螺杆-导流筒搅拌器的循环和功率特性

测定了19种不同几何尺寸的螺杆-导流筒搅拌器层流域的轴向循环流量、功率消耗和Metzner常数K_(?).通过对螺杆挤出机的动力学分析结果进行实验修正,得到了半经验的无因次循环流量C_1、功率数K_(?)以及K_(?)的计算式.实验发现流体的弹性显著地抑制轴向循环流动,与牛顿流体相比,弹性流体的C_1有所降低.     

螺带式搅拌器的循环时间分布及其混合特性

采用单个悬浮粒子法和脱色法分别测定了多种不同几何尺寸的螺带式搅拌器的循环时间分布以及混合时间。得到同频度C_5值和混合时间C_1计算式。考察了流体的弹性对循环时间分布和循环流量的影响。     

新型高效正反旋转兼上下往复动搅拌器

对开发的正反旋转兼上下往复动搅拌器机械及原理作了简介，并对其宏观混合时间和搅拌功率做了实验考察，同时进行了性能评价。结果表明，该搅拌器适用于中低粘度体系，并对过渡流和湍流区域流体也具有优异的混合性能，但不适用于层流区域流体的混合。     

导流筒搅拌器在种分槽上的应用

对氧化铝生产的主要设备Φ10m×32m种分槽采用空气搅拌式的弊端进行了分析,详细介绍了导流筒搅拌器的结构及特点,并对该搅拌器的试验情况进行了分析,通过改造达到了预期的效果。     

三螺杆挤出机螺杆元件混合特性的数值研究

采用聚合物流体分析软件Polyflow对倒三角形三螺杆挤出机的6种螺杆元件的流道模型进行了三维等温数值模拟。使用Fieldview软件对结果进行统计处理,并采用不同的评价指标来表征混合性能,进而比较螺杆元件之间的混合特性。结果表明,捏合块的剪切和拉伸作用均强于螺纹元件;中性捏合块和左旋元件的回流效果好于其他元件;SME元件剪切弱于螺纹元件,但其拉伸作用和回流效果强于螺纹元件。因此,可根据物料对剪切的敏感性来合理地选择螺杆元件,以获得所期望的产品性能。     

双轴异桨组合搅拌器混合特性及传热性能研究

以聚合反应器中存在的传热,传质问题为研究背景,设计了双螺带－斜叶双驱动变速搅拌器。在实验室基础上,探讨了这一搅拌器的流型、功率消耗、混合特性和传热性能,为该组合浆的开发应用奠定了基础。     

浅析三螺杆挤出机的混合作用

介绍了新研制开发的三螺杆挤出机,并从倒品字形排布的三螺杆所构成的三个啮合区及由此形成的复杂的料流流动,粗浅分析了其混合作用。     

气液混合搅拌器组合的优化

研究了由3种基本搅拌桨类型(圆盘涡轮、上翻斜叶涡轮和下压斜叶涡轮)组成的9种搅拌桨组合在搅拌槽中的气液分散能力,得到了不同气体流速下优化的搅拌桨组合.     

螺带式搅拌器在假塑液中的混合及放大的研究

本文综合研究了螺带式搅拌器在假塑性液体中的混合特性及动力特性，测定了双螺带，内外螺带及螺带螺旋３种类型搅拌器的功率常数Ｋｐ和Ｍｅｔａｎｅｒ常数Ｋｓ，并得出混匀操作和传质工艺过程的放大准则。     

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。     

不同类型搅拌器的气—液分散和混合特性

在通气式搅拌槽内研制了直叶圆盘涡轮、直叶桨式涡轮、４５度折叶圆盘涡轮、４５度折叶桨工涡轮、凹弧叶圆盘涡轮、锥形涡轮和布鲁马金式搅拌器的临界分散转速、分散状态、搅拌功率、气含率、气泡停留时间、排量准数和输出效率，并获得了适用上述种类搅拌器的临界分散转速、搅拌功率、气含率和气泡停留时间关联式。     

强化单螺杆挤出机内层流混合的方法

综述了单螺杆挤出机内聚合物熔体层流混合机理的研究进展，对提高混合的措施进行了分析总结，指出了进一步强化混合效果的方法。     

搅拌生物反应器的循环时间分布和混合结构模型

利用磁粒子流动跟踪法对搅拌生物反应器的循环时间分布进行测定,并将Rushton径向流桨和两种新型轴向流桨在不同介质粘度和转速下的循环时间分布进行比较和性能评价。建立了单桨搅拌生物反应器的混合结构模型,对循环时间分布数据进行拟合,求得模型参数,进而讨论了不同实验条件下模型参数的变化。结果表明,对于非牛顿、高粘度发酵过程,轴向流桨比Rushton桨具有更好的混合特性。     

振动力场对销钉螺杆挤出机混炼过程的影响

利用流体动力学软件POLYFLOW对销钉螺杆挤出机的混炼段进行三维等温数值模拟.通过引入振动力场,采用粒子示踪分析方法对比分析不同振动力场参数对销钉螺杆挤出机混炼过程的影响.结果表明,振动力场对销钉的混炼性能有着明显的改善作用,但存在最佳的振动频率和振幅范围.该结论为寻求最优振动力场参数从而提高塑料混炼质量提供了参考.     

MIXING CHARACTERISTICS IN SLURRY STIRRED TANK REACTORS WITH MULTIPLE IMPELLERS

Hydrodynamic parameters such as power consumption, gas holdup, critical impeller speed for solid suspension and mixing time were measured in slurry stirred tank reactors with multiple impellers. The experiments were mainly conducted in a stirred tank of 0.2mi.d. with baffles. It contained two four-pitched blade downflow turbines for gas dispersion and one Pfaudler type impeller for solid suspension. As a part of scaling studies, additional experiments were also carried out in a larger stirred tank reactor (0,8m i.d.) geometrically similar to the smaller one. Glass beads and polymeric particles were used as a solid phase. Solid concentration was in the range of 0-20% (K/K). Tap water and methanol were used as a liquid phase

The power consumption decreased due to an introduction of gas and the presence of solids caused a decrease in the extent of reduction in power consumption. A correlation for power consumption in aerated slurry systems was proposed, It was found that the presence of solids is responsible for a decrease in gas holdup. A new correlation for gas holdup in gas-liquid-solid three-phase stirred tank reactors was developed. It fit the present experimental data reasonably. The critical impeller speed for solid suspensions increased with increasing gas flow rate. However, its increase was rather smaller as compared with the predictions of the correlations available in the literature. We proposed a correlation of the critical impeller speed for solid suspension in the presence of gas. The mixing time complicatedly increased or decreased depending on gas flow rate, impeller speed, solids type and concentration.     

EXPERIMENTAL STUDIES ON HEAT TRANSFER AND FRICTION FACTOR CHARACTERISTICS OF TURBULENT FLOW THROUGH A CIRCULAR TUBE FITTED WITH RIGHT AND LEFT HELICAL SCREW-TAPE INSERTS

Experimental investigation on heat transfer and friction factor characteristics of a circular tube fitted with right-left helical screw inserts of equal and unequal length of different twist ratios is presented. The experimental data obtained were compared with those obtained from plain tube published data. The heat transfer enhancement for right-left helical screw inserts is higher than that for straight helical twist for a given twist ratio. The effect of right-left twist length on heat transfer augmentation is presented. The empirical relations for Nusselt number, friction factor relating Reynolds number, twist ratio, and right-left twist distance were formed and found to fit the experimental data within 10% and 20% for Nusselt number and friction factor respectively. Performance evaluation analysis was made, and the performance ratio of more than one was obtained, indicating that the proposed twist inserts can be used effectively for heat transfer augmentation without any loss in pumping power.     

犁钉螺杆在VC403上纺制PP长丝的应用

在VC403纺丝机上应用犁钉螺杆生产PP长丝。生产实践表明:犁钉螺杆以分流三维混合为特征,加大了槽深,强化了剪切、混合。与常规螺杆相比,生产过程稳定,工艺易于控制,产品物理性能指标提高,不匀率降低,相同工艺条件下,产量约增加30%;同样产量下,螺杆转速、加热温度降低,减少了能耗。