Method for producing clean thermoplastic particles

Patent metadata

Field	Value
Publication number	US-2017198064-A1
Application number	US-201515313572-A
Country	US
Kind code	A1
Filing date	Apr 29, 2015
Priority date	May 26, 2014
Publication date	Jul 13, 2017
Grant date	—

Abstract

A process for increasing purity of a low density polyethylene (LDPE) composition, comprising the steps of: a) providing a melted composition comprising LDPE having Mn of at least 5.0 kg/mol according to size exclusion chromatography, Mw of at least 50 kg/mol according to size exclusion chromatography, a density of 915 to 935 kg/m 3 according to ISO1183 and a melt flow rate of 0.10 g/10 min to 80 g/10 min according to ISO1133:2011 measured at 190° C. and 2.16 kg, and b) providing particles from the melted composition by: b1) mixing a supercritical fluid in the melted composition to obtain a solution saturated with the supercritical fluid and b2) expanding the solution through an opening to obtain the particles.

First claim

1 . A process for increasing purity of a low density polyethylene (LDPE) composition, comprising the steps of:
a) providing a melted composition comprising LDPE having Mn of at least 5.0 kg/mol according to size exclusion chromatography, Mw of at least 50 kg/mol according to size exclusion chromatography, a density of 915 to 935 kg/m 3 according to ISO1183 and a melt flow rate of 0.10 g/10 min to 80 g/10 min according to ISO1133:2011 measured at 190° C. and 2.16 kg, and b) providing particles from the melted composition by:
b1) mixing a supercritical fluid in the melted composition to obtain a solution saturated with the supercritical fluid and
b2) expanding the solution through an opening to obtain the particles.

2 . The process according to claim 1 , wherein the supercritical fluid is selected from the group consisting of CO 2 , NH 3 , H 2 O, N 2 O, CH 4 , ethane, propane, propylene, n-butane, i-butane, n-pentane, benzene, methanol, ethanol, isopropanol, isobutanol, chlorotrifluoromethane, monofluoromethane, toluene, pyridine, cyclohexane, cyclohexanol, o-xylene, dimethyl ether and SF 6 .

3 . The process according to claim 1 , wherein the supercritical fluid is SF 6 .

4 . The process according to claim 1 , wherein the LDPE has a melt flow rate as determined using ISO1133:2011 (190° C./2.16 kg) of from 0.10 to 70 g/10 min.

5 . The process according to claim 1 , wherein the LDPE particles obtained by step b) comprises essentially no amount of low molecular weight ethylene derived polymers with 31-59 carbons as determined by mass spectrometry direct inlet probe system.

6 . The process according to claim 1 , wherein the LDPE particles obtained by step b) comprise at most 1000 ppm of low molecular weight ethylene derived polymers with 10-32 carbons as determined by programmed temperature vaporisation-gas chromatography-mass spectrometry.

7 . The process according to claim 1 , wherein the mixing is performed using a mixing element, wherein the mixing element is selected from the group consisting of a static mixer, a stirrer and an extruder.

8 . The process according to claim 1 , wherein the melted composition provided in step a) comprises at least 95 wt % of the LDPE.

9 . The process according to claim 1 , wherein step a) involves the steps of:
a1) polymerizing ethylene to obtain a composition comprising LDPE and ethylene, a2) removing ethylene from the composition of step a1) by a high pressure separator and a3) removing ethylene from the composition of step a2) by a low pressure separator to obtain the melted composition.

10 . The process according to claim 1 , wherein step a) involves the steps of providing a solid composition comprising the LDPE having Mn of at least 5.0 kg/mol according to size exclusion chromatography, Mw of at least 50 kg/mol according to size exclusion chromatography, a density of 915 to 935 kg/m 3 according to ISO1183 and a melt flow rate of 0.10 g/10 min to 80 g/10 min according to ISO1133:2011 measured at 190° C. and 2.16 kg and melting the solid composition.

11 . A process for making a master batch, comprising
forming a masterbatch of the particles produced according to the process of claim 1 , wherein the particles are not grinded.

12 . The masterbatch according to claim 11 .

13 . A process for making a carpet backing, comprising
forming a carpet backing from the particles produced according to the process of claim 1 , wherein the particles are not grinded.

14 . The carpet backing according to claim 13 .

15 . A process for increasing purity of a low density polyethylene (LDPE) composition, comprising the steps of:
a) providing a melted composition comprising at least 97 wt % LDPE having Mn of at least 5.0 kg/mol according to size exclusion chromatography, Mw of at least 50 kg/mol according to size exclusion chromatography, a density of 915 to 935 kg/m 3 according to ISO1183 and a melt flow rate of 0.10 g/10 min to 80 g/10 min according to ISO1133:2011 measured at 190° C. and 2.16 kg, by
a1) polymerizing ethylene to obtain a composition comprising LDPE and ethylene,
a2) removing ethylene from the composition of step a1) by a high pressure separator and
a3) removing ethylene from the composition of step a2) by a low pressure separator to obtain the melted composition, and
b) providing particles from the melted composition by:
b1) mixing a supercritical fluid in the melted composition to obtain a solution saturated with the supercritical fluid and
b2) expanding the solution through an opening to obtain the particles,
wherein the LDPE particles obtained by step b) comprise at most 500 ppm of low molecular weight ethylene derived polymers with 10-32 carbons as determined by programmed temperature vaporisation-gas chromatography-mass spectrometry.

16 . The process according to claim 15 , wherein the LDPE particles obtained by step b) comprises essentially no amount of low molecular weight ethylene derived polymers with 31-59 carbons as determined by mass spectrometry direct inlet probe system.

17 . The process according to claim 15 , wherein the LDPE has a melt flow rate as determined using ISO1133:2011 (190° C./2.16 kg) of 0.10 to 50 g/10 min.

Assignees

• Sabic Global Technologies Bv

Inventors

• Castaneda Zuniga Diego Mauricio
• Neuteboom Peter
• Duchateau Jan Nicolaas Eddy
• Knez Zeljko

Classifications

• C08F6/005

  from solid polymers · CPC title

• C08F6/003 Primary

  from polymer solutions, suspensions, dispersions or emulsions without recovery of the polymer therefrom · CPC title

• C08J2323/06

  Polyethene · CPC title

• C08F6/12

  Separation of polymers from solutions · CPC title

• Y02P20/54

  using solvents, e.g. supercritical solvents or ionic liquids · CPC title