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Print version ISSN 0103-5053
On-line version ISSN 1678-4790
J. Braz. Chem. Soc. vol.16 no.6a São Paulo Nov./Dec. 2005
Luciano G. Furlan; Osvaldo L. Casagrande Jr.*
Instituto de Química, Universidade Federal do Rio Grande do Sul, Av. Bento Gonçalves, 9500, 91509-900 Porto Alegre - RS, Brazil
Branched polyethylene/high-density polyethylene blends (BPE/HDPE) were prepared using the combined [NiCl2(a-diimine)] (1) (a-diimine = 1,4-bis(2,6-diisopropylphenyl)-acenaphthenediimine) and [TpMs*VCl2(NtBu)] (2) (TpMs* = hydridobis(3-mesitylpyrazol-1-yl)(5-mesitylpyrazol-1-yl)) catalysts. The polymerization reactions were performed in hexane or toluene at three different polymerization temperatures (0, 30 and 50 °C) and several nickel molar fractions (xNi), using MAO as cocatalyst. At all temperatures, the activities show an approximate linear correlation with xNi, indicating a non-synergistic effect between the nickel and the vanadium species. Higher activities were found in toluene at 0 °C. The melting temperatures for the polyethylene blends produced at 0 °C decrease as xNi increases in the medium indicating good miscibility between the polyethylene phases made by both catalysts. The surface morphology of the BPE/HDPE blends studied by scanning electron microscopy (SEM) revealed low miscibility between the PE phases mainly in the case of the polymer blends produced at high temperature (50 ºC).
Keywords: BPE/HDPE blends, ethylene polymerization, homogeneous binary catalyst system, Nickel and Vanadium catalysts
Blendas de polietileno ramificado/polietileno de alta densidade (BPE/HDPE) foram preparadas usando uma combinação de catalisadores [NiCl2(diimina-a)] (1) (diimina-a = 1,4-bis(2,6-diisopropilfenila)-acenafeteno) e [TpMs*VCl2(NtBu)] (2) (TpMs* = hidridobis(3-mesitilapirazol-1-il)(5-mesitilapirazol-1-il)). As reações de polimerização foram realizadas em hexano ou tolueno em três diferentes temperaturas (0, 30 e 50 °C), utilizando várias razões molares de níquel (xNi), na presença de metilaluminoxano (MAO) como cocatalisador. Em todas as temperaturas, as atividades mostraram uma correlação aproximadamente linear com xNi, indicando o não aparecimento de um efeito sinérgico entre as espécies de níquel e vanádio. Altas atividades foram obtidas a 0 °C. As temperaturas de fusão (Tm) das blendas de polietileno produzidas a 0 °C diminuem conforme a xNi aumenta no meio reacional, indicando uma boa miscibilidade entre as fases de polietileno produzidas por ambos catalisadores. A morfologia da superfície das blendas de BPE/HDPE estudadas por microscopia eletrônica de varredura (MEV) revelou uma baixa miscibilidade entre as fases de PE, principalmente no caso das blendas poliméricas produzidas a alta temperatura (50 ºC).
A large range of polyolefinic materials with interesting properties have been disclosed in the last decades as a result of the development of new classes of olefin polymerization catalysts1 as well as of blending existing polymers.2 Furthermore, a new approach has been introduced that is based on catalyst systems that combine, in a single reactor, two or more types of catalysts that produce polymers with different and controlled molecular weight averages (Mw) and molecular weight distributions (MWD).3 This method has been successfully used to produce linear low density PE (LLDPE),4 branched polyethylenes,5 polyethylenes with long chain branches (LCB-PE),6 ethylene/1-hexene copolymers,7 and polyethylene blends.8
In the last few years we have developed homogeneous binary catalyst systems for the production of polyethylene blends,9 and LLDPE.10 Our studies demonstrated that the variation of polymerization parameters such as solvent, cocatalyst, temperature of polymerization as well as metal mole fraction strongly influences the activity and polymer properties. Particularly, for the binary catalytic system composed of [NiCl2(a-diimine)] (a-diimine = 1,4-bis(2,6-diisopropylphenyl)-acenaphthenediimine)/[TpMs*TiCl 3] (TpMs*= hydridobis(3-mesitylpyrazol-1-yl)(5-mesityl-pyrazol-1-yl))9 we have found evidence of synergistic effects between the two catalytic species.
Herein, we describe the use of [NiCl2(a-diimine)] (1) (a-diimine = 1,4-bis(2,6-diisopropylphenyl)-acenaphthenediimine) and [TpMs*VCl2(NtBu)] (2) [TpMs*= hydridobis(3-mesitylpyrazol-1-yl)(5-mesitylpyrazol-1-yl)] in the ethylene polymerization toward the production of polymer blends. Studies related to the effect of poly-merization temperature, solvent, and nickel mole fraction (xNi)11 on the activity and polymer properties are presented.
The compounds [NiCl2(a-diimine)] (1) (a-diimine = 1,4-bis(2,6-diisopropylphenyl)-acenaphthenediimine),12 and [TpMs*VCl2(NtBu)] (2) (TpMs* = hydridobis(3-mesitylpyrazol-1-yl)(5-mesitylpyrazol-1-yl)),13 were synthesized following procedures described in the literature. Ethylene (polymer grade, White Martins) and argon were deoxygenated and dried by passage through columns of BTS (BASF) and activated molecular sieves (3 Å) prior to use. MAO (Witco, 5.21 wt. % toluene solution) was used as received. Toluene and hexane were refluxed and distilled over sodium benzophenone ketyl. Solvents were stored under argon or vacuum prior to use.
All polymerization reactions were performed in a 1.0 L Pyrex glass reactor connected to a constant temperature circulator and equipped with mechanical stirring and inlets for argon and ethylene. The reactor was rinsed with 300 mL of a 0.04 mol L-1 Al(iBu)3 solution in hexane prior to use. Under argon atmosphere were introduced sequentially the proper amounts of solvent (toluene or hexane) and MAO solution, and then the system was saturated with ethylene. After complete saturation with ethylene at atmospheric pressure and thermal equilibration of the system, the polymerization reactions were started by adding solutions of 1 and/or 2 to the reactor. The total volume of the reaction mixtures was 300 mL for all polymerizations. The polymerization reaction was stopped by the addition of 1 mL of methanol. The polymer was washed with acidic ethanol, then water and ethanol, and dried in a vacuum oven at 60 °C for 12 h. On the basis of the results of multiple runs, we estimate the accuracy of the activities to ± 8%.
Differential scanning calorimetry (DSC) data and morphology studies were evaluated from films. Polyethylene films were prepared in a Carver press Monarch series, model 3710 ASTM. The polymers were pre-heated for 2 min at 160 °C between the press plates without pressure and then pressed for 2 min at 3 kgf cm-2 at the same temperature. After this time, the pressure was released and the films were control-cooled down to room temperature at the cooling rate of 10 or 18 ºC min-1, or quenched in water-ice bath or liquid nitrogen. The film thickness was 0.15 mm ± 0.02.
Polymer melting temperatures (Tm) were determined on a Thermal Analysis Instruments DSC-2010 calibrated with Indium, using a heating rate of 10 ºC min-1 in the temperature range 40-180 ºC and cooling to 40 °C at 10 °C min-1. The heating cycle was performed twice, and only the results of the second cycle are reported. Melt flow indexes (MFI) were determined at 190 °C using a 21.6 kg standard charge.
The morphology was studied by using a Scanning Electron Microscope (JEOL JSM 5800). Samples were fractured under liquid nitrogen and the fractured surfaces were coated with gold.
Results and Discussion
Influence of xNi, temperature, and solvent on activity.
The ethylene polymerization reactions were carried out using methylaluminoxane-activated [NiCl2(a-diimine)] (1) and [TpMs*VCl2(NtBu)] (2) in hexane/toluene at 0, 30, and 50 °C. Tables 1 and 2 show the results of polymerization runs by varying the nickel loading molar fraction (xNi).
The ethylene polymerization reactions performed employing 1 and 2 separately showed that the catalytic system 1/MAO exhibited higher activities than 2/MAO for all temperatures and solvents employed in the polymerization runs as can be seen in Figures 1 and 2. The catalytic system 1/MAO reached a maximum activity in toluene at 0 ºC (2248 Kg of PE mol[Ni]-1 h-1, entry 20) while a highest activity for system 2/MAO was obtained in hexane at 30 ºC (456 Kg of PE mol[V]-1 h-1, entry 6).
Comparing the performance of both catalytic systems it was observed that the nickel catalyst was more sensitive to temperature, than the vanadium catalyst decreasing the activity with increasing polymerization temperature. Furthermore, the difference between the activities obtained for the systems 1/MAO and 2/MAO decreases as the polymerization temperature increases, this effect being more pronounced in hexane. For instance, at 50 °C this activity difference was 1.2 fold and reaches 3.9 fold at 0 °C (compare entries 1 and 5, and 11 and 15).
Polymerization runs carried out when varying xNi and temperature, with constant amount of MAO, showed that the activities are strongly dependent on these parameters as can be seen in Figures 1 and 2. At low temperature (0 °C) apparently the solvent does not promote any significant influence on the activity. In that case, the activities increase linearly with xNi indicating that each catalyst precursor work independently. At higher polymerization temperatures (30 and 50 ºC) the influence of the solvent on the activity is more clearly presented. For the polymerization reactions performed in toluene the dependence of the activity with respect to the xNi was roughly linear.
On the other hand, the use of hexane instead toluene determined a clearly non-linear correlation between the nickel molar fraction (xNi = 0.25, 0.50 and 0.75) and the activity, suggesting that the combination of 1 and 2 in this solvent can be promoting a partial deactivation of these catalyst precursors. For instance, the activities found for xNi = 0.50 (30 °C, 188 kg of PE mol[M]-1 h-1; 50 °C, 204 kg of PE mol[M]-1 h-1) are 3.4 and 2.4 times respectively lower than the predicted ones (30 °C, 640 kg of PE mol[M]-1 h-1; 50 °C, 488 kg of PE mol[M]-1 h-1).14
Influence of xNi and polymerization temperature on the polymer properties
The influences of xNi, solvent and polymerization temperature on polyethylene microstructure have been evaluated by means of differential scanning calorimetry (DSC), and melt flow index (MFI). The results are summarized in Tables 1 and 2.
The melting temperature (Tm) of the polymers produced by 1 or 2 is not extensively affected by changing the solvent. As expected, the branched polyethylenes (BPE) produced by 1 (xNi = 1.00) have Tm of 118 ºC (toluene) and 121 °C (hexane) while the high-density polyethylenes (HDPE) produced by 2 (xNi = 0.00) show Tm around 145 ºC.
In contrast to the thermal behavior of the PE blends produced at 0 ºC using the homogeneous binary catalyst system [NiCl2(a-diimina)]/[rac-etilenebis(IndH4)ZrCl 2]9, broad single melting and crystallization peaks were observed in the PE blends produced by 1/2/MAO catalyst system, indicating good miscibility between the branched and high-densisty PE phases (Figures 3 and 4). It is significant to note that the Tm is strongly influenced by the nickel molar fraction whatever the solvent used in the polymerization reaction. For instance, the Tm values for the polyethylene blends produced in hexane varied from 122 ºC (xNi = 0.75) to 141 ºC (xNi = 0.25).
At higher polymerization temperatures (30 and 50 °C) only a slight decrease of Tm was observed. At these temperatures, the polyethylenes formed by 1 are totally amorphous due to the higher branch content15 and apparently they do not interfere in the crystallization process of the high-density polyethylenes due to a higher level of phase segregation. This phenomenon could be better visualized in the polymerization reactions carried out in hexane at 50 ºC where two polymers (BPE and HDPE) separated spontaneously and thus allowed the analysis of both phases (entries 13 and 14).
A comparition of the DSC results of the polymer samples produced in toluene at 0, 30, and 50 °C (Figure 5), shows higher dependence of the Tm values with respect to the xNi for the polyethylene blends produced at 0 °C than at 30 or 50 °C. Tm values decrease as the polymerization temperature increases indicating that at lower polymerization temperatures the miscibility between the PE phases is more effective. It is worth noting that nickel-a-diimine complexes show ability to promote the displacement of the metal along the growing polymer chain so-called chain walking mechanism.16 This process determines the number of branches in the polymer backbone. Therefore the extent of branching in the PE is sensitive to polymerization temperature, decreasing with decreasing polymerization temperature. At 0 ºC, 1 produces PE with lower degree of branching and thus, its miscibility with the PE produced by 2 is more pronounced.
As expected, the polyethylenes produced by 1 showed higher melt flow indexes (MFI) compared to those obtained using 2, since catalyst 2 produces ultra-high molecular weight PE.13 The MFI data for the polymer blends produced at 0 ºC indicate the formation of polymer with high molecular weight. These very low MFI values can be associated to the production of high molecular weight polyethylene by 1 at this polymerization temperature.17,9 In general, at higher polymerization temperatures (30 and 50 ºC) the MFI values increase as the xNi increases in the medium, this behavior being attributed to the formation of more branched and lower molecular weight polyethylenes produced mainly by 1.15
Morphology of the PE blends
The morphology of the polymer blends was investigated using scanning electron microscopy (SEM). SEM micrographs made on cryo-fractured surfaces of the polyethylene blend samples produced at 30 and 50 °C using xNi = 0.25 are shown in Figures 6 and 7. The SEM micrograph of the blend samples produced at 30 °C showed two phase components (Figure 6a) well dispersed. Increasing the polymerization temperature (50 ºC) there occured the production of a BPE/HDPE blend which also shows a double morphology, but in this case the presence of very small particles of BPE dispersed in the HDPE matrix was observed (Figure 7a). In order to evaluate the distribution of the PE phases in the matrix, cryo-fractured surfaces were etched with hot o-xylene and studied by SEM. Figure 6b shows the formation of large holes and defects distributed on HDPE matrix as a consequence of the extraction of the branched PE produced by 1. The non-uniform distribution of these holes and defects on the HDPE surface indicates the high incompatibility degree of these two phase components, considering mainly the large difference between the molecular weight of the PE produced by 1 and that produced by 2, which is responsible for the formation of ultra-high molecular weight PE. The extraction of the highly branched PE from the PE blend produced at 50 ºC generated a "sandwich structure" (Figure 7b) similarly found for homogeneous binary catalyst system composed by [NiCl2(a-diimine)] and [TpMs*TiCl3].9
We have shown that the combination of precursor catalysts 1 and 2 in the presence of MAO generates an effective binary catalyst system for ethylene polymerization. Different types of polyethylene blends can be produced depending on the polymerization temperature, solvent, and xNi. Higher activities have been found using toluene as solvent at 0 ºC as a consequence of better stability of 1 at this polymerization conditions. The surface morphology of the blends revealed very low miscibility between the PE phases, resulting in the formation of big holes and defects distributed on the HDPE matrix. This behavior is associated mainly to the large difference of the PE properties produced by 1 and 2 that has led to spontaneous phase separation during ethylene polymerization carried out in hexane at 50 ºC.
We are grateful to the CNPq for the fellowships and CTPETRO-CNPq for financial support of this research. L. G. F. acknowledges CAPES (Brazil) for a fellowship.
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Received: January 12, 2005
Published on the web: October 6, 2005