๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

Kinetic Study of Ethylene Polymerization Over Supported Bis(imino)pyridine Iron (II) Catalysts

โœ Scribed by Artem A. Barabanov; Gennady D. Bukatov; Vladimir A. Zakharov; Nina V. Semikolenova; Tatiana B. Mikenas; Ljudmila G. Echevskaja; Michail A. Matsko


Publisher
John Wiley and Sons
Year
2006
Tongue
English
Weight
146 KB
Volume
207
Category
Article
ISSN
1022-1352

No coin nor oath required. For personal study only.

โœฆ Synopsis


Abstract

Summary: The number of active centers (C~P~) and propagation rate constants (k~P~) for polymerization of ethylene with supported catalysts LFeCl~2~/SiO~2~, LFeCl~2~/Al~2~O~3~ and LFeCl~2~/MgCl~2~ (Lโ€‰=โ€‰2,6โ€(2,6โ€(Me)~2~C~6~H~3~N๏ฃพCMe)~2~C~5~H~3~N), activated by an Al(iโ€Bu)~3~ coโ€catalyst, were determined by a method of polymerization inhibition with radioactive ^14^CO. In contrast to homogeneous systems based on LFeCl~2~, the supported catalysts are highly active and stable in ethylene polymerization at 70โ€“80โ€‰ยฐC. In the presence of hydrogen, the activity of the supported catalysts substantially increases (2โ€“4 fold). The data obtained on the effect of hydrogen on the calculated C~P~ and k~P~ values suggests that for ethylene polymerization without hydrogen, the โ€œdormantโ€ active centers are formed in the catalytic systems. A scheme for the formation of these โ€œdormantโ€ centers and their reactivation in presence of hydrogen is suggested. For the investigated supported catalysts the C~P~ values were found to be only 2 to 4% of the total iron complex content in the catalysts. The k~P~ value for the catalysts prepared using different supports (SiO~2~, Al~2~O~3~ and MgCl~2~) were close (3.2โ€‰ร—โ€‰10^4^ to 4.5โ€‰ร—โ€‰10^4^ Lโ€‰ยทโ€‰(molโ€‰ยทโ€‰s)^โˆ’1^ at 70โ€‰ยฐC). The support composition affects neither the molecular mass (MM) nor the molecular mass distribution (MMD) of the polymers produced. The obtained C~P~ and k~P~ values and data on the polymer MM and MMD lead to conclusion that the nature of the support has almost no effect on the structure of the active centers and the distribution of their reactivity.

Effect of support on the MMD of PE produced over supported LFeCl~2~ catalysts.

magnified imageEffect of support on the MMD of PE produced over supported LFeCl~2~ catalysts.


๐Ÿ“œ SIMILAR VOLUMES


Kinetic Peculiarities of Ethylene Polyme
โœ Artem A. Barabanov; Gennady D. Bukatov; Vladimir A. Zakharov; Nina V. Semikoleno ๐Ÿ“‚ Article ๐Ÿ“… 2005 ๐Ÿ› John Wiley and Sons ๐ŸŒ English โš– 125 KB

## Abstract Summary: Method of polymerization inhibition by radioactive carbon monoxide (^14^CO) has been used to determine the number of active centers (__C__~P~) and propagation rate constant (__k__~P~) for ethylene polymerization with homogeneous complex 2,6โ€(2,6โ€(Me)~2~C~6~H~3~N๏ฃพCMe)~2~C~5~H~3~

Modeling of Ethylene Polymerization Kine
โœ Kyu Yong Choi; Shihua Tang; Won Jung Yoon ๐Ÿ“‚ Article ๐Ÿ“… 2004 ๐Ÿ› John Wiley and Sons ๐ŸŒ English โš– 168 KB

## Abstract **Summary:** Silica supported chromium oxide catalysts have been used for many years to manufacture polyethylene and they still account for more than 50% of world production of highโ€density polyethylene. Along with its commercial success, the catalytic mechanism and polymerization kinet

Ethylene Polymerization over Homogeneous
โœ Artem A. Barabanov; Gennady D. Bukatov; Vladimir A. Zakharov; Nina V. Semikoleno ๐Ÿ“‚ Article ๐Ÿ“… 2008 ๐Ÿ› John Wiley and Sons ๐ŸŒ English โš– 175 KB

## Abstract The number of active centers (__C__~P~) and propagation rate constant (__k__~P~) for ethylene polymerization with homogeneous catalyst LCoCl~2~โ€‰+โ€‰MAO and supported catalyst LCoCl~2~/SiO~2~โ€‰+โ€‰Al(__i__โ€Bu)~3~, where L is 2,6โ€(2,6โ€(Me)~2~C~6~H~3~Nโ€‰=โ€‰CMe)~2~C~5~H~3~N, have been determined u

Introducing a Flat Model of the Silica-S
โœ Wei Han; Christian Mรผller; Dieter Vogt; Hans (J. W.) Niemantsverdriet; Peter C. ๐Ÿ“‚ Article ๐Ÿ“… 2006 ๐Ÿ› John Wiley and Sons ๐ŸŒ English โš– 214 KB

## Abstract **Summary:** A wellโ€defined flat model of a supported homogeneous polyolefin catalyst is prepared on the basis of an immobilized bis(imino)pyridyl iron complex on a super flat silica surface. The amount of supported catalyst precursor is quantified using XPS. This model catalyst remains