High drawdown extrusion process with greater resistance to draw resonance
AssigneeThe Dow Chemical Company
InventorsTodd J. Obijeski, Shih-Yaw Lai, Rajen M. Patel, Lichih R. Peng, Michael F. Langohr, David C. Kelley, David A. Eversdyk, Nicole F. Whiteman
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Abstract
A process for extruding a thermoplastic composition at higher drawdown rates with less neck-in and greater resistance to draw resonance as well as processes for extrusion coating a substrate and for making an extrusion-cast film are disclosed. The thermoplastic composition is made of at least one substantially linear ethylene polymer used alone or in combination with at least one high-pressure ethylene polymer and/or with at least one heterogeneous linear olefin polymer.
Claims19
In a process for extrusion coating a substrate or for making a cast film with a thermoplastic composition, comprising the steps of:
- (i) feeding a thermoplastic composition into at least one extruder,
- (ii) melting and mixing the thermoplastic composition to form at least one uniform molten polymer stream, and
- (iii) extruding the molten polymer stream through a die to form a primary web,
- the improvement comprising:
- (i) operating said extruder at line speeds greater than 152 meters/minute, and either
- (a) drawing down said web onto said substrate to thereby coat said substrate with at least one layer of said thermoplastic composition, or
- (b) cooling and drawing down said web onto a take-off device to make said film with at least one layer of said thermoplastic composition,
- (ii) conveying or collecting said coated substrate or said film for subsequent use, and
- (iii) using as said thermoplastic composition:
- (I) from about 10 to 100 percent by weight of at least one substantially linear ethylene polymer characterized as having:
- (a) a melt flow ratio, I.sub.10 /I.sub.2,.gtoreq.5.63,
- (b) a molecular weight distribution, M.sub.w /M.sub.n, defined by the equation:
- M.sub.w /M.sub.n .ltoreq.(I.sub.10 /I.sub.2)-4.63,
- (c) a critical shear rate at the onset of surface melt fracture of at least 50 percent greater than the critical shear rate at the onset of surface melt fracture of a linear olefin polymer having about the same I.sub.2 and M.sub.w /M.sub.n, and
- (d) a single melting peak as determined using differential scanning calorimetry;
- and
- (II) from 0 to about 90 percent by weight of at least one polymer selected from the group consisting of a heterogeneous linear ethylene polymer and high pressure ethylene polymer.
The process defined in claim I wherein (I) is a copolymer of ethylene and one C.sub.3 -C.sub.20 .alpha.-olefin.
The process defined in claim I wherein the Dow Rheology Index (DRI) of (I) is at least 0.1.
Dependencies are inferred from the claim text.