Microstructure and on-line shear viscosity of PP/nano-CaCO3 composites prepared by twin-screw extruder
Microstructure and on-line shear viscosity of PP/nano-CaCO3 composites prepared by twin-screw extruder
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DOI:
10.1007/s10853-006-0128-2
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发表时间:
2006-06
影响因子:
4.5
通讯作者:
Hanxiong Huang;G. Jiang;S. Mao
中科院分区:
文献类型:
--
作者:
Hanxiong Huang;G. Jiang;S. Mao
Accepted: 6 February 2006/Published online: 28 June 2006 Ó Springer Science+ Business Media, LLC 2006 nano-CaCO3 was manufactured by Inner Mongolia Mengxi High-Tech Materials Co. Ltd. This nano-CaCO3 was pretreated by the manufacturer. Stearic acid was used as coupling agent. The PP/nano-CaCO3 composites were prepared using a modular co-rotating, intermeshing twin-screw extruder with a screw diameter of 35 mm and a length-diameter-ratio of 40: 1. The screw elements were selected and arranged to provide high shear intensity and help decrease the aggregation of the nano-CaCO3. In more detail, five kneading block sections alternate with the common conveying elements along the screw. A reverse kneading block is set in the second kneading block section to increase the filled degree in the screw elements. The addition of two neutral kneading elements extends the residence time of materials and further increases the shear intensity. The nano-CaCO3 was first dried in an oven at 90 C for 4 h and then mixed with the coupling agent for about 10 min to facilitate the dispersion of the nanoparticles in the PP matrix. The content of the coupling agent was 1.5 wt% of the nano-CaCO3. The PP and the nano-CaCO3 particles were dry-mixed thoroughly before feeding into the twin-screw extruder. The compounding was carried out at temperature profiles of 160-180-195-195-190-190-190-190-190 C from the hopper to the strand die. The screw speed was set at 400 rpm unless otherwise noted. The Haake ProFlow on-line rheometer, which was designed for measuring the melt viscosity and flow index, was side-mounted at the end of the twin-screw extruder and the melt shear viscosity of nanocomposites was measured online during the compounding. The ProFlow system continuously diverted a small flow of material from the end of the twin-screw extruder and pushed that material through a capillary by means of a melt pump. The pressure before the melt pump was controlled by an automatic bypass valve to avoid the disturbance of the process during the measurement. The extruded nanocomposites (strands) were collected and then used for the microstructure observation. Ultra-thin films with about 100 nm in thickness were cut from the nanocomposites in a nitrogen environment. The ultra-thin films were then examined by transmission electron microscopy (TEM, Jeol JEM-100CX II) operated at an accelerating voltage of 100 kV to observe the dispersion state of nano-CaCO3 particles. The size distribution of nanoparticles was quantitatively determined by analyzing the TEM photomicrographs using Scion image software (Beta 4.02, Scion Corp.). At least three TEM photomicrographs were analyzed for each nano-CaCO3 content. Figure 1 shows the TEM photomicrographs of the nanocomposites containing 5, 10, and 20 wt% nano-CaCO3, respectively. As can be seen, most nanoparticles were dispersed well in the PP matrix. It is demonstrated that the screw design used in this work is good for the dispersion of the nanoparticles. With the increase of nano-CaCO3 content, the particle size becomes larger and some large aggregates occur at the CaCO3 loading of 20 wt%. The quantitative analysis on the TEM photomicrographs showed that the sizes of most nanoparticles are less than 100 nm and the smallest one is lower than 5 nm. With the increase of nanoparticles, the size of the particles becomes larger. The comparison of