RU98108397A - POLYOLEPHINE COMPOSITIONS WITHOUT STITCHING - Google Patents
POLYOLEPHINE COMPOSITIONS WITHOUT STITCHINGInfo
- Publication number
- RU98108397A RU98108397A RU98108397/04A RU98108397A RU98108397A RU 98108397 A RU98108397 A RU 98108397A RU 98108397/04 A RU98108397/04 A RU 98108397/04A RU 98108397 A RU98108397 A RU 98108397A RU 98108397 A RU98108397 A RU 98108397A
- Authority
- RU
- Russia
- Prior art keywords
- composition
- composition according
- molecular weight
- ethylene
- polymer
- Prior art date
Links
- 239000000203 mixture Substances 0.000 title claims 32
- 229920000642 polymer Polymers 0.000 claims 10
- 238000009826 distribution Methods 0.000 claims 9
- 150000001336 alkenes Chemical class 0.000 claims 8
- 238000005227 gel permeation chromatography Methods 0.000 claims 8
- 229920000573 polyethylene Polymers 0.000 claims 7
- 229920000098 polyolefin Polymers 0.000 claims 7
- 125000004432 carbon atoms Chemical group C* 0.000 claims 4
- 239000003431 cross linking reagent Substances 0.000 claims 4
- 239000005977 Ethylene Substances 0.000 claims 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims 3
- 125000000217 alkyl group Chemical group 0.000 claims 2
- 230000000875 corresponding Effects 0.000 claims 2
- 238000004132 cross linking Methods 0.000 claims 2
- 238000000034 method Methods 0.000 claims 2
- 238000010408 sweeping Methods 0.000 claims 2
- 239000012190 activator Substances 0.000 claims 1
- 125000004423 acyloxy group Chemical group 0.000 claims 1
- 125000001931 aliphatic group Chemical group 0.000 claims 1
- 125000003545 alkoxy group Chemical group 0.000 claims 1
- 125000004104 aryloxy group Chemical group 0.000 claims 1
- 239000007789 gas Substances 0.000 claims 1
- 125000004435 hydrogen atoms Chemical group [H]* 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 239000000155 melt Substances 0.000 claims 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims 1
- 125000000962 organic group Chemical group 0.000 claims 1
- 125000001820 oxy group Chemical group [*:1]O[*:2] 0.000 claims 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 claims 1
- BLRPTPMANUNPDV-UHFFFAOYSA-N silane Chemical group [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 claims 1
- 150000004756 silanes Chemical class 0.000 claims 1
- 239000000725 suspension Substances 0.000 claims 1
- 239000004711 α-olefin Substances 0.000 claims 1
Claims (23)
Mn1/Mn2 > 7,0; Mn2 > 3000 и
0,7 ≥ A1/(A1 + A2) ≥ 0,15
где A1, A2, Mn1 и Mn2 являются производными молекулярно-массового распределения композиции, полученного методом гель-проникающей хроматографии путем развертки относительного ответа (RR) в зависимости от молекулярной массы (MW) для того, чтобы RR и MW удовлетворяли следующей зависимости, которая представляет собой взвешенную сумму двух функций логарифмически нормального распределения:
с использованием методики нелинейной регрессии для получения параметров A1, A2, μ1, μ2, σ1 и σ2, в которых MW представляет собой значение молекулярной массы по данным гель-проникающей хроматографии (ГПХ); RR - это относительный ответ, который для набора индивидуальных данных RR/MW представляет собой: RR[i] = Нормализованная высота [i] / (log (MW[i - 1]) - log (MW[i])),
где Нормализованная высота [i] является выходным сигналом ГПХ для соответствующей фракции MW[i];
μ1 и σ
μ2 и σ
A1 + A2 = 1 и 0 < A1 < 1;
Mn1= 10μ1exp(-0,5(ln(10)×σ1)2) и
Mn2= 10μ2exp(-0,5(ln(10)×σ2)2);
и полиолефиновая композиция имеет суммарную плотность менее 0,907 г/см3.1. Polyolefin composition containing two or more components of olefin polymers, and this composition satisfies the following conditions:
M n1 / M n2 >7.0; M n2 > 3000 and
0.7 ≥ A 1 / (A 1 + A 2 ) ≥ 0.15
where A 1 , A 2 , M n1 and M n2 are derivatives of the molecular weight distribution of the composition obtained by gel permeation chromatography by sweeping the relative response (RR) depending on the molecular weight (MW) so that RR and MW satisfy the following dependence, which is a weighted sum of two functions of a lognormal distribution:
using non-linear regression techniques to obtain the parameters A 1 , A 2 , μ 1 , μ 2 , σ 1 and σ 2 , in which MW is the molecular weight value according to gel permeation chromatography (GPC); RR is a relative answer, which for a set of individual data, RR / MW is: RR [i] = Normalized height [i] / (log (MW [i - 1]) - log (MW [i])),
where Normalized height [i] is the GPC output for the corresponding MW [i] fraction;
μ 1 and σ
μ 2 and σ
A 1 + A 2 = 1 and 0 <A 1 <1;
M n1 = 10 μ1 exp (-0.5 (ln (10) × σ 1 ) 2 ) and
M n2 = 10 μ2 exp (-0.5 (ln (10) × σ 2 ) 2 );
and the polyolefin composition has a total density of less than 0.907 g / cm 3 .
(Mw/Mn ≅ (I10/I2) - 4,63,
где отношение индексов течения расплава (I10/I2) равно или больше 5,63.9. The composition of claim 8, in which each of the substantially linear ethylene polymers has a molecular weight distribution (M w / M n ) defined by the formula:
(M w / M n ≅ (I 10 / I 2 ) - 4.63,
where the ratio of the melt flow indices (I 10 / I 2 ) is equal to or greater than 5.63.
в которой R' представляет собой атом водорода или метильную группу; x и y являются нулем или 1, при условии, что когда x равно 1, y = 1; n - это целое число от 1 до 12, включая, предпочтительно, от 1 до 4; и каждый R независимо представляет собой гидролизуемую органическую группу, такую как алкокси-группа, имеющая 1 - 12 атомов углерода, арилокси-группа, аралокси-группа, алифатическая ацилокси-группа, имеющая от 1 до 12 атомов углерода, оксимо- или замещенная амино-группа, или низшая алкильная группа, имеющая 1 - 6 атомов углерода включительно, при условии, что не более чем три группы R являются алкилами.13. The composition according to item 12, in which the unsaturated silane is represented by the formula
in which R 'represents a hydrogen atom or a methyl group; x and y are zero or 1, provided that when x is 1, y = 1; n is an integer from 1 to 12, including, preferably, from 1 to 4; and each R independently represents a hydrolyzable organic group, such as an alkoxy group having 1 to 12 carbon atoms, an aryloxy group, an araloxy group, an aliphatic acyloxy group having from 1 to 12 carbon atoms, an oxy or substituted amino a group or lower alkyl group having 1 to 6 carbon atoms inclusive, provided that no more than three R groups are alkyl.
Mn1/Mn2 > 7,0; Mn2 > 3000 и
0,7 ≥ A1/(A1 + A2) ≥ 0,15
где A1, A2, Mn1 и Mn2 являются производными молекулярно-массового распределения композиции, полученного методом гель-проникающей хроматографии путем развертки относительного ответа (RR) в зависимости от молекулярной массы (MW) для того, чтобы RR и MW удовлетворяли следующей зависимости, которая представляет собой взвешенную сумму двух функций логарифмически нормального распределения:
с использованием методики нелинейной регрессии для получения параметров A1, A2, μ1, μ2, σ1 и σ2, в которых MW представляет собой значение молекулярного веса по данным гель-проникающей хроматографии (ГПХ); RR - это относительный ответ, который для набора индивидуальных данных RR/MW представляет собой: RR[i] = Нормализованная высота [i] / (log (MW[i - 1]) - log (MW[i])), где Нормализованная высота [i] является выходным сигналом ГПХ для соответствующей фракции MW[i]; μ1 и σ
A1 + A2 = 1 и 0 < A1 < 1;
Mn1= 10μ1exp(-0,5(ln(10)×σ1)2) и
Mn2= 10μ2exp(-0,5(ln(10)×σ2)2);
и полиолефиновая композиция имеет суммарную плотность менее 0,907 г/см3.17. A method for producing a polyolefin composition, which comprises a) preparing a first olefin polymer and a second olefin polymer; b) mixing the first and second olefin polymers so that the first and second olefin polymers are mixed homogeneously to form a polyolefin composition that satisfies the following conditions:
M n1 / M n2 >7.0; M n2 > 3000 and
0.7 ≥ A 1 / (A 1 + A 2 ) ≥ 0.15
where A 1 , A 2 , M n1 and M n2 are derivatives of the molecular weight distribution of the composition obtained by gel permeation chromatography by sweeping the relative response (RR) depending on the molecular weight (MW) so that RR and MW satisfy the following dependence, which is a weighted sum of two functions of a lognormal distribution:
using non-linear regression techniques to obtain the parameters A 1 , A 2 , μ 1 , μ 2 , σ 1 and σ 2 , in which MW is the molecular weight value according to gel permeation chromatography (GPC); RR is the relative answer, which for a set of individual data, RR / MW is: RR [i] = Normalized height [i] / (log (MW [i - 1]) - log (MW [i])), where Normalized height [i] is the GPC output for the corresponding MW [i] fraction; μ 1 and σ
A 1 + A 2 = 1 and 0 <A 1 <1;
M n1 = 10 μ1 exp (-0.5 (ln (10) × σ 1 ) 2 ) and
M n2 = 10 μ2 exp (-0.5 (ln (10) × σ 2 ) 2 );
and the polyolefin composition has a total density of less than 0.907 g / cm 3 .
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/538,689 US5795941A (en) | 1995-10-03 | 1995-10-03 | Crosslinkable bimodal polyolefin compositions |
US08/538,689 | 1995-10-03 |
Publications (2)
Publication Number | Publication Date |
---|---|
RU98108397A true RU98108397A (en) | 2000-02-10 |
RU2173324C2 RU2173324C2 (en) | 2001-09-10 |
Family
ID=24148001
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU98108397/04A RU2173324C2 (en) | 1995-10-03 | 1996-10-02 | Polyolefin compositions capable of being cross linked |
Country Status (17)
Country | Link |
---|---|
US (2) | US5795941A (en) |
EP (1) | EP0853643B1 (en) |
JP (1) | JP3782459B2 (en) |
KR (1) | KR100445938B1 (en) |
CN (1) | CN1117810C (en) |
AR (1) | AR003770A1 (en) |
AU (1) | AU704844B2 (en) |
BR (1) | BR9611582A (en) |
CA (1) | CA2227279C (en) |
DE (1) | DE69612560T2 (en) |
ES (1) | ES2155946T3 (en) |
MY (1) | MY113524A (en) |
NO (1) | NO319083B1 (en) |
RU (1) | RU2173324C2 (en) |
TW (1) | TW368512B (en) |
WO (1) | WO1997012934A1 (en) |
ZA (1) | ZA968278B (en) |
Families Citing this family (59)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6399708B2 (en) * | 1993-07-19 | 2002-06-04 | Visteon Systemes Interieurs S.A.S. | Grafted and crosslinkable pulverulent thermoplastic polyolefin composition which has elasticity and flexibility properties |
AR012814A1 (en) * | 1996-01-22 | 2000-11-22 | Dow Chemical Co | DIFFERENT CRYSTALLINE POLYOLEFIN MIXTURES, PROCEDURE FOR OBTAINING MOLDED ITEMS WITH SUCH MIXTURES AND MOLDED ITEMS OBTAINED |
US6395839B2 (en) * | 1996-04-01 | 2002-05-28 | Visteon Systemes Interieurs S.A.S. | Grafted and crosslinkable pulverulent thermoplastic polyolefin composition which has elasticity and flexibility properties |
EP0870803A1 (en) * | 1997-04-07 | 1998-10-14 | Phillips Petroleum Company | A process to produce a crosslinked composition that comprises polymers that comprise ethylene and a crosslinked composition that comprises polymers that comprise ethylene |
US5986002A (en) * | 1997-12-05 | 1999-11-16 | Becton, Dickinson And Company | Medical article of improved sterilizability |
EP1388570B1 (en) * | 1998-10-30 | 2009-08-26 | Mitsui Chemicals, Inc. | Crosslinked olefin elastomer foam and elastomer composition therefor |
JP3727010B2 (en) * | 2000-07-14 | 2005-12-14 | 西川ゴム工業株式会社 | Manufacturing method of weather strip for automobile and glass run |
US6548600B2 (en) * | 2000-09-22 | 2003-04-15 | Dupont Dow Elastomers L.L.C. | Thermoplastic elastomer compositions rheology-modified using peroxides and free radical coagents |
US6455602B1 (en) * | 2000-10-24 | 2002-09-24 | Union Carbide Chemicals & Plastics Technology Corporation | High-speed processable cellular insulation material with enhanced foamability |
MY137183A (en) * | 2001-03-16 | 2009-01-30 | Dow Global Technologies Inc | Method of making interpolymers and products made therefrom |
US20040124554A1 (en) * | 2002-09-23 | 2004-07-01 | Toray Plastics (America), Inc. | Polyolefin isolation membrane |
EP2261292B1 (en) | 2002-10-15 | 2014-07-23 | ExxonMobil Chemical Patents Inc. | Polyolefin adhesive compositions |
US7700707B2 (en) | 2002-10-15 | 2010-04-20 | Exxonmobil Chemical Patents Inc. | Polyolefin adhesive compositions and articles made therefrom |
KR100469470B1 (en) * | 2003-01-30 | 2005-02-02 | 엘지전자 주식회사 | Damper using thermal transformation and washing machine having the same |
MXPA06000916A (en) * | 2003-07-24 | 2006-05-04 | Union Carbide Chem Plastic | Cable insulation system with flexibility, high temperature deformation resistance, and reduced degree of stickiness. |
US6870010B1 (en) | 2003-12-01 | 2005-03-22 | Univation Technologies, Llc | Low haze high strength polyethylene compositions |
US7288596B2 (en) | 2003-12-22 | 2007-10-30 | Univation Technologies, Llc | Polyethylene compositions having improved tear properties |
US7193017B2 (en) * | 2004-08-13 | 2007-03-20 | Univation Technologies, Llc | High strength biomodal polyethylene compositions |
EP1634896A1 (en) * | 2004-09-10 | 2006-03-15 | Borealis Technology Oy | Polymer composition |
EP1634913B1 (en) * | 2004-09-10 | 2008-10-29 | Borealis Technology Oy | Semiconductive polymer composition |
US7557301B2 (en) | 2004-09-28 | 2009-07-07 | Southwire Company | Method of manufacturing electrical cable having reduced required force for installation |
US10763008B2 (en) | 2004-09-28 | 2020-09-01 | Southwire Company, Llc | Method of manufacturing electrical cable, and resulting product, with reduced required installation pulling force |
US7749024B2 (en) | 2004-09-28 | 2010-07-06 | Southwire Company | Method of manufacturing THHN electrical cable, and resulting product, with reduced required installation pulling force |
US7312279B2 (en) * | 2005-02-07 | 2007-12-25 | Univation Technologies, Llc | Polyethylene blend compositions |
JP2006258122A (en) * | 2005-03-15 | 2006-09-28 | Ntn Corp | Slide type constant velocity universal joint |
EP1834987B1 (en) * | 2006-03-15 | 2015-08-12 | Borealis Technology Oy | Method for the production of a polypropylene composition with selective cross-linkable dispersed phase |
US20070264512A1 (en) * | 2006-05-11 | 2007-11-15 | Mehta Sameer D | Extrusion coating process for improved adhesion to metal(lized) substrates |
KR101433138B1 (en) * | 2006-12-27 | 2014-09-25 | 시바 홀딩 인코포레이티드 | Multifilament, monofilament, non-woven or tape |
US8800967B2 (en) | 2009-03-23 | 2014-08-12 | Southwire Company, Llc | Integrated systems facilitating wire and cable installations |
US8138264B2 (en) * | 2007-05-04 | 2012-03-20 | Fina Technology, Inc. | Bimodal polyethylene resins that have high stiffness and high ESCR |
KR101152413B1 (en) * | 2008-09-12 | 2012-06-05 | 에스케이이노베이션 주식회사 | Ethylene copolymer and a method of preparing the same |
US8986586B2 (en) | 2009-03-18 | 2015-03-24 | Southwire Company, Llc | Electrical cable having crosslinked insulation with internal pulling lubricant |
DE102009002559A1 (en) * | 2009-04-22 | 2010-10-28 | Robert Bosch Gmbh | sensor arrangement |
EP2256159A1 (en) * | 2009-05-26 | 2010-12-01 | Borealis AG | Polymer composition for crosslinked pipes |
US8658576B1 (en) | 2009-10-21 | 2014-02-25 | Encore Wire Corporation | System, composition and method of application of same for reducing the coefficient of friction and required pulling force during installation of wire or cable |
US10325696B2 (en) | 2010-06-02 | 2019-06-18 | Southwire Company, Llc | Flexible cable with structurally enhanced conductors |
US9126353B2 (en) * | 2010-11-03 | 2015-09-08 | Ineos Olefins & Polymers Usa | Method and apparatus for making polyolefin pellets |
WO2012067777A2 (en) * | 2010-11-19 | 2012-05-24 | Exxonmobil Chemical Patents Inc. | Processes for making multimodal molecular weight distribution polyolefins |
KR20180107291A (en) * | 2011-02-04 | 2018-10-01 | 다우 글로벌 테크놀로지스 엘엘씨 | Cross-linkable polyolefin composition for formed textured skin applications |
US9352371B1 (en) | 2012-02-13 | 2016-05-31 | Encore Wire Corporation | Method of manufacture of electrical wire and cable having a reduced coefficient of friction and required pulling force |
EP2703528A1 (en) * | 2012-08-31 | 2014-03-05 | baumhueter extrusion GmbH | Cross-linked polyethylene fibre, its use and process for its manufacture |
US11328843B1 (en) | 2012-09-10 | 2022-05-10 | Encore Wire Corporation | Method of manufacture of electrical wire and cable having a reduced coefficient of friction and required pulling force |
US10056742B1 (en) | 2013-03-15 | 2018-08-21 | Encore Wire Corporation | System, method and apparatus for spray-on application of a wire pulling lubricant |
WO2014209256A1 (en) | 2013-06-24 | 2014-12-31 | Dow Global Technologies Llc | Reinforced polypropylene composition |
US10431350B1 (en) | 2015-02-12 | 2019-10-01 | Southwire Company, Llc | Non-circular electrical cable having a reduced pulling force |
WO2018013285A1 (en) | 2016-07-14 | 2018-01-18 | Exxonmobil Chemical Patents Inc. | Dual metallocene-catalyzed bimodal copolymer compositions |
SG11201903393RA (en) * | 2016-11-08 | 2019-05-30 | Univation Tech Llc | Bimodal polyethylene |
RU2020100898A (en) * | 2017-06-29 | 2021-07-14 | Дау Глоубл Текнолоджиз Ллк | WATER-COOLED WIRE AND CABLE CONSTRUCTIONS |
EP3692079B1 (en) | 2017-10-06 | 2024-09-04 | ExxonMobil Chemical Patents Inc. | Polyethylene extrudates and methods of making the same |
CN107624515A (en) * | 2017-10-24 | 2018-01-26 | 建瓯市元润塑料有限公司 | Black fungus open air cultivating bacteria bag and its preparation and application method |
US10995166B2 (en) | 2017-11-07 | 2021-05-04 | Nova Chemicals (International) S.A. | Ethylene interpolymer products and films |
US10683376B2 (en) | 2017-11-07 | 2020-06-16 | Nova Chemicals (International) S.A. | Manufacturing ethylene interpolymer products at higher production rate |
CA3097342A1 (en) | 2018-04-27 | 2019-10-31 | Dow Global Technologies Llc | Non-foam polyolefin compositions for wire and cable coating |
US11629245B2 (en) | 2018-06-28 | 2023-04-18 | Exxonmobil Chemical Patents Inc. | Polyethylene compositions, wire and cables, and methods for making the same |
JP2022512506A (en) | 2018-12-17 | 2022-02-04 | アルケマ フランス | Mulch (meth) acrylate functionalized resin as a cross-linking aid for thermoplastic polymers |
CN109771722A (en) * | 2019-01-22 | 2019-05-21 | 西安乐析医疗科技有限公司 | A kind of novel peritoneum dialysis tubing |
US11325999B2 (en) | 2019-09-30 | 2022-05-10 | Exxonmobil Chemical Patents Inc. | High pressure polyethylene tubular reactor processes for improved wire coating product |
EP3831590A1 (en) | 2019-12-05 | 2021-06-09 | Lapmaster Wolters GmbH | Press ram for a fine blanking press |
CN114163763B (en) * | 2021-12-27 | 2023-12-22 | 复旦大学 | Polyethylene compound capable of thermoplastic processing |
Family Cites Families (47)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3280220A (en) * | 1963-04-29 | 1966-10-18 | Phillips Petroleum Co | Blend of high density polyethylene-1-butene copolymer |
CA849081A (en) * | 1967-03-02 | 1970-08-11 | Du Pont Of Canada Limited | PRODUCTION OF ETHYLENE/.alpha.-OLEFIN COPOLYMERS OF IMPROVED PHYSICAL PROPERTIES |
BE794718Q (en) * | 1968-12-20 | 1973-05-16 | Dow Corning Ltd | OLEFINS CROSS-LINKING PROCESS |
US3914342A (en) * | 1971-07-13 | 1975-10-21 | Dow Chemical Co | Ethylene polymer blend and polymerization process for preparation thereof |
GB2007685B (en) * | 1977-10-11 | 1982-05-12 | Asahi Dow Ltd | Composition for drawn film cold drawn film made of said composition and process for manufacture of said film |
US4302565A (en) * | 1978-03-31 | 1981-11-24 | Union Carbide Corporation | Impregnated polymerization catalyst, process for preparing, and use for ethylene copolymerization |
US4335034A (en) * | 1978-12-18 | 1982-06-15 | J. P. Stevens & Co., Inc. | Thermoplastic compositions and automotive carpeting backed therewith |
JPS5734145A (en) * | 1980-08-07 | 1982-02-24 | Mitsui Petrochem Ind Ltd | Ethylene-alpha-olefin copolymer composition |
US4403007A (en) * | 1980-08-11 | 1983-09-06 | E. I. Du Pont De Nemours & Co. | Filled thermoplastic compositions based on ethylene interpolymers and polyester, polyether and polyether ester plasticizers |
US4339507A (en) * | 1980-11-26 | 1982-07-13 | Union Carbide Corporation | Linear low density ethylene hydrocarbon copolymer containing composition for extrusion coating |
US4438238A (en) * | 1981-01-30 | 1984-03-20 | Sumitomo Chemical Company, Limited | Low density copolymer composition of two ethylene-α-olefin copolymers |
US4461873A (en) * | 1982-06-22 | 1984-07-24 | Phillips Petroleum Company | Ethylene polymer blends |
US4525257A (en) * | 1982-12-27 | 1985-06-25 | Union Carbide Corporation | Low level irradiated linear low density ethylene/alpha-olefin copolymers and film extruded therefrom |
US4500648A (en) * | 1983-04-25 | 1985-02-19 | Exxon Research & Engineering Co. | Long chain branching in polyolefins from ziegler-natta catalysts |
US4530914A (en) * | 1983-06-06 | 1985-07-23 | Exxon Research & Engineering Co. | Process and catalyst for producing polyethylene having a broad molecular weight distribution |
US4937299A (en) * | 1983-06-06 | 1990-06-26 | Exxon Research & Engineering Company | Process and catalyst for producing reactor blend polyolefins |
US4540753A (en) * | 1983-06-15 | 1985-09-10 | Exxon Research & Engineering Co. | Narrow MWD alpha-olefin copolymers |
US4786697A (en) * | 1983-06-15 | 1988-11-22 | Exxon Research & Engineering Co. | Molecular weight distribution modification in a tubular reactor |
IL75719A (en) * | 1984-07-18 | 1988-11-30 | Du Pont Canada | Polyolefin blends containing reactive agents |
US4614764A (en) * | 1985-03-06 | 1986-09-30 | Mobil Oil Corporation | Linear low density ethylene polymers blended with modified linear low density ethylene polymers |
US4701432A (en) * | 1985-11-15 | 1987-10-20 | Exxon Chemical Patents Inc. | Supported polymerization catalyst |
US4798081A (en) * | 1985-11-27 | 1989-01-17 | The Dow Chemical Company | High temperature continuous viscometry coupled with analytic temperature rising elution fractionation for evaluating crystalline and semi-crystalline polymers |
FR2592051B1 (en) * | 1985-12-24 | 1988-10-14 | Charbonnages Ste Chimique | COMPOSITIONS OF ETHYLENE POLYMERS, A PROCESS FOR THEIR PREPARATION AND THEIR APPLICATION FOR OBTAINING INDUSTRIAL ARTICLES |
US4939217A (en) * | 1987-04-03 | 1990-07-03 | Phillips Petroleum Company | Process for producing polyolefins and polyolefin catalysts |
US5382631A (en) * | 1988-09-30 | 1995-01-17 | Exxon Chemical Patents Inc. | Linear ethylene interpolymer blends of interpolymers having narrow molecular weight and composition distributions |
US5371143A (en) * | 1989-11-16 | 1994-12-06 | Minnesota Mining And Manufacturing Company | Polymer blend composition of fluorinated elastomers, thermoplastic polymers and thermoplastics elastomers |
GB8927174D0 (en) * | 1989-12-01 | 1990-01-31 | Exxon Chemical Patents Inc | Cross-linkable polymer blends |
US5272236A (en) * | 1991-10-15 | 1993-12-21 | The Dow Chemical Company | Elastic substantially linear olefin polymers |
JP3045548B2 (en) * | 1990-12-28 | 2000-05-29 | 日本石油化学株式会社 | Polyethylene composition |
US5089321A (en) * | 1991-01-10 | 1992-02-18 | The Dow Chemical Company | Multilayer polyolefinic film structures having improved heat seal characteristics |
US5278272A (en) * | 1991-10-15 | 1994-01-11 | The Dow Chemical Company | Elastic substantialy linear olefin polymers |
JP3157163B2 (en) * | 1991-12-30 | 2001-04-16 | ザ・ダウ・ケミカル・カンパニー | Polymerization of ethylene interpolymer |
US5210142A (en) * | 1992-02-13 | 1993-05-11 | The Dow Chemical Company | Reduction of melt fracture in linear polyethylene |
GB9215821D0 (en) * | 1992-07-24 | 1992-09-09 | Exxon Chemical Patents Inc | Thermoplastic compositions and processes for cross-linking |
US5414040A (en) * | 1992-09-15 | 1995-05-09 | The Dow Chemical Company | Formulated ethylene/α-olefin elastomeric compounds |
CA2103380C (en) * | 1992-11-19 | 2002-07-02 | Mitsui Chemicals, Inc. | Ethylene/.alpha.-olefin copolymer composition, graft modified ethylene/.alpha.-olefin copolymer composition, ethylene copolymer composition, and multi-stage olefin polymerization process |
PT681592E (en) * | 1993-01-29 | 2001-01-31 | Dow Chemical Co | ETHYLENE INTERPOLIMERIZATIONS |
US5470993A (en) * | 1993-06-24 | 1995-11-28 | The Dow Chemical Company | Titanium(II) or zirconium(II) complexes and addition polymerization catalysts therefrom |
US5408004A (en) * | 1993-08-17 | 1995-04-18 | The Dow Chemical Company | Polyolefin blends and their solid state processing |
US5387630A (en) * | 1993-08-31 | 1995-02-07 | Eastman Chemical Company | Polyolefin-extrusion coating compositions having good coatability, good adhesion to the substrate, and good chill roll release |
JP3398451B2 (en) * | 1994-01-14 | 2003-04-21 | 積水化学工業株式会社 | Crosslinked polyolefin resin foam |
AU688500B2 (en) * | 1994-04-20 | 1998-03-12 | Dow Chemical Company, The | Silane-crosslinkable, substantially linear ethylene polymers and their uses |
US5773106A (en) * | 1994-10-21 | 1998-06-30 | The Dow Chemical Company | Polyolefin compositions exhibiting heat resistivity, low hexane-extractives and controlled modulus |
US5589539A (en) * | 1994-11-23 | 1996-12-31 | Union Carbide Chemicals & Plastics Technology Corporation | Process for preparing an in situ polyethylene blend |
US5492760A (en) * | 1994-12-05 | 1996-02-20 | At Plastics Inc. | Water tree resistant, moisture curable insulation composition for power cables |
US5578682A (en) * | 1995-05-25 | 1996-11-26 | Exxon Chemical Patents Inc. | Bimodalization of polymer molecular weight distribution |
ID17196A (en) * | 1996-03-14 | 1997-12-11 | Dow Chemical Co | ADHESIVE INGREDIENTS THAT CONTAIN OLEFIN POLYMER |
-
1995
- 1995-10-03 US US08/538,689 patent/US5795941A/en not_active Expired - Lifetime
-
1996
- 1996-08-26 US US08/703,263 patent/US5852116A/en not_active Expired - Lifetime
- 1996-10-02 RU RU98108397/04A patent/RU2173324C2/en not_active IP Right Cessation
- 1996-10-02 AR ARP960104575A patent/AR003770A1/en unknown
- 1996-10-02 CN CN96197436A patent/CN1117810C/en not_active Expired - Lifetime
- 1996-10-02 ES ES96937652T patent/ES2155946T3/en not_active Expired - Lifetime
- 1996-10-02 EP EP96937652A patent/EP0853643B1/en not_active Expired - Lifetime
- 1996-10-02 WO PCT/US1996/015863 patent/WO1997012934A1/en active IP Right Grant
- 1996-10-02 AU AU75141/96A patent/AU704844B2/en not_active Ceased
- 1996-10-02 ZA ZA9608278A patent/ZA968278B/en unknown
- 1996-10-02 DE DE69612560T patent/DE69612560T2/en not_active Expired - Lifetime
- 1996-10-02 JP JP51441997A patent/JP3782459B2/en not_active Expired - Lifetime
- 1996-10-02 MY MYPI96004071A patent/MY113524A/en unknown
- 1996-10-02 CA CA002227279A patent/CA2227279C/en not_active Expired - Lifetime
- 1996-10-02 KR KR10-1998-0702042A patent/KR100445938B1/en not_active IP Right Cessation
- 1996-10-02 BR BR9611582A patent/BR9611582A/en not_active IP Right Cessation
- 1996-12-09 TW TW085115216A patent/TW368512B/en active
-
1998
- 1998-04-02 NO NO19981493A patent/NO319083B1/en not_active IP Right Cessation
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