共查询到16条相似文献,搜索用时 218 毫秒
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目的:提高双螺杆挤出机的混合效率和工作性能。方法:设计了一种内嵌行星轮系和安装捏合块的新型双螺杆挤出机,并用SolidWorks建立三维模型,以有限体积法为基础,用ANSYS/CFS有限元分析软件对其流道进行分析。获得其宏观压力图、速度矢量图、速度流线图并与传统双螺杆挤出机三维流场进行对比。结果:在行星轮系和捏合块的渐加速作用下,渐加速双螺杆挤出机的混合性能和工作效率要明显优于传统双螺杆,经计算渐加速型双螺杆比普通双螺杆提高20%~25%。结论:渐加速双螺杆在不断加速的过程中使得物料在机筒内停留的时间变短,从而提高产量且减少耗能,捏合块的加入更使得物料可以得到更好的剪切。 相似文献
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针对普通单螺杆挤出机剪切混合模式单一、工作性能差等问题,研究设计一种新组合型单螺杆。采用SolidWorks建模,ANSYS/CFX有限元分析和对比试验的方法;形成新组合型单螺杆流道整体压力差高于传统单螺杆1.22 MPa左右,物料在进出强剪切段过程中有回流产生,强剪切段物料输送速度较传统单螺杆加快0.012 m/s左右的结果;得出新组合型单螺杆挤出机在80?160 r/min的转速下,物料停留时间较传统单螺杆挤出机缩短5%?12%的试验结论。研究为高性能单螺杆挤出机的优化创新提供理论依据。 相似文献
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为了明确和量化同向全啮合双螺杆挤出机各螺杆元件的功能,增加配置用于生产植物基肉双螺杆挤出机螺杆的合理性,以低温脱脂花生蛋白粉的物性参数为条件,对SLZ36型挤出机的3种元件长度为32 mm的螺杆元件双头螺旋元件、5啮合盘啮合元件及3齿形盘齿形元件的剪切速率、混合指数、物料停留时间、最大剪切应力分布进行仿真分析。采用Solidworks软件建立元件的几何模型,应用Gambit软件进行模型的网格划分及网格质量分析,在Polyflow软件中进行数值模拟,通过Fieldview软件对仿真结果进行后处理分析。结果表明:通过混合指数分析得到3种螺杆元件对物料的混合性能大小为齿形元件>啮合元件>螺旋元件;通过物料停留时间分析得到3种螺杆元件的轴向混合性能大小为齿形元件>螺旋元件>啮合元件;通过剪切速率及平均最大剪切应力分析得到对物料的剪切性能大小为啮合元件>螺旋元件>齿形元件。进行植物基肉双螺杆挤出机螺杆组合时,针对目前整个螺杆配置螺旋元件最多的情况,在进行物料更换时可以合理地配置啮合元件以增加螺杆剪切能力,配置齿形元件以增加螺杆的混合能力。 相似文献
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采用POLYFLOW软件对单螺杆挤压膨化机中食品熔体的三维等温流场进行数值模拟,结合粒子示踪技术,探索不同螺棱间隙(0.4,0.8,1.2mm)对食品熔体流场和混合性能的影响。研究表明:随着螺棱间隙的减小,螺棱顶端的剪切速率增大,食品熔体平均黏度变小,螺杆的轴向输送能力变差;随着螺棱间隙的增大,食品熔体的停留时间先增后减,分散混合能力变差。当螺棱间隙增至1.2mm时,物料停留时间反而比间隙值为0.4 mm时长,说明螺棱间隙过大,食品物料的停留时间将难以控制,同时对各物料组分的混合效果也较差。螺棱间隙对熔体流场和混合特性均有一定的影响,螺棱间隙为0.8mm时,既能保证对熔体的输送能力,又能保证良好的流场分布和混合效果,为比较理想的螺棱间隙。 相似文献
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单螺杆挤压可以破裂植物细胞,用于辅助植物有效成分的提取.通过选取单螺杆中物料运动方向上的一段微元进行受力分析,分别求得螺杆、机筒、背压对物料的作用力和物料由于自身形变而产生的作用力,得到单螺杆中压力分布的数学模型;并针对截面为正六边形的柱状植物细胞模型,得到植物细胞受力的数学模型.模型表明细胞的受力情况和螺杆自身的结构参数、螺杆转速和挤出速率有关系,在螺杆结构参数确定的前提下,可以通过调整螺杆的转速和挤出速率来改变物料的受力情况,从而达到理想的破壁效果. 相似文献
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单螺杆挤压机工作性能探讨 总被引:5,自引:0,他引:5
单螺杆挤压机由于结构简单、价格低而得到广泛的应用。本文从单螺杆挤压机的喂料、输送、挤压的全过程进行分析,探讨改善其输送性能和提高对物料的混合作用的方法。 相似文献
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The flow of plasticized maize starch in a co-rotating twin screw extruder was simulated by using computational fluid dynamics (CFD). Sensitivity of the simulation to the selected viscosity model was analyzed. The results suggest that about 16 times increase in zero shear viscosity has no influence on the flow, whereas a slight change in viscosity at the shear thinning region leads to significant increase in pressure drop along the mixing zone of extruder. Simulation results were validated quantitatively by experimental data. Furthermore, the flow type and profile in the extruder were discussed by using the influence of screw speed and screw configuration as exemplary process parameters. To evaluate the dispersive mixing efficiency, material specific critical capillary number was implemented into particle tracking simulations. Maximum shear stress generated at the tip of the screws was used to calculate the maximum capillary ratio, and therefore to determine the dispersive mixing efficiency. The results show that increase in screw speed led to better dispersive mixing, although the generated shear stresses decreased. To investigate the influence of screw geometry, two different screw configurations were simulated. The results show that the dispersive mixing efficiency can be improved by using reverse kneading blocks at which more particles are exposed to high shear stresses. 相似文献
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目的:探究熔体输送段正向螺纹元件间的不同组合对反向螺纹元件的熔体输送特性的影响。方法:通过改变导程构建两种不同模型,使用SolidWorks软件建立三维模型,使用Polyflow软件对两种模型在熔体输送段的挤出过程进行数值模拟,分析不同导程下螺纹元件的螺槽宽度及螺棱厚度对流场的影响及不同转速下流场的变化,通过实验验证转速对物料混合效果的影响。结果:所构建的模型均可使熔体通过反向螺纹元件;在相同螺杆转速下,由大导程螺纹元件构建的模型一建压能力和输送能力强于由小导程构建的模型二;模型一在分散混合能力上优于模型二,在分布混合能力上弱于模型二;在两端压差相同的情况下,增加转速可以提高物料的分散混合效果。结论:在聚乳酸改进加工过程中采用模型一且提高螺杆转速可进一步破碎物料,提高挤出物的质量。 相似文献
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目的:探究啮合同向双螺杆挤出机不同螺杆构型对流场的影响,改善聚乳酸的材料性能。方法:应用Solidworks软件建立双头螺纹元件的几何模型,在Polyflow中进行数值模拟,借助Fieldview软件对仿真结果进行后处理分析,并对比剪切速率场、压力场、速度场、黏度场以及停留时间分布曲线RTD,得出螺槽深度对流场的影响。结果:在中心距相同的情况下,通过改变螺纹元件的外径和内径之比改变螺槽深度,在相同的工艺条件下,同向双螺杆流道内各物理场以及混合性能均存在较大差异;与构型二相比,构型一的剪切作用更强,但构型二的建压能力更好;挤出过程中,构型二轴向混合能力较好但自清洁能力较差,而构型一轴向混合能力较差、自清洁能力较好。结论:螺槽深度的改变对流道混合性能有着一定影响且存在规律性,可有效指导双螺杆挤出机螺纹元件的设计。 相似文献
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Mahmut Seker 《International Journal of Food Science & Technology》2004,39(10):1053-1060
Starch was extruded with sodium trimetaphosphate and sodium hydroxide in a single‐screw extruder at 40% moisture content and screw speeds of 90 and 140 r.p.m. The effect of screw configurations, which included one and two mixing elements, on mean residence time, spread of residence time distribution (RTD), and flow pattern were determined. Increasing the screw speed and reducing the number of mixing elements reduced mean residence time. Higher RTD spread values were obtained at a screw speed of 90 r.p.m. when compared with 140 r.p.m. and increasing the number of mixing elements in the screw increased the RTD spread. The flow pattern was between plug and mixed flow, and increasing the number of a mixing element in the screw did not significantly affect the flow pattern in the single‐screw extruder. 相似文献
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The influence of screw configuration and screw speed on the residence time distribution and product expansion was determined for rice meal processed in a corotating twin screw extruder. Screw speed had strong effect on the E(t)- and F(t)-diagrams, with the mean residence time varying inversely with screw speed from 206 s to 256 s. the F-diagram was modeled by the combination of perfect mixing and plug flow. the P estimates, which express the fraction of material in plug flow, varied inversely with screw speed from 0.41 to 0.55 for the operating conditions in this study. Both screw configuration and screw speed were statistically significant to the expansion ratios of rice extrudate, with the expansion in the height ranging from 2.98 to 4.13. 相似文献
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PROPERTIES of CROSS-LINKED STARCH PRODUCED IN A SINGLE SCREW EXTRUDER WITH and WITHOUT A MIXING ELEMENT 总被引:1,自引:0,他引:1
Starch was extruded with sodium hydroxide and sodium trimetaphosphate in order to cross‐link it in a single‐screw extruder with and without a mixing element at constant screw speed of 90 rpm in the first set of experiments and at similar mean residence time controlled by screw speed in the second set of experiments. For the screw without mixing element in the second set of experiments, screw speed was adjusted to give the similar residence time as the single‐screw extruder with mixing element at 220 rpm. Phosphorus content and pasting curves of extrudates showed that starch was cross‐linked during extrusion. Replacing the screw without mixing element by the screw with mixing 相似文献