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1)  area turbulent kinetic energy
面积湍动能
2)  interfacial turbulence
界面湍动
1.
Influence of interfacial turbulence on gas-liquid mass transfer;
界面湍动对气液传质的影响
2.
Optical observation and analysis of the interfacial turbulence in mass transfer processes of gas-liquid systems;
气液传质相界面湍动现象的实验及分析
3.
Influence of interfacial turbulence on the mass transfer rate in physical absorption processes;
吸收过程中界面湍动对传质的影响
3)  Turbulence Kinetic Energy
湍动能
1.
At the centre of the section near the top of burners,its rising velocity is minimum,its turbulence kinetic energy is maximum,and its temperature is maximum too.
结果表明 ,大空间锅炉炉膛的速度场、温度场分布很不均匀 ;燃烧器上部附近的炉膛中心烟气上升速度最小 ,湍动能最大 ,温度最高 。
2.
Then the result of turbulence kinetic energy of numerical simulation near the roof in the 90° direction was present,which was used to analyse the rule of distribution of fluctuating wind pressure on the cantilever.
随后给出90°风向下贴近屋盖面上数值模拟湍动能,以此分析悬挑屋盖面上脉动风压分布规律,且用风洞实验的脉动风压均方根值结果进行验证。
3.
By performing a number of experiments on the turbulence kinetic energy of smooth plate surfaces and different V-riblet surfaces in various sizes at different wind velocities,the distributing rule of the turbulence kinetic energy over the riblet surfaces in the boundary layer is acquired.
通过对不同风速下不同尺寸V型沟槽表面及光洁平板表面边界层内湍动能的测试,对比分析了沟槽表面边界层湍动能的分布规律。
4)  turbulent kinetic energy
湍动能
1.
The varying rule of vertex center depth and the distribution of turbulent kinetic energy in the mould have been studied when the structure and size of submerged entry nozzle(SEN) and processing parameters are changed.
根据湍流理论及异形坯连铸的特点 ,建立了异形坯结晶器三维流场数学模型 ,对不同条件下的流场进行了数值模拟 ,分析了水口结构和工艺参数变化时异形坯结晶器内涡心深度的变化规律及液面湍动能的分布状态。
2.
The static pressure,turbulent kinetic energy, streamlines distributions and external performance were analyzed and compared.
结合外特性预测结果、内部静压、流线和湍动能分布,讨论了低比转速消防泵性能影响因素,得出以下结论:叶片出口角和叶片数对扬程和驼峰的影响较明显,增加分流叶片后,扬程提高明显;增加合理布置的分流叶片可以提高泵的扬程和效率,改善叶轮内部流动和湍动能分布;泵体的喉部面积对性能影响非常敏感,其可以有效控制高效区范围和最高效率。
3.
In order to study the interaction between two spheres and the effect of different space on wake and turbulent kinetic energy,numerical simulations on five cases between L=2.
为了研究不同间距下并列双圆球的相互作用以及对尾涡和湍动能的影响,本文选取在L=2。
5)  turbulent kinetic energy
湍流动能
1.
Average velocity and turbulent kinetic energy k distribution were obtained.
476m的六直叶涡轮桨搅拌槽内,采用粒子图像测速仪(PIV)对桨叶区的流场进行了实验研究,得到了桨叶区的平均流速和湍流动能(k)分布,采用大涡PIV方法对湍流动能耗散率(ε)分布进行了估算,计算了ε与k的相关系数。
2.
Based on the tendency equation of turbulent kinetic energy, its simplified equation including only wind shear and air stability was derived.
基于湍流动能倾向方程,推导出了其只含风切变和大气稳定度的简化方程。
3.
The distribution of Reynolds shear stress and turbulent kinetic energy was described and the correlation of these two quantities was discussed.
简述了在西北工业大学低湍流度风洞中,用热线风速仪对翼型边界层及近场尾流中雷诺正应力及切应力等的测量结果,着重讨论了雷诺切应力及湍流动能的分布规律及相关特性。
6)  turbulence kinetic energy
湍流动能
1.
), turbulence kinetic energy and sensible heat flux are calculated and their characters are analyzed under different stability and compared with the r.
采用2000年8月在美国加州棉花地两个高度上应用超声三分量仪、快速响应温度和湿度仪进行的EBEX2000(InternationalEnergyBalanceExperiment,2000)风速三分量、温度和湿度湍流实验观测数据,计算分析了湍流宏观量(即u,T,σu/u,σv/u,σw/u和σT/T等),湍流动能和感热通量等的特征,并与其他湍流实验得到的结果进行了比较。
补充资料:比释动能


比释动能
kinetic energy released in material; kerma

bishi由叩neng比释动能(kineticene卿rele胎ed in Irlaterial;ke~)剂量学量之一。1958年,w.c.勒施提出单位质t所释放的动能的概念,称为kerm(kinetiee”e咬万回eaa司卿画t~),反映不带电粒子辐射与物质相互作用中的能t传递。后又采用比释动能ke~(七杨。ene耳妙花1以曰妇inm川e‘目),符号为K。比释动能的定义为dE。除以dm所得的商,即 K== dE,/dm式中dE。为不带电粒子在质量为dm的物质中所释放的所有带电粒子的初始动能之和。sI单位为凡一‘(焦耳每千克),专用单位为仰(戈〔瑞」)。适当选择物质中的比释动能,可以方便地描述不带电粒子的辐射场,例如空气比释动能、组织比释动能等。 (吕维纯徐涌)
说明:补充资料仅用于学习参考,请勿用于其它任何用途。
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