塑料电磁动态逆化挤出机的挤出功率研究与模拟

本文采用自行修正的Tanner本构方程研究了塑料电磁动态塑化挤出机中熔体输送挤出功率对振动力场的响应。建立了振支力场作用下熔体输送挤出功率的理论模型,以此为基础模拟塑料电磁动态逆化挤出设备的设计和生产应用提供重要的理论指导依据。     

振动对mLLDPE加工影响的研究

研究了电磁动态塑化挤出条件下振动力场对茂金属线性低密度聚乙烯(mLLDPE)加工的影响。振动力场有效地降低了模头压力和挤出机消耗的功率,并使mLLDPE的熔体强度得到了提高,从而大大改善了mLLDPE的加工。     

振动力场作用下聚合物熔体单螺杆挤出过程数值模拟

根据塑料电磁动态塑化挤出过程中熔体输送的实际情况，对三维模型进行简化，利用大型有限元软件ANSYS模拟了叠加轴向振动力场作用下聚合物熔体在螺槽中的流动情况，求解出周期性变化的速度，压力场分布，结果表明，与稳态挤出过程相比，振动力场的引入在进出口压力差恒定的情况下，可以提高熔全输送流率。采用有限元模拟方法可以为确定和优化工艺参数，产品质量控制提供指导。     

振动力场下填充聚合物挤出过程研究

研究了利用塑料电磁动态塑化挤出机加工ＰＰ／ＣａＣＯ３和ＬＤＰＥ／ＣａＣＯ３时的动态挤出过程,探讨了振动力场对聚合物填充体系挤出过程扣影响规律和作用机理。结果表明,在一定的振动条件下,振动力场的作用使挤出压力减同功率降低,混合分散效果明显提高。     

塑料电磁动态挤出机中挤出压力对振动强度的响应

采用自行修正的Tanner本构方程,对塑料电磁动态塑化挤出机中挤出压力对振动力场的响应进行了研究,建立了振动力场下挤出压力响应的理论模型,分析了振动力场作用下挤出压力降低的原因,并从实验方面进行了验证,结果表明,理论分析的结论是基本合理的。     

单螺杆挤出机中熔体混合理论的研究

综述采用不同的函数对单螺杆挤出机中熔体混合过程进行描述的研究情况和新的混沌混合的研究进展，以及近几年来利用可视化和可视化技术对矣合物材料在挤出过程中的行为所作的观测和分析研究，指出在新型电磁动态塑化挤出机中，引入挤出加工全过程的振动力场，对熔体的混合起到了较好的促进作用。     

基于电磁动态塑化挤出的模头挤出特性的研究

本文以塑料电磁动态塑化挤出机上的圆截面模头为对象,研究了将振动力场引入聚合物塑化挤出全过程条件下圆截面模头的挤出特性,建立了圆截面模头脉动挤出特性的数学模型,并进行了实验研究,理论分析与实验结果趋向一致,从而揭示了振动力场引入聚合物塑化挤出全过程对圆截面模头挤出特性的影响规律。     

振动力场下聚合物塑化挤出技术研究

介绍玫种将电磁场引起的机械振动力场引入聚合物塑化挤出全过程的塑料电磁动态塑化挤出设备,讨论了它的原理、结构及应用,实验与生产表明,塑料电磁动态塑化挤出设备在加工聚烯烃时能耗降低２０％～５０％,挤出熔体温度降低２０℃以上,制品拉伸强度提高１６％以上,对无机填料充体系的兴旺聚散效果提高。     

塑料电磁动态塑化挤出机加工制品的力学性能

本文采用塑料电磁动态塑化剂出机挤出的条料和吹塑的薄膜进行制样,并对其试样进行力学性能测试分析,结果表明,由于在挤出加工的全过程中引入了周期性振动力场,经塑料电磁动态塑化挤出机加工的制品的力学性能得到了改善和提高,对于PP和LDPE挤出试样,拉伸强度分别提高4.2%和4.7%,对HDPE吹塑膜,纵模向拉伸强度分别提高19.2%和37.4%。     

动态挤出PP板材制品的结构与性能

利用电磁动态塑化挤出机挤出PP板材制品,并对其聚集态结构与力学性能进行测试分析。结果表明在挤出过程中引入振动力场,可以改变PP制品的聚集态结构,从而使其力学性能得到改善。     

Analysis on Pulsating Flow of Melt for Reciprocating Extrusion in the Screw Channel

In the reciprocating extrusion, the vibration force field (VFF) is applied to the entire plasticating process by the axial vibration of screw and the novel concept on the polymer dynamic plasticating process being strengthened has been brought forward in the paper. The mathematical model is established that describes the plasticating process under the VFF and the approximative analytical solutions of the velocity distribution, pressure gradient in the screw channel and the plasticating capability are obtained. The theoretical results show that the axial vibration of screw can accelerate the blend capability of polymer and make melt temperature more uniform. With increase of the vibration intensity, the effect of blend and plasticating is enhanced further. The average pressure gradient drops down the channel under the VFF because of lower virtual viscosity of polymer melt and smaller flow resistance in the channel. The comparison between the theoretical analysis and the experimental results shows the plasticating capability of melt is improved with increase of vibration intensity.     

A Computer Model for Single-Screw Plasticating Extrusion

A fully predictive computer model has been developed for a single-screw plasticating extrusion (with conventional screws). The model takes into account five zones of the extruder (hopper, solids conveying, delay zone, melting zone, melt conveying) and the die, and describes an operation of the extruder-die system, making it possible to predict a mass flow rate of the polymer, pressure and temperature profiles along the screw channel and in the die, solid bed profile, and power consumption. Moreover, mixing degree, temperature fluctuation and viscoelastic properties of the polymer are estimated. The simulation parameters are the material and rheological properties of the polymer, the screw, hopper and die geometry, and the operating conditions (screw speed and barrel temperature profile). Such a comprehensive approach to the modeling of extrusion creates the possibility of optimizing the process, for example, from the point of view of the quality of extrusion. The model has been verified experimentally for a low-density polyethylene on a 45 mm diameter single-screw extruder.     

Simulation of cottonseed cake melt flow in metering zone of a single screw extruder

Research on the extrusion of natural polymers (food, feed, etc.) is relatively new due to the complex physicochemical transformations of raw materials, although plastics melt conveying and transport have been well studied. The structure and composition, rheological behavior as well as extrusion processing of natural polymer are much more complicated. In this study, a quasi-three-dimensional (3D) fluid flow model for non-Newtonian, non-isothermal and undeveloped temperature was developed, the model prediction being in reasonably good agreement with the experiment. Results show that the influence of moisture content, among other process variables, is the most significant, followed by screw speed. Some interaction exists between these two variables and the screw speed effect becomes marginal at high moisture contents. In addition, viscosity change in the channel was studied.     

Simulation of cottonseed cake melt flow in metering zone of a single screw extruder

Research on the extrusion of natural polymers (food, feed, etc.) is relatively new due to the complex physicochemical transformations of raw materials, although plastics melt conveying and transport have been well studied. The structure and composition, rheological behavior as well as extrusion processing of natural polymer are much more complicated. In this study, a quasi-three-dimensional (3D) fluid flow model for non-Newtonian, non-isothermal and undeveloped temperature was developed, the model prediction being in reasonably good agreement with the experiment. Results show that the influence of moisture content, among other process variables, is the most significant, followed by screw speed. Some interaction exists between these two variables and the screw speed effect becomes marginal at high moisture contents. In addition, viscosity change in the channel was studied.     

Simulation of nonisothermal flow of melt during melting process of vibration‐induced polymer extruder

A simplified 2D melt film model was established to simulate the nonisothermal melt flow during the melting process of the vibration‐induced polymer extruder of which the screw can vibrate axially. Since polymer has time‐dependent nonlinear viscoelastic characteristic with vibration force filed (VFF), a self‐amended nonisothermal Maxwell constitutive equation that can reflect the relaxation time spectrum of polymer was adopted. Using the 2D melt film model, melt films of two kinds of thickness representing different melting stages were simulated to investigate the influence tendency of the same VFF on the different melting stage. Special flow patterns and temperature distribution of melt in the melt film between the driving wall and the solid/melt interface with various vibration force fields were systematically simulated. It is found out that within a certain range of vibration strength, the application of vibration can optimize the time‐averaged shear‐rate distribution, improve the utilization efficiency of energy, and promote melting process; and the thinner the melt film is, the more intense the nonlinear viscoelastic response becomes with the same VFF; moreover, there exists optimum vibration strength to make the melting process fastest, which is in accord with the visualization experimental results. © 2006 Wiley Periodicals, Inc. J Appl Polym Sci 102: 5825–5840, 2006     

塑料异型材挤出口模的三维罚有限元设计

讨论了现有塑料异型材挤出口模研究中的流变学分析方法,指出了前人运用流变学方法设计挤出口模的不足。本文采用三维罚有限元方法,对幂律流体在塑料异型材口模中的流动进行了计算机模拟研究,阐述了采用三维罚有限元方法进行塑料异型材挤出口模设计的重要意义     

在挤出机口模中聚合物不稳定流动的模拟

对挤出机口模流道中高聚物的流动情况进行了分析。引用高聚物黏弹性流体本构方程,建立了高聚物在挤出机机头口模中流动的数学模型。用MathCAD软件对该模型进行了数值模拟,结果表明:机头压力、材料的松弛时间以及口模流道的几何尺寸对高聚物在机头中应力张量的变化影响较大,适当调整口模流道尺寸会有利于高聚物的稳定挤出。     

单螺杆精密挤出机并联式稳压系统的研究

介绍了精密挤出及精密挤出设备的研究现状。一种新型的单螺杆并联式稳压装置的工作原理及数学模型的建立和MathcAD计算的结果，在模拟计算的基础上，进行了多次实验，采集的数据分析与计算结果相近，证明了该装置有实际应用的前景和价值。     

注气口前后段螺杆中聚合物熔体的数值研究

运用Polyflow软件对微孔塑料挤出成型过程中注气口前后段螺杆进行三位瞬态模拟,研究了不同聚合物黏度、不同螺杆转速下注气口处的熔体压力场及熔体质量流量。结果表明,沿轴向640~670 mm处最符合作为超临界气体注入口的工艺条件;注气口处熔体压力在径向范围变化幅度不大,只需在注气口处所注入的超临界气体压力略大于熔体压力即可;随着螺杆转速的增大,注气口处聚合物熔体质量流量也随之增加,且两者之间呈现规律性变化,故可得到在不同螺杆转速下聚合物熔体质量流量大小。