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NR/SBR混炼胶挤出流动中自然收敛角的计算 被引量:3

Calculation of Natural Convergent Angle of NR/SBR Compound Flow during Extrusion
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摘要 考察了NR/SBR共混胎面胶在毛细管挤出流动中的末端效应、基于以前的工作[1]提出了粘弹性流体自然收敛半角方程,并估算了试样在挤出条件下的人口自然收敛角(2α0)。结果表明,2α0值随着温度的升高而有所增大.随着剪切速率的增加而减小。 The end effect of NR/SBR tread compound flow during capillary extrusion was investigated. Based on the previous workLlj,an equation for calculating the natural convergent semiangle of viscoelastic fluid was proposed and the natural convergent angle (2a0)of the sample at the inlet during extrusion was estimated. The results showed that 2a0 increased with the rise of the temperature and decreased with the increase of the shear rate.
作者 梁基照
机构地区 华南理工大学
出处 《橡胶工业》 CAS 北大核心 1996年第8期458-461,共4页 China Rubber Industry
关键词 混炼胶 橡胶 天然橡胶 丁苯橡胶 挤出成型 compound,convergent flow,die,extrusion
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同被引文献16

  • 1梁基照.粘弹性流体的入口收敛流动[J].力学进展,1993,23(2):234-248. 被引量:6
  • 2梁基照.非牛顿流体自然收敛半角方程的实验验证[J].化工学报,1996,47(6):755-757. 被引量:7
  • 3Liang J Z.Effect of diameter ratios on entry pressure drop and die-swell behavior for rubber compound in capillary extrusion[J].Plast. Rubber Comps. Process. Appl.,1993,19:311-314.
  • 4Liang J Z.Estimation of vertical region length of rubber compound during entry flow[J].Plast. Rubber Compos. Process. Appl.,1996,25: 495-498.
  • 5Liang J Z.Converging flow of non-Newtonian fluids through an abrupt contraction[J].Developments and Applications of Non-Newtonian Flows,ASME,1995,231(66):35-37.
  • 6Liang Ji-Zhao.Converging flow of non-Newtonian fluids through an abrupt contraction[J].Developments and Applications of Non-Newtonian Flows,ASME,1995,231/66:35~37.
  • 7Liang J Z.Influence of die angles on pressure drop during extrusion of rubber compound[J].J Appl Po1ym Sci,2001,80:1150~1154.
  • 8Congswell F N.Converging flow of polymer melts in extrusion dies[J].Polym Eng Sci,1972,1:64~72.
  • 9Llang J Z, Li R K Y.Rheological properties of glass bead-filled low density polyethylene composite melts in capillary extrusion[J].J Appl Polym Sci,1999,73:1451~1456.
  • 10Liang Ji-Zhao.Determination of the entry region length of viscoelastic fluid flow in a channel[J].Chem Eng Sci,1998,53:3185~3187.

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