Difference of pressure makes a liquid flow through a siphon.
压力差使得液体通过虹吸管。
The liquid flow system of a stope is a key for stope leaching.
采场液流系统的研究是就地浸出的关键技术之一。
Automatic Constant liquid flow supply that ensures the average coating.
涂料自动恒流压供给，确保涂覆一致性。
The distribution of falling liquid flow on upright water jet was studied.
研究了竖直射流液体回落的分布规律。
Gradient of liquid level increases with the increase of liquid flow and the height of weir.
液面梯度随液体流量的增加而增加，随堰高的增加而增大。
Traditional well-test models for liquid flow are not consistent with material balance equation.
传统的试井模型与物质平衡方程都是不一致的。
The liquid flow behaviour and mechanism of sugar extraction in the cane diffuser have been discussed.
对床层中液体的流动特性进行了分析，对渗滤式渗出器的糖分渗出机理进行了探讨。
The pump heads are made of PPS, and condensate-repellant surfaces optimized liquid flow paths and fast drying.
泵头由PPS制造，冷凝物防护表面使液体流量和快速干燥达到最佳。
And it also makes use of the microscope simulation ability of FLUENT software on liquid flow and conduct heat.
利用FLUENT软件的流体流动和传热问题的微观模拟功能，找到换热器内部的温度分布。
It has been analysed that liquid flow pattern and liquid crosswise eddy diffusion influence on efficiency of bubble tray.
本文分析了液相流动形态及液相横向扩散对鼓泡型塔板板效率的影响。
The maximum size of the bubbles was obtained through calculating the energy dissipation rate of liquid flow in the shroud.
通过计算套管中注流的能量分散强度，得出了套管中弥散微小气泡的最大尺寸，并采用伯努利方程分析了套管中注流的压力分布。
The hydraulic turbine similarity in the solid-liquid flow has been established, gaining the expressions of the unit values.
然后系统地建立了固液两相流中水轮机的相似准则，得到了单元工作量的表达形式。
The expansion ratio is related to the liquid flow rate, fluidization velocity and free descending velocity of the packing material.
填料膨胀率的大小与液体流量、填料的流化速度及自由沉降速度有关。
Using the model, the liquid holding efficiency and pressure drop of gas lifting flow with liquid flow rate being zero was calculated.
提出了零液流量气提流动的两相流水动力学模型，应用该模型计算了零液流量气提流动的持液率和压力降。
Liquid flow field in a tube with a combination of a stenosis and a bifurcation was measured using refractive index matching technique.
通过折射率匹配方法，应用激光多普勒测速仪测量了突缩与分叉复合管内的液体流场。
Based on the plane and section isoline of fluid potential, the distribution features of liquid flow in the studied areas were analyzed.
在编制流体势平面和剖面等值线图的基础上，分析研究区的流体势分布特征。
An analysis is made on the vapor liquid flow and the heat mass transfer of the wave shaped baffle trays, with emphasis on the mechanism.
阐述波型挡板塔盘气液两相接触流动、传热、传质的机理分析。
A new type of indirect flow control method shows that liquid flow can be controlled with a mass flow controller on the squeeze air system.
介绍了一种新型的调压式流量控制方法，即通过气路安装质量流量控制器的方法对液路流量进行控制。
The comparison of the results of the calculations and the experiments indicates that the model can reflect the true liquid flow on CTST well.
通过与实验结果的对比，结果表明该模型较好地反映了CTST塔板上液体流动的真实情况。
It was summarized in present paper that the liquid flow acted in the transfers process, solidification structure and componential segregation.
文章从传输过程、凝固组织和成分偏析等三个方面对液相流动的作用作了综述。
Based on coupling control of mechanical motion and liquid flow, an automatable adjusting technology for cell position and attitude was proposed.
基于机械运动和流场流动的耦合控制，提出了自动化的细胞位姿调节技术。
A new mathematic model based on analysis of liquid flow, mass transfer and heat transfer is proposed to describe wiped film molecular distillation.
在对刮膜式蒸馏器蒸发表面流体流动和传质传热进行分析的基础上，研究了分子蒸馏过程，并建立了数学模型。
In circle triangle expression liquid flow direction, if the triangle acme outward, showed the liquid flow outputs outward, expressed this is an oil pump.
圆圈中的三角形表示液流方向，如果三角形尖端向外，说明液流向外输出，表示这是油泵。
On the basis of discussion on liquid flow and distribution regular pattern in rotating packing layer, calculating methods of four parts horsepower are found.
在讨论旋转填料层内液体流动及分布规律的基础上，建立起四部分功率的计算方法。
Several spinning procedure conditions were discussed, such as coagulation bath concentration, temperature, extruding rate and core layer liquid flow rate etc.
并对凝固浴浓度和温度、挤出速率、芯液流量等纺丝工艺条件进行了探讨。
The liquid-solid mass transfer coefficients and liquid flow-rate within the catalyst capsule have been measured in a countercurrent flow column by this study.
通过气液在塔内的逆向流动，测定了液固传质系数和催化剂包内流速。
The results show that errors of the model are reasonable acceptable despite the variations of viscosity of liquid, and in a wide gas and liquid flow rate range.
实验数据表明：该计测模型可以适用于多相流中不同粘度的液相流量计量；可适用于较宽的气、液相流量变化范围，模型计测误差稳定在可接受的水平。
The results show that errors of the model are reasonable acceptable despite the variations of viscosity of liquid, and in a wide gas and liquid flow rate range.
实验数据表明：该计测模型可以适用于多相流中不同粘度的液相流量计量；可适用于较宽的气、液相流量变化范围，模型计测误差稳定在可接受的水平。
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