The effects of partial replacement of TiCl4 by Ti(OR)4 on the performance of MgCl2-supported Ziegler-Natta catalysts

被引:12
作者
de Lemos, Cristovao [2 ]
Franceschini, Fernando [2 ]
Radtke, Claudio [1 ]
dos Santos, Joao H. Z. [1 ]
Wolf, Carlos R. [3 ]
机构
[1] Univ Fed Rio Grande do Sul, Inst Quim, BR-91501970 Porto Alegre, RS, Brazil
[2] Braskem SA, BR-95853000 Passo Raso, Triunfo, Brazil
[3] Univ Luterana Brasil, Fac Quim, BR-92425900 Canoas, Brazil
关键词
Ziegler-Natta catalyst; High-density polyethylene; Titanium tetra-alkoxide; MOLECULAR-WEIGHT DISTRIBUTION; ALKYL-AL COCATALYSTS; POLYMERIZATION; POLYPROPYLENE; MULTIPLICITY; METALLOCENE; SURFACE; SITES; MODEL;
D O I
10.1016/j.apcata.2012.02.022
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
In a Ti-based Ziegler-Natta catalyst with in situ generated MgCl2, the titanium tetrachloride (TlCl4) was partially replaced by titanium tetra-alkoxide (Ti(OR4)), where R was either ethyl or n-butyl. and the effect of the addition order of the titanium compound was evaluated. For comparison, two other catalysts were synthesized: (1) one had the same amount of Ti, exclusively from TiCl4; (2) the other is employed in industrial processes and was used as the reference. Ti3+ comprised 85% of the total amount of titanium added during the catalyst synthesis. The amount of soluble Ti in the supernatant phase was at most 0.002 mol L-1, indicating that the added Ti reacted with the support. In general, Ziegler-Natta catalysts demand a significant amount of raw materials, while these catalysts require a lower amount of titanium compounds and save a significant amount of solvent in particular during the synthesis (approximately 80%). The preparation time of the catalysts was also reduced. The performance of these catalysts during ethylene polymerization suggests that adding Ti(OR)(4) created a catalyst with a similar activity and ability to form high-density polyethylene as the reference catalyst. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:69 / 77
页数:9
相关论文
共 54 条
[1]   Modeling of fluidized bed reactor of ethylene polymerization [J].
Alizadeh, M ;
Mostoufi, N ;
Pourmahdian, S ;
Sotudeh-Gharebagh, R .
CHEMICAL ENGINEERING JOURNAL, 2004, 97 (01) :27-35
[2]   Mathematical Modeling of the Microstructure of Poly(propylene) Made with Ziegler-Natta Catalysts in the Presence of Electron Donors [J].
Alshaiban, Ahmad ;
Soares, Joao B. P. .
MACROMOLECULAR REACTION ENGINEERING, 2011, 5 (02) :96-116
[3]  
[Anonymous], 2000, HDB POLYETHYLENE STR, DOI DOI 10.1201/9781482295467
[4]  
Arthur W. A., 1958, Du Pont US Patent, Patent No. [2,862,917, 2862917]
[5]   Moving up and down the Titanium Oxidation State in Ziegler-Natta Catalysis [J].
Bahri-Laleh, Naeimeh ;
Correa, Andrea ;
Mehdipour-Ataei, Shahram ;
Arabi, Hassan ;
Haghighi, Mehdi Nekoomanesh ;
Zohuri, Gholamhosein ;
Cavallo, Luigi .
MACROMOLECULES, 2011, 44 (04) :778-783
[6]  
Berger E.D., 1981, J CAT COMP POLYM OLE
[7]  
Berthold J., 1984, Google Patents, Patent No. [US 4447587, 4447587]
[8]   THE INDUSTRIAL SYNTHESIS OF BIMODAL POLYETHYLENE GRADES WITH IMPROVED PROPERTIES [J].
BOHM, LL ;
ENDERLE, HF ;
FLEISSNER, M .
CATALYST DESIGN FOR TAILOR-MADE POLYOLEFINS, 1994, 89 :351-363
[9]  
Bretas R.E.S., 2000, RHEOLOGY MELTING POL
[10]   Characteristics of ethylene polymerization over Ziegler-Natta/metallocene catalysts - Comparison between hybrid and mixed catalysts [J].
Cho, HS ;
Choi, YH ;
Lee, WY .
CATALYSIS TODAY, 2000, 63 (2-4) :523-530