US5283300A
Expired / Lapsed
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Process for preparing polyolefin fluff using metallocene catalyst
Assignee: TotalEnergies Onetech Belgium SA
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Filing: 1990-11-05
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Granted: 1994-02-01
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Expires: 2010-11-05
Abstract
Abstract Olefin polymers and copolymers having controlled morphology are prepared by bulk or slurry polymerization using metallocene catalysts in the presence of an alumoxane cocatalyst. Prepolymerization at a temperature of -10° C. to +35° C. during 1.5 to 3.5 minutes is immediately followed by polymerization at 55°-70° C. The fluff has a narrow grain size distribution, a smooth surface and a high bulk density.
Inventors
- 👤 Luc Haspeslagh
- 👤 Eric Maziers
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 17:33
CPC Classifications
C; C08; C08F; C08F10/00; C08F4/00; C08F4/42; C08F4/44; C08F4/60; C08F4/62; C08F4/64; C08F4/659; C08F4/65912; C08F4/6592; Y; Y10; Y10S; Y10S526/00; Y10S526/943
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
265 words
Process for the preparation of olefin polymers and copolymers having controlled morphology by bulk or slurry polymerization, comprising the steps of: (i) providing a homogeneous non-supported system comprising a metallocene transition metal catalysts of general formula (Cp) m R n MQ k wherein each Cp is a cyclopentadienyl or a cyclopentadienyl substituted by one or more hydrocarbyl radical having from 1 to 20 carbon atoms, R is a structural bridge between two Cp rings, M is a transition metal selected from groups 4 or 5, Q is a hydride or a hydrocarbyl group having from 1 to 20 carbon atoms or an alkenyl group having from 2 to 20 carbon atoms or a halogen, m=1-3 with the proviso that if m=2 or 3 each Cp may be the same or different, n=0 or 1 with the proviso that n=0 if m=1, and k is such that the sum of m+k is equal to the oxidation state of M with the proviso that if k is greater than 1 each Q may be the same or different, and an alumoxane cocatalyst; and (ii) prepolymerizing said homogeneous system in the present of at least one olefin for a period of from 1.5 to 3.5 minutes and at a temperature of from -10° to +35° C.; (iii) introducing said prepolymerized system either into at least one olefin in the liquid state for bulk polymerization or into an inert liquid hydrocarbon containing at least one olefin for slurry polymerization, the polymerization being carried out at a temperature of from 55° C. to 70° C.; and (iv) recovering polyolefin fluff.
Claim 2
Dependent Claim
265 words
Process for the preparation of olefin polymers and copolymers having controlled morphology by bulk or slurry polymerization, comprising the steps of: (i) providing a homogeneous non-supported system comprising a metallocene transition metal catalysts of general formula (Cp) m R n MQ k wherein each Cp is a cyclopentadienyl or a cyclopentadienyl substituted by one or more hydrocarbyl radical having from 1 to 20 carbon atoms, R is a structural bridge between two Cp rings, M is a transition metal selected from groups 4 or 5, Q is a hydride or a hydrocarbyl group having from 1 to 20 carbon atoms or an alkenyl group having from 2 to 20 carbon atoms or a halogen, m=1-3 with the proviso that if m=2 or 3 each Cp may be the same or different, n=0 or 1 with the proviso that n=0 if m=1, and k is such that the sum of m+k is equal to the oxidation state of M with the proviso that if k is greater than 1 each Q may be the same or different, and an alumoxane cocatalyst; and (ii) prepolymerizing said homogeneous system in the present of at least one olefin for a period of from 1.5 to 3.5 minutes and at a temperature of from -10° to +35° C.; (iii) introducing said prepolymerized system either into at least one olefin in the liquid state for bulk polymerization or into an inert liquid hydrocarbon containing at least one olefin for slurry polymerization, the polymerization being carried out at a temperature of from 55° C. to 70° C.; and (iv) recovering polyolefin fluff.
Claim 3
Dependent Claim
18 words
Process according to claim 1, wherein M is selected from the group consisting of Ti, Zr and Hf.
Claim 4
Dependent Claim
29 words
Process according to claim 1, wherein m=2, n=1, the first Cp is cyclopentadienyl, the second Cp is fluorenyl, and R is a 2,2-propanediyl bridge linking the two Cp rings.
Claim 5
Dependent Claim
9 words
Process according to claim 1, wherein Q is chlorine.
Claim 6
Dependent Claim
10 words
Process according to claim 1, wherein the olefin is propylene.
Claim 7
Dependent Claim
21 words
Process according to claim 1, wherein the prepolymerization step is carried out for a period of from 2 to 3 minutes.
Claim 8
Dependent Claim
22 words
Process according to claim 1, wherein the prepolymerization step is carried out at a temperature of from +10° C. to +25° C.
Claim 9
Dependent Claim
19 words
Process according to claim 1, wherein the polymerization step is carried out at a temperature of about 60° C.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1997-01-31 | 1997-08-02 | 1998-02-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2001-01-31 | 2001-08-02 | 2002-02-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2005-01-31 | 2005-08-02 | 2006-02-01 | $7700.00 | Window Closed / Lapsed |