein at least 50% by weight of the polyethylene polymer has a molecular weight of greater than about 4 claim 1 ,000 claim 1 ,000 g/mol.5. A polymer article as defined in claim 1 , wherein from about 65% by weight to about 95% by weight of the polyethylene polymers have a molecular weight greater than about 4 claim 1 ,000 claim 1 ,000 g/mol.6. A polymer article as defined in claim 1 , wherein from about 75% by weight to about 85% by weight of the polyethylene polymers have a molecular weight greater than about 4 claim 1 ,000 claim 1 ,000 g/mol.7. A polymer article as defined in claim 1 , wherein less than about 50% by weight of the polyethylene ...

Подробнее
15-03-2018 дата публикации

THERMALLY STABLE SCALE INHIBITOR COMPOSITIONS

Номер: US20180072599A1
Принадлежит:

The present invention relates to a thermally stable polymeric scale inhibitor compositions and use thereof. Preferably, the polymeric scale inhibitor is a polycarboxylic acid copolymer comprising a styrene sulfonic acid group. The polymeric scale inhibitor compositions of the present invention are particularly suitable for high pressure/high temperature scale inhibition treatment of oil and gas production wells and/or subterranean formations. 1. A method for scale inhibition treatment of an operation comprising a water system comprising the step of introducing an aqueous scale inhibiting composition into the water system wherein the aqueous scale inhibiting composition comprises a polycarboxylic acid copolymer comprising the following monomers:i) one or more monoethylenically unsaturated acid and/or anhydride and/or one of its saltsandii) styrene sulfonic acid and/or one of its salts.2. The method of whereini) the one or more monoethylenically unsaturated acid and/or anhydride and/or one of its salts is acrylic acid, methacrylic acid, or mixtures thereofandii) the styrene sulfonic acid and/or one of its salts is 4-styrene sulphonic acid.3. The method of whereini) the one or more monoethylenically unsaturated acid and/or anhydride and/or one of its salts is present in an amount of 50 to 98 weight percentandii) styrene sulfonic acid and/or one of its salts is present in an amount of 2 to 50 weight percent,wherein weight percent is based on the total weight of the polymerized monomers.4. The method of wherein the polycarboxylic acid copolymer is a copolymer consisting of acrylic acid and 4-styrene sulphonic acid having a weight average weightcular weight of from 1 claim 1 ,000 to 50 claim 1 ,000 Daltons.5. The method of wherein the aqueous scale inhibiting composition is introduced by a squeeze treatment.6. The method of wherein the aqueous scale inhibiting composition is introduced by a capillary injection treatment.7. The method of wherein the operation comprising a ...

Подробнее
15-03-2018 дата публикации

FARNESENE-BASED MACROMONOMERS AND METHODS OF MAKING AND USING THE SAME

Номер: US20180072826A1
Принадлежит: FINA TECHNOLOGY, INC.

A macromonomer precursor is provided that includes a polymeric chain derived from farnesene and a single functional terminal end. The functional terminal end may include a hydroxyl group, an amino group, an epoxy group, an isocyanato group, or a carboxylic acid group. The terminal end of the macromonomer precursor may then be reacted with a (meth)acrylate to form a macromonomer having a (meth)acrylate functionalized terminal end that may be (co)polymerized with radically polymerizable monomers, such as alkyl(meth)acrylate monomers. Alternatively, a copolymer may be obtained by first deriving a poly(meth)acrylate from (meth)acrylate monomers having reactive groups that would allow the macromonomer precursors to be grafted onto the poly(meth)acrylate in a second step. The resulting copolymer may be incorporated as an additive in various formulations, such as a lubricant, a hydraulic fluid, a cosmetic composition, and an adhesive composition. 1. A macromonomer precursor comprising:a polymeric chain derived from farnesene; anda single functional terminal end selected from a hydroxyl group, an amino group, an epoxy group, an isocyanato group, and a carboxylic acid group.2. The macromonomer precursor of claim 1 , wherein the polymeric chain is less than or equal to 10% saturated.3. The macromonomer precursor of claim 1 , wherein the farnesene comprises at least 25 wt. % of the macromonomer precursor.4. The macromonomer precursor of having a weight average molecular weight of from 1 claim 1 ,000 to 100 claim 1 ,000.5. The macromonomer precursor of claim 1 , wherein the polymeric chain is derived from farnesene and monomer selected from dienes claim 1 , vinyl aromatics claim 1 , and combinations thereof.6. A copolymer derived from monomers comprising:a) radically polymerizable monomers; and a polymeric chain derived from farnesene, and', 'a (meth)acrylate functionalized terminal end., 'b) one or more macromonomers comprising'}8. The copolymer of claim 7 , wherein the ...

Подробнее
15-03-2018 дата публикации

POLYMERIZATION PROCESS IN THE PRESENCE OF ANTISTATIC AGENT

Номер: US20180072876A1
Принадлежит: BASELL POLYOLEFINE GMBH

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

Подробнее
15-03-2018 дата публикации

COMPOSITION FOR PREPARING SAN COPOLYMER, SAN COPOLYMER, PREPARATION METHOD THEREFOR, HEAT-RESISTANT ABS RESIN BLEND COMPRISING SAME, AND HEAT-RESISTANT ABS PELLETS

Номер: US20180072881A1
Принадлежит:

The present invention relates to a composition for preparing a SAN copolymer, a SAN copolymer, a preparation method therefor, a heat-resistant ABS resin blend comprising the same, and heat-resistant ABS pellets. Specifically, the present invention provides a composition for preparing a SAN copolymer, the composition comprising a monomer mixture, and ethylene glycol dimethacrylate as a chain extender, wherein the monomer mixture comprises 60 to 75 wt % of an α-methylstyrene monomer and 25 to 40 wt % of an acrylonitrile-based monomer based on the total weight of the monomer mixture; and the ethylene glycol dimethacrylate is contained in an amount of 0.001 to 0.15 parts by weight based on 100 parts by weight of the monomer mixture. 1. A composition for preparing a SAN copolymer comprising:a monomer mixture; andethylene glycol dimethacrylate as a chain extender,wherein the monomer mixture includes an α-methylstyrene monomer in an amount of 60 to 75 wt % and an acrylonitrile-based monomer in an amount of 25 to 40 wt % based on the total weight of the monomer mixture, and the ethylene glycol dimethacrylate is included in an amount of 0.001 to 0.15 parts by weight based on 100 parts by weight of the monomer mixture.2. The composition of claim 1 , wherein the ethylene glycol dimethacrylate is included in an amount of 0.03 to 0.06 parts by weight based on 100 parts by weight of the monomer mixture.3. The composition of claim 1 , wherein the composition for preparing the SAN copolymer further comprises 1 claim 1 ,1-bis(t-butylperoxy)cyclohexane as an initiator.4. The composition of claim 3 , wherein the 1 claim 3 ,1-bis(t-butylperoxy)cyclohexane is included in an amount of 0.2 to 0.35 parts by weight based on 100 parts by weight of the monomer mixture.5. A method of preparing a SAN copolymer comprising:preparing a composition for preparing a SAN copolymer,wherein the composition includes a monomer mixture and ethylene glycol dimethacrylate as a chain extender, and the monomer ...

Подробнее
24-03-2022 дата публикации

Olefin Polymer And Preparation Method Thereof

Номер: US20220089797A1
Принадлежит: LG Chem Ltd

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

Подробнее
14-03-2019 дата публикации

Polyethylene resin composition for injection-molding

Номер: US20190077892A1
Принадлежит: Lotte Chemical Corp

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

Подробнее
22-03-2018 дата публикации

CONTINUOUS GAS-PHASE POLYMERIZATION PROCESSES

Номер: US20180079842A1
Принадлежит: BASELL POLYOLEFINE GMBH

The present disclosure relates to a continuous process for the preparation of ethylene homopolymers or ethylene copolymers comprising polymerizing ethylene or copolymerizing ethylene and one or more other olefins in the presence of a chromium catalyst in a gas-phase polymerization reactor which is equipped with a cycle gas line for withdrawing reactor gas from the reactor, leading the reactor gas through a heat-exchanger for cooling and feeding the reactor gas back to the reactor, wherein the polymerization is carried out at a temperature from 30° C. to 130° C. and a pressure of from 0.1 to 10 MPa and an aliphatic carboxylic acid ester having from 8 to 24 carbon atoms is added. 1. A continuous process for the preparation of ethylene homopolymers or ethylene copolymers comprising polymerizing ethylene or copolymerizing ethylene and one or more other olefins in the presence of a chromium catalyst in a gas-phase polymerization reactor , which contains a reactor bed of particulate polymer and which is equipped with a cycle gas line for withdrawing reactor gas from the reactor , leading the reactor gas through a heat-exchanger for cooling and feeding the reactor gas back to the reactor , wherein the polymerization is carried out at a temperature from 30° C. to 130° C. and a pressure of from 0.1 to 10 MPa and an aliphatic carboxylic acid ester having from 8 to 24 carbon atoms is added.2. The process of claim 1 , wherein the aliphatic carboxylic acid ester is fed into the cycle gas system at a position upstream of the heat-exchanger.3. The process of claim 1 , wherein the cycle gas line is equipped with a cyclone upstream of the heat-exchanger and the aliphatic carboxylic acid ester is fed into the cycle gas system at a position between the reactor and the cyclone.4. The process of claim 3 , wherein the mixture of fine dust and aliphatic carboxylic acid ester which has been separated off in the cyclone is added to the polymerization product discharged from the ...

Подробнее