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Isotactic polypropylene produced from supercritical polymerization process

An isotactic, propylene technology, used in the production of bulk chemicals, etc.

Inactive Publication Date: 2010-12-29
EXXONMOBIL CHEM PAT INC +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This patent does not deal with the copolymerization of propylene at much higher temperature or pressure than the above

Method used

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  • Isotactic polypropylene produced from supercritical polymerization process
  • Isotactic polypropylene produced from supercritical polymerization process
  • Isotactic polypropylene produced from supercritical polymerization process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment S0

[0179] Embodiment S01-S012: C3 monomer feed 14g / min, hexane solvent 90ml / min

Embodiment S013-S0

[0180] Embodiment S013-S022: C3 monomer feed 14g / min, hexane solvent 80ml / min

[0181] The supercooling limit (SCL) is given by SCL=0.907x-99.64, where x is Tmp.

[0182] Slurry polymerized polypropylene (comparative example)

[0183] Tables 5, 6 and 7 describe prior art bulk slurry polymerized propylene homopolymers and their preparation conditions. The technology for producing propylene homopolymers via bulk slurry polymerization is based on conventional Ziegler-Natta catalysts as well as supported Metallocene catalysts are well documented in the literature.

[0184] ACHIEVE TM 1605, 3854 and 6025G1 are commercial homopolymers made in commercial reactors available from ExxonMobil Chemical Co., Houston, TX. Slurry Examples SL1-SL4 were similar to these ACHIEVE products. They were produced in similar commercial reactors, but the process conditions were adjusted to achieve different MFR and molecular weight (Mw by GPC) values, as shown in Table 6.

[0185] Table 5. Catal...

Embodiment S

[0201] Embodiment SL5 Embodiment SL6

[0202] Catalyst feed rate (g / hr) 4.9 3.4

[0203] Scavenger (TEAL) feed rate (ml / min) 4.6 4.5

[0204] (2wt% in hexane)

[0205] Leading reactor temperature (°C) 74 74

[0206] Lead Reactor Pressure (psig) 471.6 474.6

[0207] Lead reactor C3 feed (kg / hr) 79.5 79.6

[0208] Leading reactor H2 gas concentration (mppm) 1156 2986

[0209] Tail reactor temperature (°C) 68 68

[0210] Tail reactor pressure (psig) 421.7 421.2

[0211] Tail reactor C3 feed (kg / hr) 29.5 29.5

[0212] Tail reactor H2 gas concentration (mppm) 1314 3613

[0213] Leading reactor production rate (kg / hr) 28.5 22.7

[0214] Tail reactor production rate (kg / hr) 10.7 11.8

[0215] Total production rate (kg / hr) 39.1 34.5

[0216] Leading reactor residence time (hr) 2.56 2.85

[0217] Tail reactor residence time (hr) 1.87 1.86

[0218] Total residence time (hr) 4.4 4.7

[0219] The polymer is discharged from the reactor as a...

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Abstract

This invention relates to an isotactic propylene homopolymer having: more than 15 and less than 100 regio defects (sum of 2,1-erythro and 2,1-threo insertions and 3,1-isomerizations ) per 10,000 propylene units; an Mw of 35000 g / mol or more; a peak melting temperature of greater than 149 0C; anmmmm pentad fraction of 0.85 or more; a heat of fusion of 80 J / g or more; and a peak melting temperature minus peak crystallization temperature (Tmp-Tcp) of less than or equal to (0.907 times Tmp) minus 99.64 (Tmp-Tcp < (0.907xTmp) - 99.64), as measured in 0C on the homopolymer having 0 wt% nucleating agent.

Description

[0001] Inventors: Aspy K. Mehta, Manika Varma-Nair, Gabor Kiss, Patrick Brant, Robert P. Reynolds, John W. Chu, Steven P. Rucker, and PeijunJiang technical field [0002] The present invention relates to a propylene homopolymer, preferably a propylene homopolymer prepared using a supercritical polymerization process. Background technique [0003] Metallocene catalysts have been used in high-pressure reactors since the mid-1980s, mainly for the production of ethylene-backbone polymers containing one or more of the monomers propylene, butene, and hexene Ethylene copolymers together with other specialty monomers such as 4-methyl-1,5-hexadiene. For example, US 5,756,608 (to Langhausen et al.) reports a process for the polymerization of C2-C101-alkenes using bridged metallocene catalysts. It has however been noted that the production of polypropylene under high pressure conditions is impractical and not feasible at temperatures well above the critical point of propylene. A proc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F110/06C08F2/06C08F4/6592
CPCC08F4/65908C08F110/06C08F4/65912C08F10/06C08F10/00Y02P20/54C08F4/65927C08F2/14C08F2/06C08F2500/15C08F2500/20C08F2500/03C08F2500/09C08F2500/12C08F2500/17
Inventor A·K·麦塔M·万玛-内尔G·基斯P·布兰特R·P·雷诺兹J·W·丘S·P·拉克江培军
Owner EXXONMOBIL CHEM PAT INC
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