نتایج جستجو برای: Ziegler-Natta Catalyst

تعداد نتایج: 45447  

Journal: Polyolefins Journal 2016

A novel imido-modified SiO2-supported Ti/Mg Ziegler-Natta catalyst for ethylene and ethylene/1-hexene polymerization is investigated. The catalyst is prepared by modification of (SiO2/MgO/MgCl2)TiClx Ziegler-Natta catalysts via supporting vanadium species followed by reaction with p-tolyl isocyanate as imido agents, to get the merits from both the SiO2-supported imido vanadium catalyst and the ...

Journal: :Proceedings of the National Academy of Sciences of the United States of America 2006
Seong H Kim Gabor A Somorjai

This article reviews the surface science of the heterogeneous olefin polymerization catalysts. The specific focus is on how to prepare and characterize stereochemically specific heterogeneous model catalysts for the Ziegler-Natta polymerization. Under clean, ultra-high vacuum conditions, low-energy electron irradiation during the chemical vapor deposition of model Ziegler-Natta catalysts can be...

Journal: :polyolefins journal 2014
maria marques renato oliveira rafael araujo bruno amantes

a fourth-generation ziegler-natta catalyst was prepared to synthesize polypropylene (pp), which was stabilized by in situ polymerization employing lignin as antioxidant. the antioxidant properties of lignin were compared with those of the commercial antioxidant irganox 1010. the presence of lignin in the reaction medium slightly decreased the catalytic activity of the reaction. the isotacticity...

ژورنال: :فصلنامه علمی- ترویجی بسپارش 2015
رضا بازوند نعیمه بحری مهدی نکومنش حسین عابدینی

فعالیت کاتالیزور از مهم ترین پارامترها در فرایندهای پلیمرشدن است. برای یک سامانه کاتالیزوریفعالیت ممکن است به شرایط پلیمرشدن از قبیل دما و فشار وابسته باشد. با این حال، برای شرایط ثابتپلیمرشدن، افزایش فعالیت به روش تغییر دما و فشار رضایت بخش نیست و صنعتگران مجبورند تا مقدارکاتالیزور در راکتور یا زمان انجام پلیمرشدن را افزایش دهند که این کار نیز از لحاظ اقتصادی مقرونبه صرفه نیست. در سال های اخیر...

Journal: :The Journal of the Society of Chemical Industry, Japan 1970

Journal: :علوم و تکنولوژی پلیمر 0
علی فرهنگیان کاشانی حسین عابدینی محمدرضا کلایی

a linear low density polyethylene (lldpe) production process, including two- fuidized bed reactors in series (fbrs) and other process equipment, was completely simulated by aspen polymer plus software. fluidized bed reactors were considered as continuous stirred tank reactors (cstr consisted of polymer and gas phases). poly-srk and nrtl-rk equations of state were used to describe polymer and no...

Journal: :علوم و تکنولوژی پلیمر 0
محمد سلطانیه احمد رمضانی سعادت آبادی علی دشتی جعفر مختاری

in this article, a complete model for the mixed flow slurry reactor for polymerization of ethylene to high density polyethylene in the presence of ziegler-natta catalyst is presented. in addition to the effects of the multiple active sites, the effect of other important parameters such as the catalyst concentration, co-catalyst, hydrogen, monomer, impurities and pressure on the mass-average and...

Journal: :علوم و تکنولوژی پلیمر 0
مهشید مشهدی حسن شیرازی رضا مرندی مهدی سلامی کلجاهی وحید حدادی اصل سید مهدی قافله باشی زرند

in this study, the slurry polymerization of ethylene over ticl4/mgcl2/alet3 was obtained. firstly, to obtain the optimum value of [al]/[ti], the effect of [al]/[ti] on polymerization rate and catalyst yield was studied. also, the effect of catalyst content on yielding, crystallization, melting point and density of product were obtained. to determine the order of reaction, the monomer pressure w...

Journal: :علوم و تکنولوژی پلیمر 0
شکوفه حکیم محمدمهدی مرتضوی

ethylene was polymerized in slurry phase over a ticl4/mg(oc2h5)2 catalyst activated by al(c2h5)3. it was shown experimentally that mass transfer resistance has no effect on polymerization kinetics. after estimation ofthe active site concentration by inhibition method with carbon monoxide, the effects of polymerization temperature, monomer and cocatalyst  oncentrations and hydrogen were investig...

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