Method for processing polyethylene

Patent metadata

Field	Value
Publication number	US-9920172-B2
Application number	US-201214373705-A
Country	US
Kind code	B2
Filing date	Jan 24, 2012
Priority date	Jan 24, 2012
Publication date	Mar 20, 2018
Grant date	Mar 20, 2018

Abstract

A method can include consecutively batch processing at least two different polyethylene grades in pellet form in a pellet handling unit. A ratio of a melt flow index (MI) of a first polyethylene in pellet form (MI f ) to a MI of a later processed polyethylene in pellet form (MI l ) can be smaller than 0.30. The method can include processing an intermediate polyethylene grade in pellet form. An amount of intermediate polyethylene grade processed can be at most 1/100 th of a handling capacity of the pellet handling unit. The intermediate polyethylene grade can have the same MI as the later processed polyethylene in pellet form.

First claim

The invention claimed is:

1. A method of consecutively batch processing different polyethylene grades comprising:
processing a first polyethylene in pellet form in a pellet handling unit comprising one or more transfer lines and one or more homogenization silos downstream of an extruder, wherein processing the first polyethylene in pellet form comprises transferring the pellets of the first polyethylene from the extruder via the one or more transfer lines and homogenizing batches of the pellets of the first polyethylene in the one or more homogenization silos to form homogenized pellets of the first polyethylene;
after processing the pellets of the first polyethylene, processing a second polyethylene, the second polyethylene a different polyethylene than the first polyethylene, in pellet form in the pellet handling unit downstream of the extruder, wherein processing the second polyethylene in pellet form comprises transferring the pellets of the second polyethylene from the extruder via the one or more transfer lines and homogenizing batches of the pellets of the second polyethylene in the one or more homogenization silos to form homogenized pellets of the second polyethylene; and
after processing the second polyethylene, processing a later processed polyethylene in pellet form in the pellet handling unit downstream of the extruder, wherein processing the later processed polyethylene in pellet form comprises transferring the pellets of the later processed polyethylene from the extruder via the one or more transfer lines and homogenizing batches of the pellets of the later processed polyethylene in the one or more homogenization silos to form homogenized pellets of the later processed polyethylene;
wherein a ratio of a melt flow index (MI) of the first polyethylene in pellet form (MI f ) to a MI of the later processed polyethylene in pellet form (MI l ) is smaller than 0.30, wherein MI f and MI l are determined in accordance with ASTM D1238, condition E, at a temperature of 190° C. and a load of 2.16 kg;
wherein the second polyethylene has the same MI as the later processed polyethylene in pellet form; and
wherein the first polyethylene, the second polyethylene, and the later processed polyethylene are all processed in the same pellet handling unit.

2. The method according to claim 1 , wherein the consecutively batch processed polyethylene pellets are obtained from polyethylene resins produced in the presence of a metallocene catalyst.

3. The method according to claim 1 , wherein the processing of each polyethylene in pellet form comprises consecutively transferring the pellets of each polyethylene from the extruder via the one or more transfer lines.

4. The method according to claim 1 , wherein at least one of the first polyethylene and the later processed polyethylene has a monomodal molecular weight distribution.

5. The method according to claim 1 , wherein the first polyethylene and the later processed polyethylene have monomodal molecular weight distributions.

6. The method according to claim 1 , wherein the first polyethylene and the later processed polyethylene have different molecular weight distributions.

7. The method according to claim 1 , wherein the pellet handling unit is not cleaned between the processing of the first polyethylene and the later processed polyethylene.

8. The method according to claim 1 , wherein the processing of the second polyethylene in pellet form in the pellet handling unit removes substantially all remaining first polyethylene in the pellet handling unit.

9. The method according to claim 1 , wherein an amount of the second polyethylene that is processed in the pellet handling unit is at most 0.01 of a handing capacity of the pellet handling unit.

10. The method according to claim 1 , wherein from 100 kg to 2000 kg of the second polyethylene is processed in the pellet handling unit per 40 tonnes/hour handling capacity of the pellet handling unit.

11. The method according to claim 1 , wherein the pellet handling unit comprises one or more dryers.

12. The method according to claim 1 , wherein the pellet handling unit further comprises one or more storage silos, and wherein the processing of each polyethylene in pellet form further comprises consecutively storing the pellets of each polyethylene in the one or more storage silos.

13. The method according to claim 12 , wherein the pellet handling unit downstream the processing of each polyethylene in pellet form comprises:
consecutively transferring the pellets of each polyethylene from the extruder to the one or more homogenization silos via the one or more transfer lines;
consecutively homogenizing batches of the pellets of each polyethylene in the one or more homogenization silos to form homogenized pellets of each polyethylene; and
consecutively transferring the homogenized pellets of each polyethylene from the one or more homogenization silos to the one or more storage silos via the one or more transfer lines.

14. The method according to claim 1 , wherein the processing of each polyethylene in pellet form further comprises consecutively treating the pellets of each polyethylene with solids, liquids, gasses, or irradiation; consecutively adding additives to the pellets of each polyethylene; consecutively drying the pellets of each polyethylene; consecutively heating or cooling the pellets of each polyethylene; or consecutively washing the pellets of each polyethylene.

Assignees

• Stevens Peter
• Fant Franky
• Dewachter Daan
• Brusselle Alain
• Total Res & Technology Feluy

Inventors

• Stevens Peter
• Fant Franky
• Dewachter Daan
• Brusselle Alain

Classifications

• C08J3/203 Primary

  Solid polymers with solid and/or liquid additives · CPC title

• C08J2423/06

  Polyethene · CPC title

• C08J2323/16

  Ethene-propene or ethene-propene-diene copolymers · CPC title

• B29C47/0066

  Operations & Transport · mapped topic

• B29C47/0004

  Operations & Transport · mapped topic