温度和固相粒径与浓度对水煤浆管内流动壁面滑移的影响

通过改变管径、温度、煤粉粒度和浓度,在中试规模的输送装置上研究水煤浆直管内的滑移流动规律,联合采用Mooney滑移修正方法和Tikhonov正则化方法确定浆体壁面滑移特性。结果表明,随温度和固相粒径的增大,临界剪切应力降低,壁面滑移速度显著增加;浓度越高,临界剪切应力及产生相同滑移速度所需的壁面剪切应力越大,温度升高对临界剪切应力和屈服应力的降低越显著;低壁面剪切应力下的滑移贡献率主要取决于临界剪切应力及屈服应力的相对大小,高壁面应力下主要取决于壁面滑移速度和浆体真实流变特性。     

水焦浆流变特性的影响因素研究

用石油焦与3种不同的分散剂成浆,研究几种因素对水焦浆流变特性的影响。结果表明水焦浆的流变特性主要取决于石油焦本身的性质。其次对其有影响的因素主要是粒度和分散剂种类,粒度越小越容易形成胀塑性流体,分散剂不同流变特性会有所不同。除此之外,分散剂的用量、浆体浓度对流变特性的影响不是很大。     

石油焦的成浆性及水焦浆的流变性和稳定性

对某石油焦在加入不同添加剂后的成浆特性以及水焦浆的温升特性、流变特性和稳定性进行了实验研究。加入不同添加剂后各浆样的定黏浓度均在70%左右,石油焦成浆性良好;水焦浆的表观黏度随温度的升高而降低,随浓度的升高而增大;水焦浆的流变特性和稳定性在不同的添加剂下呈现出较大的差别,当使用亚甲基萘磺酸钠-苯乙烯磺酸钠-马来酸钠(NSM)和亚甲基萘磺酸盐甲醛缩合物(NC)添加剂时,水焦浆呈胀流性,且稳定性差。当使用木质素磺酸盐(LS)和石油磺酸盐(PS)时,水焦浆在较高浓度下呈假塑性,且稳定性较好。浆体浓度越大,稳定性越好。     

滑移壁面蛇形微通道两相流数值模拟

基于Fluent平台,采用CLSVOF方法对滑移壁面蛇形微通道气液两相流动进行了数值计算。计算选用的方法与理论结果具有较好的一致性,同时可以表明疏水壁面会产生滑移现象,且在高度较小的微通道内滑移效果更显著,从而减小通道内流体流动阻力,实现减阻;不同壁面性质通道内流体流动情况的计算结果表明,滑移壁面对截面速度分布趋势几乎没有影响,但上下壁面疏水性不同会影响通道截面最大速度分布。此外接触角及相对粗糙度对滑移特性影响较大,合理设计壁面润湿性及微粗糙元结构可以最大限度发挥滑移现象引起的减阻效果;与无滑移壁面相比,滑移壁面微通道内传热效果更好,且随滑移速度的增大,通道换热增强。     

滑移壁面蛇形微通道两相流数值模拟

基于Fluent平台,采用CLSVOF方法对滑移壁面蛇形微通道气液两相流动进行了数值计算。计算选用的方法与理论结果具有较好的一致性,同时可以表明疏水壁面会产生滑移现象,且在高度较小的微通道内滑移效果更显著,从而减小通道内流体流动阻力,实现减阻;不同壁面性质通道内流体流动情况的计算结果表明,滑移壁面对截面速度分布趋势几乎没有影响,但上下壁面疏水性不同会影响通道截面最大速度分布。此外接触角及相对粗糙度对滑移特性影响较大,合理设计壁面润湿性及微粗糙元结构可以最大限度发挥滑移现象引起的减阻效果;与无滑移壁面相比,滑移壁面微通道内传热效果更好,且随滑移速度的增大,通道换热增强。     

不同聚合物熔体壁面滑移的试验研究

采用毛细管流变仪研究了聚丙烯(PP)、高密度聚乙烯(PE-HD)、聚苯乙烯(PS)和聚甲基丙烯酸甲酯(PMMA)4种聚合物熔体的壁面滑移,考察了壁面滑移速度(v_s)与剪切应力(σ_w)、温度之间的关系以及壁面滑移对熔体流动性的影响。结果表明,在4种聚合物熔体流动过程中,σ_w满足一定条件时,均有壁面滑移现象产生;随σ_w的增加,vs值明显提高,两者之间呈幂函数关系;随温度的升高,发生壁面滑移的临界σ_w降低;壁面滑移对熔体流动性的影响与聚合物种类有关;且流动通道直径越小,影响越显著。     

挤出过程中NR／CPB混炼胶壁滑移行为研究：Ⅱ.壁滑移速度

应用Ｍｏｎｓａｎｔｏ加工性能试验机，考察了天然胶／顺丁胶胶料在毛细管挤出过程中的壁滑移速度及其影响因素。发现，在较低的剪切速率下，试样的流动曲线出现不连续；壁滑移速度与壁面剪切应力之间大体上呈指数函数关系；发生壁滑移时的临界剪切应力随着温度的升高而下降。     

微注塑充模过程中壁面滑移对熔体流动影响的研究*

针对微型塑料件注塑充模过程中,壁面滑移对流动的影响不可忽略的情况,运用流体分析软件Fluent,以微阶梯圆形截面通道为模型,在考虑和不考虑壁面滑移的情况下,对微注塑充模流动过程中壁面滑移的影响进行了数值模拟。分析了细通道近壁面处熔体的剪切速率和黏度,发现考虑壁面滑移时近壁面处的剪切速率略大,黏度略低。研究了熔体在粗通道和细通道中沿径向的流动速度和温度分布,以及沿微通道流动方向上的压力分布。结果表明,考虑壁面滑移时熔体流动速度较大,与壁面接触的熔体流动速度不再为零,且微通道截面尺寸越小,这种现象越明显;考虑壁面滑移时近壁面处熔体温度略高,并且粗通道中的这种现象更明显一些;壁面滑移对微通道中的压力分布几乎没有影响。总体而言,壁面滑移有利于微注塑充模。     

幂律流体在Kenics型静态混合器中流动特性分析

为了探究Kenics型静态混合器内扭旋叶片剪切作用对幂律流体流动的影响,利用旋转流变仪测量了浓度为0.5wt%, 0.7wt%, 0.9wt%的羧甲基纤维素(CMC)水溶液的流变参数,采用数值模拟与实验研究了扭旋叶片作用下幂律流体流动阻力和剪切稀化特性。对流场研究表明,扭旋叶片诱导产生了内流涡旋、绕流涡旋和近壁面涡旋,有效强化了静态混合器内流体流动的剪切作用。受多个纵向涡旋分布的影响,扭旋叶片局域流场中周向45°位置速度最高,周向30°位置涡量与剪切应力最高而黏度最低。径向0.4倍半径位置速度最高,0.7倍半径位置黏度最高。静态混合器有效提高了流体的二次流流动速度和剪切应力,降低了幂律流体的黏度和流动阻力系数。     

絮凝氧化铁悬浮液流变性质研究

应用LVDV-Ⅲ+型可编程流变仪测定了微米级氧化铁悬浮液絮凝处理后的流变特性,考察因素包括悬浮液固相质量浓度、pH值、絮凝剂添加量、搅拌速度。结果表明,悬浮液浓度不同,其流变性能也表现出不同,在相同剪切速率下,高质量分数悬浮液的表观粘度和剪切应力都大于低质量分数悬浮液的表观粘度和剪切应力;pH对絮凝悬浮液流变性有重要的影响。絮凝悬浮液粘度随pH的增加先增大后减小,絮凝剂聚合氯化铝添加量为80 mg的条件下,pH=6.14时表观粘度最大;絮凝剂浓度的不同,对于悬浮液流变性能的影响也不同,在相同剪切速率下,添加高浓度絮凝剂悬浮液的表观粘度和剪切应力都大于添加低浓度絮凝剂悬浮液的表观粘度和剪切应力,增加絮凝剂浓度对提高悬浮液粘着性能具有积极意义;对悬浮液搅拌强度不同其流变性能也表现出不同,在相同剪切速率下,悬浮液的表观粘度和剪切应力随着测试前对它搅拌强度的增加表现出先增大后减小。     

SiCW对Al2O3基陶瓷浓悬浮体流变性能的影响

研究了SiCW加入至Al2O3基体中注凝成型料浆的流变特性.研究结果表明:该体系表现出剪切增厚的胀流型流变特性.料浆流变性能与SiCW掺量、SiCW平均长度和SiCW与浆料的混合时间有关;但随着SiCW掺量的增加,剪切应力迅速增加,系统出现中断剪切现象;为了改善含SiCW料浆的流变性能,通过在晶须表面覆盖了一层钛酸酯的憎水膜,降低了料浆的表观粘度和剪切应力,并相应提高了晶须的掺量.     

Slip flow of coal water slurries in pipelines

Experiments were carried out on a pilot scale slurry transport apparatus to investigate slip flow behavior of coal water slurries (CWSs) in pipes with various diameters (25, 32, 40 and 50 mm). The effects of volume concentration, particle size and slurry temperature on wall slip behavior (wall slip velocity, critical wall shear stress and slippage contribution) were investigated. A numerical technique based on Tikhonov regularization was applied to determine the wall slip behavior. As the slurry temperature or the particle size increased, the critical wall shear stress was observed to decrease and the wall slip velocity was observed to increase significantly, while when the solid concentration was very close to the maximum packing fraction, a slight increase in volume concentration would lead to a rapid decrease in wall slip velocity and a sharp increase in critical wall shear stress. The temperature influence on critical wall shear stress and yield stress increased as volume concentration increased. At low wall shear stress, the slippage contribution was mainly dependent on the difference between yield stress and critical shear stress. While at high wall shear stress, it was dependent on both of the shear viscosity of the bulk slurries and the wall slip velocity.     

撞击流反应器内幂律流体流动特性的数值模拟

采用数值模拟方法对撞击流反应器内幂律流体的流动特性进行研究,分析了不同喷嘴间距和入口流速下清水和不同质量分数幂律流体的径向射流扩展率、径向速度衰减率、剪切应力、表观黏度等分布规律,研究表明：幂律流体中径向射流的径向速度分布规律与清水径向射流相似。随喷嘴间距的增大,扩展率增大,径向速度衰减率减小,平均剪切应力呈先增大后减小的变化规律,其中L=3D时平均剪切应力值最大,更利于流体混合。入口流速越大,扩展率越小,径向速度衰减率越大,平均剪切应力也随之增大。幂律流体的平均剪切应力大于清水,且随质量分数的增大,其扩展率增大,为清水扩展率的1.3~3.3倍,而幂律流体的径向速度衰减率从-1.268~-1.125降低到-1.144~-1.082,逐渐小于清水。幂律流体径向射流区域的剪切应力呈“M”形分布,表观黏度则呈“W”形分布,流体的流变性质对撞击流反应器内流体的流动规律影响显著。     

Wall slip velocity measurement of molten polypropylene in capillary flow based on length‐corrected Mooney technique

In this study, to measure wall slip velocity of molten polypropylene (PP) by using different length‐to‐diameter (L/D) ratios of capillary dies with fixed diameter, a length‐corrected Mooney technique was proposed. Moreover, the effects of pressure, temperature, and L/D ratio were considered to better represent wall slip mechanism. To verify the feasibility of the length‐corrected Mooney technique, a series of capillary rheological experiments for molten PP were carried out. Meanwhile, the power‐law quantitative equations of slip velocity were established by shear stress. Moreover, the effects of L/D ratio and temperature on rheological properties of PP were investigated. In addition, numerical simulations for slip velocity and rheological properties of PP were performed. Numerical results validated that the length‐corrected Mooney technique, and the power‐law quantitative equations of slip velocity were available. Results showed that wall slip velocity of molten PP decreased with the capillary die's L/D ratio, but increased with the temperature and shear rate. © 2016 Wiley Periodicals, Inc. J. Appl. Polym. Sci. 2017 , 134, 44589.     

凝聚剂对氧化铁悬浮液流变性的影响

应用LVDV-Ⅲ+型可编程流变仪测定了凝聚剂对氧化铁悬浮液的流变特性的影响。实验结果表明,高价凝聚剂对于悬浮液颗粒的凝聚能力要比低价凝聚剂更加明显;随着凝聚剂浓度的增加,悬浮液颗粒的凝聚程度也相应增加;凝聚剂种类的不同,对于悬浮液流变性能的影响也不同,高价凝聚剂对于悬浮液流变性能的影响比低价凝聚剂大。在相同剪切速率下,添加高价凝聚剂悬浮液的表观粘度和剪切应力都大于添加低价凝聚剂悬浮液的表观粘度和剪切应力;凝聚剂浓度的不同,对于悬浮液流变性能的影响也不同。在相同剪切速率下,添加高浓度凝聚剂悬浮液的表观粘度和剪切应力都大于添加低浓度凝聚剂悬浮液的表观粘度和剪切应力,增加凝聚剂浓度对提高悬浮液粘着性能具有积极意义。     

Surface tearing and wall slip phenomena in extrusion of highly filled HDPE/wood flour composites

The extrudate surface tearing of highly filled high‐density polyethylene (HDPE)/wood flour composites has been investigated in relation to the rheological properties and the wall slip phenomenon in capillary dies. Rotational and capillary rheometers were employed to measure the rheological properties. Mooney analysis was used for determination of wall slip velocity. The results showed considerable increase of storage modulus, dynamic and shear viscosity with increasing wood flour loading. It was also found that all wood filled composites did not obey the Cox–Merz rule. The wall slip velocity depends on wood filler content and shear rate. Generally, with increasing shear rate the slip velocity sharply increases leading to plug‐like flow. It was observed that the surface of the extrudates becomes smoother with increase in shear rate and wood flour content. POLYM. ENG. SCI., 46:1204–1214, 2006. © 2006 Society of Plastics Engineers     

回收料制备人造草丝熔体的流变性能研究

采用聚合物动态流变测试仪研究了含回收料的人造草丝熔体的流变性能,探讨了回收料用量、温度、口模长径比对熔体表观黏度和挤出胀大比的影响。结果表明,人造草丝熔体属于假塑性熔体,其表观黏度随剪切速率和回收料用量的增加而降低。在剪切速率500s-1时,回收料用量越低,熔体的表观黏度降低越明显;剪切速率1800s-1时,熔体的表观黏度变化平缓且较为接近。对于100%回收料草丝熔体,其表观黏度随温度的升高和口模长径比的减小而降低;挤出胀大比则随温度的升高和口模长径比的增大而降低。     

Experimental study of rheological properties of solid propellant slurry at low-shear rate and numerical simulation

The steady state rheological properties of a three-component hydroxyl-terminated polybutadiene binder (HTPB) solid propellant slurry at low shear rate were investigated using a rotational rheometer. The data were analyzed and the rheological characteristics of the slurry were determined. The effect of shear rate on apparent viscosity and shear stress as well as the viscosity–time effect of the slurry were also analyzed. Herschel–Bulkley (H-B) model was applied for the simulation of the flow process of a two-dimensional container using CFD Ansys-polyflow software. Experimental results showed that solid propellant slurry had yield pseudoplasticity. Yield characteristics were determined based on the fact that when shear stress was greater than yield stress, the slurry began to flow and the relationship between shear stress and shear rate obeyed power law function. Simulation results further verified the correctness of experimental results.