期刊文献+

双转子连续混炼机混炼段相似放大初探 被引量:3

Similar Scale-up of Mixing Section of a Two-rotor Continuous Mixer
下载PDF
导出
摘要 基于几何相似准则,分别对3种混炼段构型进行了2倍和10倍放大,用Polyflow软件对放大前后的混炼段流场进行了模拟研究,以1个旋转周期内不同横截面上的平均压力和平均混合指数、物料在混炼段的停留时间分布、混炼段出口截面上的解聚功率密度和修正Lyapunov指数的累积概率函数、比能耗、扭矩和轴向力等为评价指标,分析了几何相似放大对流场特征、混合效果、能耗等的影响。结果表明,采用几何相似准则对不同构型的混炼段进行放大时,在转速不变的情况下,产量均可按几何放大倍数的3次方放大,而混炼段流场特征、混合效果及比能耗保持不变,混炼段转子所受的轴向力和扭矩分别按几何放大倍数的平方和立方增大;在进一步的放大设计中需兼顾热平衡相似,以便在高产量下保证塑化品质。 Three mixing section configurations, i.e. double-flight, hake, and triple-flight were magnified to two and ten times according to geometric similarity principle, respectively. Polyflow software was employed to simulate the flow field in different mixing sections. Mean pressure and mixing index of different channel cross-sections during one revolution period, residence time distribution, cumulative probability distribution of depolymerization power density, and modified Lyapunov index on the exit of mixing section, specific energy, torque, and axial force were used as evaluating index to analyze the effects of geometric similarity scale-up on mixing sectiorfs flow field feature, mixing quality, energy cost, etc. In these simulations, the rotational speed of rotors kept constant while the volume flow rate of mixing section inlet increased by the geometric scaleup ratio's cube. Simulation showed that after being magnified to different size according to geometric similarity principle, the primary features of flow field, mixing effect and specific energy of mixing section were similar to those of corresponding prototypes, while torque and axial force increased by the square and cube of the geometric scale-up ratio, respectively. In the further study, similarity of the heat equilibrium should be considered to guarantee the similar plasticization effect.
出处 《中国塑料》 CAS CSCD 北大核心 2011年第6期102-107,共6页 China Plastics
基金 "863"高技术研究项目(2009AA042142)
关键词 双转子连续混炼机 混炼段构型 几何相似放大准则 流场模拟 two-rotor continuous mixer mixing section configuration geometric similar scale uprule flow field simulation
  • 相关文献

参考文献11

  • 1Carley J F, Mckelvey M. Extruder Scaleup Theory and Experiments[J]. Ind Eng Chem, 1953, 45:969.
  • 2Chan I Chung. On the Scale-up of P1asticating Extruder Screws[J]. Polym Eng Sci, 1984, 24(9):626- 632.
  • 3Potente H. Existing Scale-up Rules for Single Screw Plas- ticating Extruders[J]. Int Polym Proc, 1991, (6):267.
  • 4Enno E Agur. Extruder Scaleup in a Corotating Twin- screw Extrusion Compounding Process[J]. Adv Polym Techn, 1986, 6(2):225-231.
  • 5Meijer H E H, Elemans P H M. The Modeling of Contin- uous Mixers Ⅰ: The Corotating Twin-screw Extruder[J]. Polym Eng Sci, 1988, 28(5) :275-290.
  • 6Nakatani M. Scaleup Theory for Twin-screw Extruder, Keeping the Resin Temperature Unchanged[J]. Advances in Polymer Technology, 1998, 17(1):19-22.
  • 7董中华,江波,许澍华,武停启.啮合同向双螺杆挤出机的相似放大[J].塑料,2004,33(5):82-86. 被引量:5
  • 8王健平,江波,李翱,毕超.相似放大理论在大型啮合同向旋转双螺杆挤出机设计中的应用[J].塑料,2007,36(3):66-68. 被引量:4
  • 9Raman V C, Jaluria Y,Sernas V. Extrusion of Non-new- tonian Fluids in a Single-screw Extruder with Pressure Back Flow[J]. Polym Eng Sei,1996, 36(3):358-367.
  • 10Chenxu Y, Sundaram G. Modeling of Melt Conveying in a Deep-channel Single-screw Cheese Stretcher [J]. Jour- nal of Food Engineering, 2004, 61(2):241-251.

二级参考文献14

  • 1[1]J F Carley,M Mckelvey.Extruder scale-up theory and experiments[J].Ind Eng Chem,1953,45:969.
  • 2[2]Chan I Chung.On the scale-up of plasticating extruder screws[J].Polym Eng Sci,1984,24(9):626-632.
  • 3[3]C Rauwendaal.塑料挤出[M].北京:中国轻工业出版社,1995.
  • 4[4]H Potente.Existing scale-up rules for single screw plasticating extruders[J].Int Polym Proc,1991,6:267.
  • 5[5]Enno E Agur.Extruder scale-up in a corotating twin-screw extrusion compounding process[J].Adv PolymTechn,1986,6(2):225-231.
  • 6[6]R J Nichols,J Lindt.Scale-up of counter-rotating non-intermeshing twin screw extruders[C].SPE ANTECPapers,1988:80.
  • 7[7]H E H Meijer,P H M Elemans.The modeling of continuous mixers I:the corotating twin-screw extruder[J].Polym Eng Sci,1988,28(5):275-290.
  • 8[8]J A Colbert.Scale up of twin screw extruder[C].Bradford University:Polymer Process Engineering Conference,1995,7.
  • 9[9]K Y Ng, L Erwin.Experiments in extensive mixing in laminar flow:I simple inustrations[J].Polym Eng Sci,1981,21(4):212-217.
  • 10[10]耿孝正,张沛.塑料混合及设备[M].北京:中国轻工业出版社,1991.

共引文献5

同被引文献28

  • 1董中华,江波,许澍华,武停启.啮合同向双螺杆挤出机的相似放大[J].塑料,2004,33(5):82-86. 被引量:5
  • 2刘晓鸣,谢林生,马玉录,曹文凤.双转子连续混炼机转子混炼段流场的数值研究[J].中国塑料,2006,20(11):95-99. 被引量:8
  • 3王健平,江波,李翱,毕超.相似放大理论在大型啮合同向旋转双螺杆挤出机设计中的应用[J].塑料,2007,36(3):66-68. 被引量:4
  • 4Yi B, Fenner R T. Scaling-up plasticating screw extruders on the basis of similar melting performance [ J ]. Plastics and Rubber : Processing, 1976, 1 : 119-123.
  • 5Rauwendaal C. Scale-up of single screw extruders [ J ]. Polymer Engineering and science,1987,27 : 1059-1 068.
  • 6Agur E E. Extruder Scale-up in a corotating twin-screw extrusion compounding process [J ]. Adv Polym Techn, 1986,6 ( 2 ) : 225-231.
  • 7Bigio D, Wang K. Scale-up rules for mixing in a non-intermeshing twin-screw extruder [ J ]. Polymer Engineering and Science, 1996,36 ( 23 ) : 2 832-2 839.
  • 8Nakatani M.Scale-up theory for twin-screw extruder, keeping the resin temperature unchanged [J].Advances in Polymer Technology, 1998,17 ( 1 ) : 19-22.
  • 9Zhang Xianming, Feng Lianfang, Chen Weixing, et al. Numerical simulation and experimental validation of mixing performance of kneading discs in a twin screw extruder [J]. Polym Eng Sci, 2009,49 ( 9 ) : 1 772-1 783.
  • 10Bai Yun, Sundararaj U, Nandakumar K. Nonisothermal modeling of heat transfer inside an internal batch mixer [J]. AIChE Journal,2010,57 (10) : 1-13.

引证文献3

二级引证文献5

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部