IP Library Granted Patent US 7,511,109
Granted Patent B2
US 7,511,109 · App. 10/513,173 · Granted Mar 31, 2009

Rotomoulding polyethylene and method for producing said rotomoulding polyethylene

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Quick Facts
Patent No.
US 7,511,109
App. No.
10/513,173
Granted
Mar 31, 2009
Kind
B2
Abstract

A method for producing rotomoulding polyethylene by fluidized bed gas phase polymerisation of ethylene and the improved rotomoulding polyethylene obtainable by the process.

Claims (15)

1. A process for producing polyethylene for rotomoulding, having a density A of from 930 to 944 kg/m 3 and a melt index B of from 3 to 7.8 g/10 min, by (co-)polymerization of ethylene in a fluidised bed gas phase reactor, said process comprising

determining the instantaneous density d and melt index MI of the polyethylene powder exiting a fluidized bed gas phase reactor,

allowing the density and melt index to vary around their A and B values by a value of plus or minus 3 kg/m 3 for the density and plus or minus 30% for the melt index,

wherein the operating temperature is controlled such that

a.) an RTSE factor is first maintained in an operating envelope corresponding to the d and MI values of the polyethylene produced, and

b.) then the RTSE factor is maintained between 4.2 and 4.4.

2. The process according to claim 1 , wherein the density and melt index are respectively allowed to vary around their A and B values by a value of plus or minus 2 kg/m 3 for the density and plus or minus 15% for the melt index.

3. The process according to claim 1 or 2 , wherein the RTSE factor is allowed to vary only by plus or minus 0.07 across the operating envelope(s), said variation occurring within a minimum of 4 hours of operation.

4. The process according to claim 3 , wherein the RTSE variation is only allowed within a minimum of 8 hours of operation.

5. The process according to claims 3 , wherein the RTSE factor is allowed to vary only by plus or minus 0.05 across the operating envelope(s).

6. The process according to claim 1 , wherein the process is applied during product grade transition between two polyethyenes for rotomoulding.

7. The process according claim 1 , wherein the polyethylene is a copolymer of ethylene and hex-1-ene.

8. The process according to claim 1 , wherein the polyethylene for rotomoulding has a density of from 933 to 941 kg/m 3 and a melt index of from 3 to 7 g/10 min.

9. A polyethylene for rotomoulding produces by the process of claim 1 , and having a density of from 930 to 944 kg/m 3 , a melt index according to ASTM-D-1238, condition A (2.16 kg) of from 3 to 7.8 g/10 min, an ESCR property according to ASTM-D-1693 equal or higher than 400 h and a Charpy property equal or higher than 10 kJ/m 2 .

10. A hex-1-ene copolymer of ethylene having a density of from 930 to 944 kg/m 3 and a melt index according to ASTM-D-1238, condition A (2.16 kg) of from 3 to 7.8 g/10 min, an ESCR property according to ASTM-D-1693 equal or higher than 400 h and a Charpy property equal or higher than 10 kJ/m 2 .

Assignments (5)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 4, 2011
From: INEOS EUROPE LIMITED
To: INEOS COMMERCIAL SERVICES UK LIMITED
Reel/Frame 027060/0001 →
CORRECTIVE ASSIGNMENT TO CORRECT ERRONEOUS SERIAL NO. 10/513,713. THE CORRECT SERIAL NO. IS 10/513,173 (PREVIOUSLY RECORDED AT REEL 021192, FRAME 0001). Recorded Feb 23, 2009
From: INNOVENE EUROPE LIMITED
To: INEOS EUROPE LIMITED
Reel/Frame 022296/0260 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 30, 2008
From: BP CHEMICALS LIMITED
To: O&D TRADING LIMITED
Reel/Frame 021191/0969 →
CHANGE OF NAME Recorded Jun 30, 2008
From: O & D TRADING LIMITED
To: INNOVENE EUROPE LIMITED
Reel/Frame 021191/0994 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 13, 2008
From: ARNOUX, JACQUES; CERMELLI, ISABELLE; MEURICE, ESTELLE; SELO, JEAN-LOIC
To: BP CHEMICALS LIMITED
Reel/Frame 020973/0758 →