Journal of South China University of Technology (Natural Science Edition) ›› 2014, Vol. 42 ›› Issue (10): 36-43.doi: 10.3969/j.issn.1000-565X.2014.10.007

• Materials Science & Technology • Previous Articles     Next Articles

Properties of PS/HDPE Blends with Different Flow Field Characteristics

Yin Xiao-chun Tang Bang Zeng Wen-bing Yang Zhi-tao Qu Jin-ping   

  1. 1. National Engineering Research Center of Novel Equipment for Polymer Processing//Key Laboratory of Polymer Processing Engineering of the Ministry of Education, South China University of Technology, Guangzhou 510640, Guangdong China; 2.Hubei Sanjiang Space Wan Feng Technology Development Co. Ltd., Xiaogan 432000, Hubei, China
  • Received:2014-06-16 Revised:2014-07-03 Online:2014-10-25 Published:2014-10-01
  • Contact: 杨智韬(1981-),男,博士,副教授,主要从事新型聚合物成型装备研究 E-mail:meztyang@scut.edu.cn
  • About author:殷小春(1975-),男,博士,副教授,主要从事高分子材料成型加工新理论与新装备研究;E-mail:mxcyin@163.com
  • Supported by:

    NSFC-广东联合基金资助项目(U1201242);国家自然科学基金青年科学基金项目(51403068);华南理工大学中央高校基本科研业务费专项资金资助项目(2013ZZ0015,2014ZB0021).

Abstract:

In the investigation, the structure and working principle of a vane compounder dominated by dynamic tensile deformation were introduced, and PS/HDPE melt blending experiments were conducted on the vane compounder and a commercial Brabender rotor internal mixer dominated by shear deformation. Then, the influences of the rotating speed and the mixing time on the mechanical property, rheological property and microstructure of the blends were discussed. The results show that (1) the tensile strength of the PS/HDPE blends molded by the vane compounder first increases and then keeps stable with the increases of the mixing time and the rotating speed, which is similar to those of the Brabender rotor internal mixer; (2) as compared with the Brabender rotor internal mixer, the rotating speed of the vane compounder has a smaller effect on the particle size of the dispersion phase of the blends, and the vane compounder needs a shorter time to achieve the same particle size of the dispersion phase at the same rotating speed; (3) the apparent viscosity of the blends molded by the Brabender rotor internal mixer remains unchanged with the increases of the mixing time and the rotating speed while that of the vane compounder decreases; and (4) the vane compounder shows a higher mixing efficiency and a better mixing effect in comparison with those of the Brabender rotor internal mixer.

Key words: vane compounder, dynamic tensile deformation, tensile strength, apparent viscosity, microstructure