静水中气泡上升运动及阻力系数研究

采用模型计算法与实验法结合的方式对静水中气泡上升运动行为进行研究。通过牛顿运动定律，基于不同物理模型，建立气泡在水中运动的微分方程；假设气泡在运动过程中的关键参数取值，推导小气泡在水中浮升过程中的气泡行为预测公式；针对不同流态下的气泡上升关键参数进行适应性分析和算例计算。通过设计气泡上升运动实验，对气泡上升运动公式进行适应性分析，修正关键参数的取值。据此提出一种小气泡上升运动规律的计算方法以及关键参数取值方式及参考区间。     

Fluid-solid coupling and dynamic response of vortex-induced vibration of slender ocean cylinders

对近几十年来国内外在涡激振动的基础研究包括机理认识和动响应分析等方面的进展进行了论述,尤其针对海洋油气平台中的立管、隔水管等细长柔性结构的涡激振动.描述了涡激振动这种典型的非线性流固耦合现象所具有的特征,包括自激、自限制、展向相关、尾迹水动力与结构动力的流固耦合等及其主要影响参数.介绍了目前常用的结构响应预测方法和相关实验.通过讨论当前理论研究和实际工程中的热点问题,诸如多模态宽带振动、浮体运动与水下立管的耦合、响应抑制措施、双向振动、高雷诺数下的大尺度物理实验等,对今后该领域的研究方向进行了力所能及的展望.     

DYNAMIC RESPONSE OF THE CATENARY RISER IN DEEP-SEA MINING SYSTEMS 1)

基于有限元模型,模拟、分析深海采矿系统悬链线立管在海流和水面船运动约束下的动力响应。结果表明：悬链线立管的最大等效应力和最大位移随时间呈周期性变化,且存在半个周期的相位差;当水面船运动到最高点时,悬链线立管位移达到最大值。悬链线立管最大 等效应力和最大位移随水面船运动位移幅值的增加而增加,随运动周期的增加而减小。进一步对比发现,水面船运动位移和周期对立管等效应力的影响大于对其位移的影响。     

提升管喷嘴进料段内气固两相流动的数值模拟

本文采用κ-ε-κ_p-κ_(pg)-θ模型,模拟了提升管喷嘴进料段内三维稠密气固交叉射流的复杂流动现象.结果表明,实验值和模拟值具有相同的变化趋势,再现了提升管喷嘴进料段内颗粒相的流动特点.     

Effect of a pulsating flow on hydrodynamics and fluid catalytic cracking chemical reaction in a circulating fluidized bed riser

The three-dimensional computational fluid dynamics (3D-CFD) of a pulsating flow applied to the fluid catalytic cracking (FCC) reaction was investigated in the riser of a circulating fluidized bed reactor. The kinetic parameters of the FCC and coke burning reactions for predicting the reactant conversion and product yield percentages were applied. To increase the reactant conversion level and product yield, the effect of the pulsating flow operating parameters was considered using a 2^k statistical experimental design with four factors (amplitude, frequency, types of the waveform, and amplitude ratio). The 3D-CFD simulation was successfully validated from the experimental literature data. The frequency and type of the waveform were found to be the significant operating parameters. The expression of the fitted regression model and response surface contour were derived and revealed that the pulsating flow provides a higher reactant conversion level and product yield percentages compared to a non-pulsating or steady flow.     

Particle size distribution in CPFD modeling of gas–solid flows in a CFB riser

A computational particle fluid dynamics (CPFD) numerical method to model gas–solid flows in a circulating fluidized bed (CFB) riser was used to assess the effects of particle size distribution (PSD) on solids distribution and flow. We investigated a binary PSD and a polydisperse PSD case. Our simulations were compared with measured solids concentrations and velocity profiles from experiments, as well as with a published Eulerian-Eulerian simulation. Overall flow patterns were similar for both simulation cases, as confirmed by experimental measurements. However, our fine-mesh CPFD simulations failed to predict a dense bottom region in the riser, as seen in other numerical studies. Above this bottom region, distributions of particle volume fraction and particle vertical velocity were consistent with our experiments, and the simulated average particle diameter decreased as a power function with riser height. Interactions between particles and walls also were successfully modeled, with accurate predictions for the lateral profiles of particle vertical velocity. It was easy to implement PSD into the CPFD numerical model, and it required fewer computational resources compared with other models, especially when particles with a polydisperse PSD were present in the heterogeneous flow.     

Modeling and simulation of severe slugging in air–water pipeline–riser systems

A mathematical model, numerical simulations and stability and flow regime maps corresponding to severe slugging in pipeline–riser systems, are presented. In the simulations air and water were used as flowing fluids. The mathematical model considers continuity equations for liquid and gas phases, with a simplified momentum equation for the mixture, neglecting inertia. A drift-flux model, evaluated for the local conditions in the riser, is used as a closure law. The developed model predicts the location of the liquid accumulation front in the pipeline and the liquid level in the riser, so it is possible to determine which type of severe slugging occurs in the system. The numerical procedure is convergent for different nodalizations. A comparison is made with experimental results corresponding to a catenary riser, showing very good results for slugging cycle and stability and flow regime maps.     

Non-linear finite element analysis of flexible risers in presence of buoyancy force and seabed interaction boundary condition

A non-linear finite element static analysis for flexible risers with large displacements is presented using a four-node pipe elbow element with 24 degrees of freedom. A pipe–soil interaction model is used to identify seabed boundary condition. The effects of buoyancy force as well as steady-state current loading are considered in the finite element solution for riser structures response. In fact considering buoyancy force among with current loading and seabed interaction boundary condition in this paper leads to a particular formulation. The resulting formulation has been implemented in a finite element code which is subsequently used to model and analyze some typical riser configurations. The results of some sample solutions are given to illustrate the accuracy and capability of the formulation.     

带整流罩隔水管流场特性的大涡模拟研究

为了深入揭示整流罩抑制涡激振动的机理，采用CFD软件FLUENT，结合大涡模拟方法，分别对附加整流罩前后隔水管模型的绕流流场进行模拟，将附加整流罩前后隔水管周围的流场特性、升力系数、阻力系数及其频谱特性等进行对比分析．结果表明，整流罩能有效抑制隔水管尾流区的漩涡脱落，隔水管背部的压力升高，升力系数和阻力系数显著降低，从而抑制了隔水管的涡激振动．     

基于聚类算法的提升管内颗粒聚团演化行为研究

本文基于K-means聚类算法对提升管内瞬时颗粒分布图进行图像分割,捕捉颗粒聚团的内部结构及演化过程,并结合聚团区域灰度直方图和分布图研究了有核聚团、颗粒云团以及提升管不同区域聚团演化特性.研究发现当固含率较高时,聚团内部形成致密的核心,且这些聚团相对比较稳定,它们由聚团核心及其周围的颗粒云组成,而在固含率较低时,聚团...