Numerical Simulation of Mixing Polymeric Fluids in Twin Screw Extruder

Author(s):  
Ebrahim Khalaj ◽  
Mohammad Hossein N. Famili ◽  
Faezeh Ghodratpour
Seikei-Kakou ◽  
1999 ◽  
Vol 11 (6) ◽  
pp. 502-509 ◽  
Author(s):  
Takeshi ISHIKAWA ◽  
Shin-ichi KIHARA ◽  
Kazumori FUNATSU ◽  
Taro AMANO

2009 ◽  
Vol 49 (9) ◽  
pp. 1772-1783 ◽  
Author(s):  
Xian-Ming Zhang ◽  
Lian-Fang Feng ◽  
Wen-Xing Chen ◽  
Guo-Hua Hu

2018 ◽  
Vol 153 ◽  
pp. 05004
Author(s):  
Yuan Zhang ◽  
Xiaohan Jiang ◽  
Huaping Fan ◽  
Xihan Li

In view of the unreasonable design of non-intermeshing counter-rotating twin screw extruder die, the problem of productivity reduction was discussed. Firstly, the mathematical model of extruder productivity was established. The extruder die model was improved. Secondly, the force analysis of twin screw extruder physical model was carried out. Meanwhile, A combination of mechanical analysis and numerical simulation was adopted. The velocity field, pressure field and viscosity field were calculated by Mini-Element interpolation method, linear interpolation method and Picard iterative convergence method respectively. The influence of die model on the quantity of each field before and after improvement was analyzed. The results show that the improved model had increased the rheological parameters of the flow field, the leakage and reverse flow decreased. Through post-processing calculation, the productivity of the third dies extruder was 10% higher than before. The research results provide a theoretical basis for the design and optimization of die model of non intermeshing counter-rotating twin screw extruder.


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