Method for predicting physical properties of polyethylene resin, and production method of polyethylene resin
US-11492423-B2 · Nov 8, 2022 · US
US9289935B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9289935-B2 |
| Application number | US-201214116087-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 8, 2012 |
| Priority date | May 10, 2011 |
| Publication date | Mar 22, 2016 |
| Grant date | Mar 22, 2016 |
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A process for homogenizing and pelletizing a polyethylene composition comprising the steps of a) providing a polyethylene composition having a density of from 0.90 g/cm 3 to 0.97 g/cm 3 and a melt flow rate MFR 21.6 at 190° C. under a load of 21.6 kg of from 1 g/10 min to 80 g/10 min, b) melting the polyethylene composition; c) passing the melt through a combination of screens consisting of screens having a mesh opening of at least 205 μm and comprising at least two screens having a mesh opening of from 205 μm to 350 μm; and e) pelletizing the molten polyethylene composition, the use of a polyethylene composition obtained by such a process for the preparation of films, fibers, pipes, blow-molded articles, injection-molded articles, compression-molded articles or rotomolded articles and films, fibers, pipes, blow-molded articles, injection-molded articles, compression-molded articles or rotomolded articles prepared from a polyethylene composition obtained by such a process.
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What is claimed is: 1. A process for homogenizing and pelletizing a polyethylene composition comprising the steps of: a) providing a polyethylene composition having a density of from 0.955 g/cm 3 to 0.97 g/cm 3 , a polydispersity index M w /M n , in the range of from 15 to 40, and a melt flow rate MFR 21.6 at 190_° C. under a load of 21.6 kg of from 5 g/10 min to 25 g/10 min; b) melting the polyethylene composition; c) passing the melt through a combination of screens consisting of a first screen having a mesh opening of 210 μm and at least five screens having a mesh opening of from 210 μm to 250 μm; and e) pelletizing the molten polyethylene composition. 2. A process for homogenizing and pelletizing a polyethylene composition according to claim 1 further comprising one or more steps of mixing the melt of the polyethylene composition before or after passing the melt through the combination of screens. 3. A process for homogenizing and pelletizing a polyethylene composition according to claim 1 , wherein the polyethylene composition is bimodal or multimodal. 4. A process for homogenizing and pelletizing a polyethylene composition according to claim 1 , wherein polyethylene composition is an ethylene copolymer of ethylene with 1-butene, 1-pentene, 1-hexene and/or 1-octene. 5. A process for homogenizing and pelletizing a polyethylene composition according to claim 1 , wherein polyethylene composition is obtained by polymerizing in suspension or in gas-phase at temperatures in the range of from −20° C. to 200° C., and under pressures of from 0.1 MPa to 20 MPa. 6. A process for homogenizing and pelletizing a polyethylene composition according to claim 1 , wherein the polyethylene composition is obtained by polymerizing in a cascade of at least two polymerization reactors. 7. A process for homogenizing and pelletizing a polyethylene composition according to claim 1 wherein the polyethylene composition is obtained by polymerizing using a mixed catalyst system. 8. The process of claim 1 comprising forming an article, wherein the article is a film, fiber, pipe, blow-molded article, injection molded article, compression molded article or rotomolded article comprising the polyethylene composition resulting from step e).
Treatment of polymers prepared in bulk {also solid polymers or polymer melts, (C08F6/001, C08F6/006, C08F6/008, C08F6/02, C08F6/04 take precedence)} · CPC title
Operations & Transport · mapped topic
Operations & Transport · mapped topic
Polyethylene · CPC title
High density, i.e. > 0.95 g/cm3 · CPC title
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