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This indicates that all the solids and liquids with a certain size can be acoustically levitated on the earth in principle.

这不仅证实了本文所提出的单轴式声悬浮优化设计理论,同时还表明,声悬浮原则上可以在地面条件下悬浮起一定尺寸的任何固体和液体。

Using Phase Doppler Anemometry , the size of the particles in every suspending layer is measured and the conclusion above is verified.

在综合管中非线性效应而对颗粒悬浮过程的分析中发现,管中声流在颗粒悬浮层的形成过程中扮演重要的角色,不同强度的声流下会有不同大小的颗粒被悬浮起来,PDA测量结果证实了这一结论。

Systematic study is carried out to the main factors that influence the levitation stability during containerless processing of materials. The effect of the medium density r f , sound speed c , gravitational acceleration g , and resonant states Hm on the acoustic containerless processing is revealed.

对材料声悬浮无容器处理过程中,影响悬浮稳定性的主要因素进行了深入研究,揭示了媒质密度 r f ,声速 c ,重力加速度 g 和声场谐振状态 Hm 对声悬浮过程的影响机制。

The performance of magnetic suspension is determined mainly by its control system. Due to the inherent nonlinearities and open-loop instability of the magnetic suspension system, as well as the problem of uncertainties caused by parameter variety and disturbance, increase the difficulty of magnetic suspension control technology.

悬浮性能的好坏主要取决于控制系统的设计;由于悬浮系统本身固有的非线性特性和开环不稳定性,以及参数摄动和外干扰引起的不确定性等问题,增加了悬浮控制技术的难度。

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有机复合阳离子絮凝(使液体中悬浮微粒集聚变大或形成絮团,从而加快粒子聚沉,达到固-液分离的过程)剂是利用化学法合成的一种新型阳离子絮凝(使液体中悬浮微粒集聚变大或形成絮团,从而加快粒子聚沉,达到固-液分离的过程)剂,属国内外首创,与其他常规药剂相比具有五大优点:与常用药剂聚合氯化铝、聚合硫酸铁、硫酸铝等相比,与聚丙烯酰胺类絮凝(使液体中悬浮微粒集聚变大或形成絮团,从而加快粒子聚沉,达到固-液分离的过程)剂联合使用,药剂量少,从而降低废水处理(通过物化方法去除水中一些物质的过程)费约20%—30%;处理废水效果好,絮团沉降速度快,使废水能再生利用,节约水资源;其絮团沉渣过滤性能好,煤泥可全部厂内回收,即节能又有利于保护环境;对设备腐蚀小;具有多功能,既有凝聚作用,又有絮凝(使液体中悬浮微粒集聚变大或形成絮团,从而加快粒子聚沉,达到固-液分离的过程)作用和助滤作用,可作为助滤剂。

This model builds up the relationship between the levitation capabilities and the geometric parameters of a single-axis acoustic levitator, and proves to be successful in predicting resonant modes, Hm ( m =1, 2, 3, 4), and in explaining the axially symmetric deviation of the levitated samples near the reflector and emitter.

该模型揭示了声悬浮性能和以声波长为参考的悬浮器几何参数之间的本征关系,成功地预测声场的谐振模式 Hm ( m =1, 2, 3, 4为模式数, Hm 为反射端-发射端谐振间距),并解释了反射端和发射端附近的悬浮样品偏离对称轴的实验现象。

Compared to the conventional magnetic suspension,the significant characteristic of the electrostatic suspension is that it is capable of suspending most of the conductive and/or nonconductive,magnetic and/or nonmagnetic objects.

静电悬浮方法的显著特点是既适用于导电体与非导电体的悬浮,又适用于磁性体与非磁性体的悬浮,克服了传统磁悬浮技术仅适用于磁性体的局限性,可广泛应用于精密元器件的悬浮与非接触无损操作。

The zinc oxidation leaching ratio can reach 86.73% in 96h. The oxidation mechanisms of zinc sulphide concentrate in different suspension electrolysis solution are almost same. However, the exchange current density in the process of oxidation is low and it will quicken electrochemical oxidation with the increasement of temperature.

通过实验分析得出:硫化锌矿在不同悬浮电解溶液中都能够被氧化,但有较大的差别,在硫酸锌、硫酸铵和硫酸的悬浮电解液中,矿物明显被氧化而溶解进入悬浮液中,氧化速度比较快,锌的氧化溶出率在96h的时间内达到86.73%。

Oxidizing feature which is oxidizing leaching of every element, studied kinetics of anode oxidation, analyzed oxidizing slag with XRD and SEM during suspension electrolysis of zinc sulphide mine. The results show that zinc sulphide concentrate in different suspension electrolysis solution can be oxidized. However, the ore in zinc sulphide, ammiaonia sulfate and sulfuric acid suspension electrolysis solution can be oxidized obviously and has better oxidation rate.

确定了硫化锌矿悬浮电解时的电解液后,我们又对硫化锌矿在悬浮电解过程氧化特征即矿物氧化时其中各元素的氧化溶出情况进行分析,对阳极氧化进行了动力学研究,对氧化渣进行XRD和SEM分析,以了解其含锌矿物在悬浮电解过程中的氧化规律,还进行了渣中元素硫的回收。

We put zinc sulphide mine into different sulphate system and analyzed polarization curve about anodic oxidation.we found that the mine was oxidized effectively and the rapid oxidation happened when we adopted the zinc sulphide ore suspension electrolyte which contained ZnSO_4,(NH_4)_2SO_4 and H_2SO_4. This system was suffice to product metal zinc industrially. The appropriate suspension electrolyte composition consisted of zinc 90~130g/l,(NH_4)_2SO_430~50g/l, H_2SO_430~50g/l, suspension electrolysis temperature 50℃, anodic oxidation potentiometer 0.6~0.8V.

研究了硫化锌矿在不同的硫酸盐体系中的溶解,通过阳极氧化极化曲线进行分析,得出当以硫酸锌、硫酸铵和硫酸作为硫化锌矿悬浮电解液时,矿物能够有效地被氧化,氧化速度最快,能满足工业上生产金属锌的要求,并且合适的悬浮电解液组成为:锌90~130g/l,硫酸铵30~50g/l,硫酸30~50g/l,悬浮电解温度40~50℃,阳极氧化电位0.6~0.8V。

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