Nova Chemicals (international) S.a.

Nova Chemicals Inc.

Stephen John Brown

Rupert Edward Von Haken Spence

Xiaoliang Gao

Peter Zoricak

Qinyan Wang

XiaoChuan Wang

Brian Molloy

Lawrence VanAsseldonk

Norman Aubee

Fazle Sibtain

Kenneth Edward Taylor

Stephen Salomons

Hamidreza Khakdaman

Niousha Kazemi

Monika Kleczek

Mehdi Keshtkar

Zengrong Zhang

Charles Carter

Christopher Dobbin

Peter Phung Minh Hoang

Cliff Baar

Cliff Robert Baar

Peter Phung Hoang

Victoria Ker

Cheng Fan

Steven Clemens

Paul Mesquita

Oleksiy Golovchenko

Stephen J Brown

P Scott Chisholm

Eric Clavelle

Norman Dorien Joseph Aubee

Wei Xu

Mohamed Aiffa

Holly Ann Severin

Gail Baxter

Holly Kalma

Marissa Clapson

Rupert Edward Spence

Kevin Dickinson

Charles Ashton Carter

Norman Dorien Aubee

Charles A Carter

Charles A G Carter

Holly Severin

Joanna Ronne Newman

Quiyan Wang

Lawrence Vanasseldonk

A polyethylene composition which when made into a film layer having a thickness of about 1 mil has a machine direction (MD) 1% secant modulus of ≥200 MPa and an oxygen transmission rate (OTR) of ≥600 cmper 100 inchper day and when made into a film layer having a thickness of about 2 mil has a seal initiation temperature (SIT) of ≤90° C. and an area of hot tack window (AHTW) of ≥160 Newtons·° C.

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

The copolymerization of ethylene with an optional comonomer is conducted in the presence of a catalyst having a specific aryloxy ether ligand structure. The process enables very high conversions of ethylene to polyethylene at very short residence times when conducted under conditions of pressures of at least 10.3 MPa and high ethylene feed concentrations of from 70 to 150 grams per liter. Using these polymerization conditions, the level of unsaturation may be controlled by the polymerization temperature: for example, a level of 0.09 vinyl groups per 1000 carbon atoms was observed at a polymerization temperature of 160° C. and a level of 0.22 vinyls per 1000 carbon atoms was observed at 220° C.

Control of unsaturation in polymers produced in solution process

The copolymerization of ethylene with an optional comonomer is conducted in the presence of a catalyst having a specific aryloxy ether ligand structure. The process enables very high conversions of ethylene to polyethylene at very short residence times when conducted under conditions of pressures of at least 10.3 MPa and high ethylene feed concentrations of from 70 to 150 grams per liter.

High productivity polymerization with aryloxy ether ligand catalyst

The copolymerization of ethylene with a cyclic mono olefin (such as norbornene) is conducted in the presence of a catalyst system comprising a bridged hafnocene catalyst and a three part activator. The catalyst system provides excellent activity at high polymerization temperatures. Copolymers produced according to this invention have unique microstructure (with methyl branching being observed) and unique rheology.

Ethylene-cyclic mono olefin copolymerizations

A polyethylene composition including a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution M/Mof &#x3c;2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 50,000 to 200,000 and a molecular weight distribution M/Mof &#x3c;2.3, and a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 70,000 to 200,000 and a molecular weight distribution M/Mof &#x3c;2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene.

Polyethylene composition and film having outstanding properties

A thermoformable film comprises a polyethylene composition. The polyethylene composition comprises a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution M/Mof &#x3c;2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 15,000 to 100,000 and a molecular weight distribution M/Mof &#x3c;2.3, and a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution M/Mof &#x3e;2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene. The polyethylene composition has a melt flow ratio (I/I) of &#x2264;50 and an area Dimensional Thermoformability Index (aDTI) at 105&#xb0; C. of less than 15.

Thermoformable film

A thermoformable film including a polyethylene composition. The polyethylene composition includes a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution M/Mof &#x3c;2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of less than 75,000 and a molecular weight distribution M/Mof &#x3c;2.3, a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of less than 75,000 and a molecular weight distribution M/Mof &#x3c;2.3, and a fourth polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 100,000 to 250,000 and a molecular weight distribution M/Mof &#x3e;2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene. The polyethylene composition has a melt flow ratio (I/I) of &#x2264;55 and an area Dimensional Thermoformability Index (aDTI) at 105&#xb0; C. of less than 15.

This invention relates to a self cleaning reactor and to a process for the oligomerization of ethylene that employs a self-cleaning reactor. The reactor includes a mass of inert, particulate cleaning bodies that are entrained by the liquid in the reactor and scour the internal surfaces of the reactor during normal operation. This scouring action reduces the level of fouling on the reactor surfaces. Foulant material (polyethylene) is removed from the process on a continuous basis but the cleaning bodies remain within the reactor.

Self cleaning reactor system

A polyethylene composition includes a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution Mw/Mn of &#x3c;2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 15,000 to 100,000 and a molecular weight distribution Mw/Mn of &#x3c;2.3, and a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution Mw/Mn of &#x3e;2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene. The polyethylene composition has a soluble fraction in a CEF analysis of at least 10 weight percent. Film made from the polyethylene composition may have a machine direction 1% secant modulus of &#x25a1;190 MPa (at a film thickness of about 1 mil), a seal initiation temperature (SIT) of &#x2264;100&#xb0; C. (at a film thickness of about 2 mil), an area of hot tack window (AHTW) of &#x2265;160 Newtons&#xb7;C&#xb0; (at a film thickness of about 2 mil) and an oxygen transmission rate (OTR) of &#x2265;650 cm3 per 100 inch2 per day (at a film thickness of about 1 mil).

Polyethylene composition and film having a good permeability, stiffness and sealability

A polyethylene composition comprises a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution M/Mof &#x3c;2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 50,000 to 200,000 and a molecular weight distribution M/Mof &#x3c;2.3, and a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 70,000 to 200,000 and a molecular weight distribution M/Mof &#x3c;2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene. The polyethylene composition has a composition distribution breadth index, CDBIobtained from a crystallization elution fractionation (CEF) analysis of &#x3c;45 weight %. A film made from the polyethylene composition may have a machine direction 1% secant modulus of &#x2265;200 MPa (at a film thickness of about 1 mil), a seal initiation temperature (SIT) of &#x2264;85&#xb0; C. (at a film thickness of about 2 mil), an area of hot tack window (AHTW) of &#x2265;220 Newtons&#xb7;C&#xb0; (at a film thickness of about 2 mil), an oxygen transmission rate (OTR) of &#x2265;600 cmper 100 inchper day (at a film thickness of about 1 mil), a dart impact strength of &#x2265;400 g/mil, and a machine direction (MD) tear strength of &#x2265;400 g/mil.

A polyethylene composition includes a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution M/Mof &#x3c;2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 15,000 to 100,000, a molecular weight distribution M/Mof &#x3e;2.3, and a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution M/Mof &#x3e;2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene. The polyethylene composition has a soluble fraction in a CEF analysis of at least 10 weight percent. Film made from the polyethylene composition may have a machine direction 1% secant modulus of 200 &#x2265;MPa (at a film thickness of about 1 mil), a seal initiation temperature (SIT) of &#x2264;90&#xb0; C. (at a film thickness of about 2 mil), an area of hot tack window (AHTW) of &#x2265;160 Newtons&#xb7;C&#xb0; (at a film thickness of about 2 mil) and an oxygen transmission rate (OTR) of &#x2265;600 cmper 100 inch per day (at a film thickness of about 1 mil).

A polyethylene composition including a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution M/Mof &#x3c;2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of less than 75,000 and a molecular weight distribution M/Mof &#x3c;2.3, and a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 100,000 to 300,000 and a molecular weight distribution M/Mof &#x3e;2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene. The polyethylene composition has a soluble fraction in a CEF analysis of at least 15 weight percent. A film made from the polyethylene composition may have a machine direction 1% secant modulus of &#x2265;200 MPa (at a film thickness of about 1 mil) and an oxygen transmission rate (OTR) of &#x2265;700 cmper 100 inchper day (at a film thickness of about 1 mil). A film made from the polyethylene composition retains much of its dart impact performance on downgauging from a thickness of 1 mil to a thickness of 0.75 mil.

Polyethylene composition and film having retained dart impact

In some embodiments disclosed herein are polyethylene composition including a first polyethylene which is an ethylene copolymer having a weight average molecular weight of from 70,000 to 250,000 and a molecular weight distribution M/Mof &#x3c;2.3, a second polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of less than 75,000 and a molecular weight distribution M/Mof &#x3c;2.3, a third polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of less than 75,000 and a molecular weight distribution M/Mof &#x3c;2.3, and a fourth polyethylene which is an ethylene copolymer or homopolymer having a weight average molecular weight of from 100,000 to 250,000 and a molecular weight distribution M/Mof &#x3e;2.3, where the first polyethylene has more short chain branching than the second polyethylene or the third polyethylene. The polyethylene composition may have a soluble fraction in a CEF analysis of at least 7.5 weight percent. Film made from the polyethylene composition may have a machine direction 1% secant modulus of 200 MPa (at a film thickness of about 1 mil) and an oxygen transmission rate (OTR) of &#x2265;550 cmper 100 inch per day (at a film thickness of about 1 mil). Film made from the polyethylene composition retains much of its dart impact performance on downgauging from a thickness of 1 mil to a thickness of 0.75 mil.

Polyethylene composition and film

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

Off-line filter free Ziegler-Natta catalyst preparation

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Calgary, Canada

Peter Zoricak