PX氧化鼓泡塔反应器内的TA浓度分布

利用新建的D476鼓泡塔冷模实验装置和沉降—扩散模型对工业鼓泡塔PX氧化反应器内的TA浓度分布进行了实验和数学模拟研究。结果表明,由于PX氧化气速较大,塔内TA浓度接近均匀分布。     

Upwind searching for an odor plume is sometimes optimal

A model is presented that suggests that the optimal strategy for an animal walking or crawling on a substrate while searching for the source of a chemical carried by a shifting wind or current may be to move upwind (or against the current). The requirements are that (1) the current direction fluctuates rapidly within a range that exceeds 30 ° on both sides of the mean direction, and (2) the searching animal can move accurately up- or downwind and, once within the influence of the chemical plume, can move efficiently to the source. Under these conditions, an upwind search is shorter (on the average) by 0.9–0.3 of the range of influence of the chemical stimulus. Thus, this strategy is relatively more important when the total search path is short, i.e., when sources are typically close by. The mean length of the downwind search path is given by L _d =d +r[(1/E) + cos ]/2 and the upwind search path by L _u =d +r[(2/E) – (/sin ) – cos ]/2 whered is the starting distance up- or downwind of the source,r is the range of stimulus influence,E is the efficiency with which the searcher moves to the source within the influence of the plume,a is the angle of the maximum extent of wind direction from the mean, and the average, , is taken over all starting positions across the wind direction that lead to search paths that intercept the area swept by the plume.     

垂直管内弹状气泡上升中壁面传递的实验研究

垂直管内弹状流壁面传递是诸多工业应用中需研究的重要问题之一。今用极限扩散电流技术,对弹状气泡上升时瞬时壁面剪应力和传质系数进行了测定,结果显示:当基于表观气速的Froude数FrG < 0.74时,壁面剪应力随弹状气泡和液塞的到来呈现方向相反的交替变化,壁面传质系数亦相应变化;而当FrG > 0.74时,剪应力方向一直向下,说明液膜向下流动,且弹状气泡和液塞的到来对壁面传质系数的影响很小。这说明下落液膜射流穿透了液塞段,控制了整个壁面传递过程。研究还对下落液膜区、尾迹区及液塞段的不同传递特征及机理进行了分析, 并结合气泡塔熔融结晶器中弹状气泡上升时的传热,对结晶操作条件的合理选择进行了讨论。     

Bubble Formation at a Rotating Cylindrical Surface in Cross‐Flowing Liquid

A novel method of gas sparging from a rotating cylinder is proposed, which prevents against formation of large attached gas cavities in cross‐flowing liquids including those flowing downwards. Experimental and theoretical results regarding critical rotation speed necessary to remove the attached cavity, bubble formation process and size distribution of the produced bubbles in a low viscosity system (air‐water) are presented in this study.     

三相流化床的流体力学特性研究

利用空气、水和玻璃珠颗粒为工作介质,对三相流化床流态化操作的流体力学特性进行了研究,主要研究了气体速度、液体速度、颗粒投加量与气含率的关系,以及气体速度与床层高度及气泡直径的关系。     

油滴釉制作工艺的研究

在研制氧化气氛烧制油滴黑釉器的基础上 ,探讨了影响油滴釉形成的工艺因素。通过一系列试验 ,进一步验证了油滴釉在结晶过程中主要发生了液液分相 ;釉料的化学组成是油滴晶斑形成的先决条件 ;釉层厚度、烧成制度等是决定釉面效果的重要因素 ;油滴晶斑的呈色不仅与烧成气氛有关 ,还与着色氧化物的引入有关。     

熔块中的气泡缺陷及其解决办法

分析了熔块生产中气泡缺陷产生的各种原因．提出了实际生产中的注意事项和具体的解决办法。     

带阻尼内构件鼓泡塔的研究(Ⅰ)——内构件对流速分布的影响

针对大型鼓泡塔径向流速分布不均易导致中心区域气体短路的问题,提出了在中心区域布置阻尼内构件改善流速分布的方案。冷模实验表明,阻尼内构件的加入可以有效地改善中心区域气-液流速分布,阻尼内构件尺寸对流速分布有显著影响。引入了阻力密度函数来表征阻尼内构件的影响,采用拟均相流动模型模拟含阻尼内构件的塔内流速分布,计算结果与实验测量值大体相符。     

MathCAD软件对塑料发泡振动的模拟

气泡膨胀过程中产生的高频振动已达到超声波范围,对聚合物中纳米粒子的分散具有很好的作用。利用MathCAD模拟了气泡振动影响因素,分析了气泡内外压差、高聚物熔体的表面张力、应力松弛时间等因素对气泡振动的影响。通过分析,对气泡振动的工艺条件提出一些参考。     

带阻尼内构件鼓泡塔的研究(Ⅱ)——内构件对气液传质速率的影响

采用化学吸收法实验考察了鼓泡塔内部的阻尼内构件对气液传质速率的影响.结果表明.在流速最高的塔中心区域设置阻尼内构件不但可以改善流速分布.而且还能显著地促进气液传质.在合适的阻尼面积密度范围内,安装内构件后气液传质速率可提高10%～30%,其机理是内构件的存在强化了流体的局部湍动.将鼓泡塔内大尺度的平均流动动能转化为小尺度的局部湍动动能.