迷宫密封结构对泄漏量和轴系临界转速影响分析研究

通过数值方法对转子-轴承-密封系统动力学模型求解,对3种密封间隙、8种密封直径、8种压差、8种入口损失率和21种密封长度对泄漏量和临界转速的影响进行研究;通过密封结构对轴系临界转速影响规律进行研究,对比分析了有、无密封力作用下转子-轴承-密封系统对临界转速影响。研究结果表明：通过与DYNLAB程序、TASCFlow程序的结果对比分析,该数学模型能较好的模拟计算泄漏量和转子系统临界转速;通过泄漏量影响规律研究,得出泄漏量随着密封间隙、密封直径和密封长度得增大而增大,泄漏量随压差和入口损失率的增大而减小。通过对临界转速影响规律研究,得到考虑密封会提高临界转速,密封长度的变化对临界转速的影响最大、密封间隙的变化对临界转速影响最小。     

逆滞流迷宫密封气流激振特性研究

密封是透平机械减小泄漏的关键部件,其气流激振特性对转子系统稳定性具有重要影响.该研究基于计算流体力学与多频涡动密封动力特性系数识别方法研究逆滞流迷宫密封气流激振特性,计算分析逆滞流喷嘴结构参数及位置对迷宫密封动静特性的影响,揭示其抗气流激振机理.结果 表明:逆滞流喷嘴能有效抑制周向流动,改善密封腔压力分布,提高系统稳定...     

燃气轮机直通式迷宫密封的非稳态流场分析

当叶轮机械的转子发生振动时,转轴与密封件间距发生变化,通过转子密封的泄漏量将与稳态下的数值存在一定的差异.本文旨在通过三维数值模拟对转子振动条件下的泄漏特性进行分析、预测.通过计算发现,转子的振动可增加迷宫密封的泄漏量,并对转子产生一定的气体作用力.     

一种采用迷宫密封的10 K G-M型制冷机研究

提出了一种采用迷宫密封的10K G-M型制冷机,对迷宫密封的机理进行了简要的理论分析,给出了这种新型10K制冷机的结构参数,建立了实验平台,给出实验降温曲线和制冷量曲线。研究证明,这种采用迷宫密封的10K G-M型制冷机是一种技术上较为完善并且更具实用性的10K温度范围的新型G-M制冷机。     

小间隙直通迷宫密封流场与泄漏特性数值模拟

采用RNGκ—ε模型对小间隙(<0.1 mm)直通迷宫密封可压缩定常湍流场进行数值模拟,得到通道内的速度、温度等流场典型分布。通过改变密封间隙、齿深等,得出通道内最大马赫数及泄漏曲线趋势图。结果表明小间隙时直通迷宫密封内存在齿尖节流、空腔膨胀及射流偏转、复热等主要特征,而小间隙下增加齿深会降低泄漏量。     

连锁迷宫密封-转子轴承系统动态特性系数的影响因素研究

基于振荡流体力学原理进行数值计算分析.本文对进出口压比、密封间隙和密封齿数(密封长度)对连锁迷宫密封-转子轴承系统动态特性系数的影响进行了详细的分析.结果表明,连锁迷宫密封-转子轴承系统动态特性系数的影响因素是多方面的.     

迷宫密封-转子系统非线性动力学模型及求解

摘 要：迷宫密封广泛应用于各种旋转机械,研究密封内流体与转子的相互作用,对系统稳定性分析有重要意义。本文利用双控制体模型给出迷宫密封内不可压缩流场的控制方程,并用Jeffcot模型对转子-密封系统建模,求解此非线性动力模型得到系统转子位移与密封腔内压强的数值解。以不平衡转子-密封系统为例,计算分析系统非线性动力特性,并用Hopf分岔图与Poincare截面图进行直观表示。结果表明减小转子质量偏心对提高系统稳定性有较大影响。     

非线性转子-密封系统动力学模型研究

针对线性化密封系统较难准确描述转子系统运动特点问题,基于双控体模型与转子运动方程提出新的非线性密封力模型研究转子运动特点。为研究密封力对转子系统影响,采用该非线性密封力模型通过绘制转子轨迹图、庞加莱图及分岔图分析转子密封系统运动特征,为进一步深入研究转子密封系统提供参考。     

基础振动作用下转子‑轴承‑密封系统动力学分析

针对受不平衡质量、轴承油膜、密封流体及基础振动多激励共同作用的转子系统,采用Lagrange 法建立其动力学模型,以Runge?Kutta 法求解系统非线性状态方程,绘制频谱图、分岔图和轴心轨迹来分析系统的动力学特性,并引入振动烈度评估转子的振动水平。对比分析了基础振动对转子系统的非线性动力学特性及失稳转速的影响,并研究了基础振动的形式、频率及幅值对系统动力学特性的影响。结果表明,基础振动使得系统稳定性降低,其对转子系统动力学响应的影响具有明确的方向性。     

多级串联密封系统泄漏仿真与实验研究

建立了多级串联密封系统的数学模型,通过理论分析和数值计算,揭示了多级串联密封结构正压泄漏的漏率、漏量与泄漏时间关系的一般规律.给出了三级密封系统泄漏的仿真计算实例.通过三级串联密封泄漏实验验证了多级串联密封泄漏理论的正确性.该泄漏规律可用于多级串联密封结构系统的设计、检漏和泄漏安全评估.     

双螺杆挤压机操作参数对加工质量影响的研究

通过实验研究了双螺杆食品挤压机的机筒温度、供料速度、螺杆转速对产品质量(以比容衡量)的影响规律,建立了相应的统计模型,并对操作参数进行了优化.研究表明,随着机筒温度的升高,比容呈增大趋势,螺杆转速与供料速度对比容的影响较复杂,与比容之间的关系呈非线性.当机筒温度在160～166℃之间,螺杆转速在143～147(r·min-1)之间,供料速度在20.6～21.4(r·min-1)之间时,加工质量较高,比容大于2.4(mL·g-1).     

低温绝热气瓶漏放气性能的研究

以低温绝热气瓶为研究对象,设计并搭建气瓶漏放气及残余气体分析实验台,开展了室温和低温下容器漏放气和残气分析的实验研究。通过理论分析与实验研究相结合得出:室温下,气瓶真空夹层内残余气体中H2的含量约为70%,可以利用复合材料扩散放气模型预测低温绝热气瓶的漏放气;低温下,气瓶真空夹层内残余气体中H2的平均含量达到81%,可以利用金属材料扩散放气模型预测低温绝热气瓶的漏放气。本文的研究有助于推动真空维持技术的应用,对于提高高真空多层绝热低温容器产品的寿命、降低成本和确保产品的可靠性,都具有十分积极的意义。     

分形模型参数与粗糙度参数Ra关系的研究

介绍了W－M分形模型参数（D,G,γ）的物理含义，研究了分形参数（D,G,γ）与粗糙度参数Ra之间的联系，导出了分形参数（D,G,γ）与粗糙度参数Ra关系式，用数值分析拟合方法验证了关系式的正确性。     

三维正交机织复合材料的单胞模型及应用

根据三维正交机织复合材料的结构特点,在假设纤维束横截面为矩形的基础上建立一种单胞模型,该模型由3组互相正交的纤维与基体组成。首先利用这一模型,推导出纤维体积分数与纤维粗度、机织密度等织物参数的关系式,通过测量单胞单元的单层厚度得到纤维体积分数,计算值和实验值较为吻合。然后在假定纤维和基体均为线弹性材料的基础上,利用材料力学方法推导出了3 个正交方向的杨氏模量表达式,该表达式简单明了,给出了三维正交机织复合材料杨氏模量与纤维和基体的杨氏模量以及纤维体积分数间的关系,算例的计算结果与实验值有良好的一致性,这说明所建立的单胞模型具有合理性。     

Study of viscosity of mono-, di-, and trialkylamines

Viscosities of several mono-, di-, and trialkylamines have been measured in the temperature range 298 to 333 K. It is observed that viscosities are highly dependent on shape, size, and association through H-bond or through dipole. Following the transition state theory, energy, Gibbs free energy, and entropy of activation of viscous flow have been calculated. The values of expansion energy for these liquids have also been calculated using free volume theory, and subsequently amines have been classified as volume-restrained or energy-restrained liquids. The group contribution method of Van Velzen, Cardozo, and Langenkamp for estimating viscosity has been examined with the present and literature data, and the new group contribution increments N _i and B _i for amines have been evaluated.     

Measurement and analysis of impact dynamics suitable for modelling pneumatic transport of metallic powder flow through a directed energy deposition nozzle

In blown powder directed energy deposition (DED) additive manufacturing powdered metal feedstock is pneumatically conveyed to the meltpool via a nozzle. DED nozzles have been the subject to a growing number of research efforts using computational fluid dynamics (CFD) with multiphase flows to study and optimize powder flow. However, many research papers published to date contain powder – nozzle impact dynamics behavior that is not realistic or not derived from experiments that resemble the powder conveyance process in the DED nozzle being studied. To provide a set of data representative of DED powder flow through a nozzle particle image velocimetry (PIV) experiments were conducted using 316L stainless steel metal powder and flat targets with varying surface roughness made of oxygen free copper, mild steel, P20 tool steel, 316L stainless steel, Inconel 718, and Ti-Al6-V4. Normal coefficients of restitution (COR) were calculated and compared to several analytical and empirical models in literature.     

CFD modelling and simulation of an industrial scale continuous fluidized bed roaster

In the present work, computational fluid dynamics (CFD) based modelling of an industrial scale continuous fluidised bed roaster (FBR) has been carried out to study its performance at different operating conditions, so that the sulphide-sulphur content in the product is within 0.4% at the designed feed rate of 39.75 DMT/h. Eulerian-Eulerian multiphase model, considering four granular phases and one gas phase has been implemented to investigate the velocity and mass fraction profile of the particles in the FBR. The heat and species mass balance calculations have been performed external to CFD, by dividing the roaster into several sections. The conversion of ZnS to ZnO at various sections of the roaster has been estimated using reaction kinetics under isothermal condition (1203 K). The heat liberated and possible temperature rise at each section was predicted based on the heat of reaction and sensible heat of the solid and gaseous products. The CFD model was validated with the plant data for a feed rate of 36.5 DMT/h, air flow rate of 65,000 Nm³/h and O₂ content of 21%. The proposed model predicted the sulphide-sulphur content in the product to be 0.4% for the designed feed rate of 39.75 DMT/h, when the O₂ content in the inlet air was increased to 25%.