基于VOF模型的层叠器流动过程分析及流道结构优化

基于FLUENT软件的流体体积(VOF)模型研究了不同壁面滑移程度以及不同流道结构参数下4层等厚熔体通过层叠器倍增为8层熔体时,流道中熔体的分层情况变化。结果表明,壁面滑移程度的降低会促使熔体在上下壁面聚集,进而导致上下壁面处熔体层厚增加;汇流段与出口段间圆角半径、汇流段扩压角和平衡段长度这3个结构参数则只会影响熔体在左右壁面的聚集,进而影响各层熔体的尺寸精度,且其中扩压角的影响程度最大,平衡段长度次之,圆角半径的影响较小。     

Numerical and experimental investigation of the metering characteristic and pressure losses of the rotary tubular spool valve

This paper presents the results of numerical and experimental performance evaluation of the rotary tubular spool valve. The aim of this work is to develop further the novel design of the tubular spool valve by confirming experimentally the validity of the simulation model and its results, thereby proving the valve's potential to represent a feasible and more efficient alternative to conventionally used translation spool valves avoiding the use of two stage valve configurations. In this research the valve performance is assessed through numerical modelling and experimental studies of its metering characteristic and pressure losses. This paper demonstrates that the used valve model yields the results, which agree well with the conducted experimental study. Therefore, validation of the numerical model and the modelling results in the form of theoretical valve characteristics was accomplished. Firstly, the paper presents details of a numerical approach employed to evaluate valve performance and then analyzes the simulation results. Next, the valve performance is experimentally validated by testing a prototype valve on a hydraulic test rig capable of measuring the volume flow rate, pressure levels in up- and downstream lines of the valve across the entire spool angular stroke. Initially, average discrepancies between modelling and test results were 52.46% for the metering and 82.78% for the pressure loss characteristics. Correcting the model geometry aimed at eliminating differences between the valve model and the practically used prototype-test rig system enabled reduction of the error between experiment and modelling by 47.75% for the pressure loss function. This confirmed validity of the simulated characteristics of the valve. The benchmark comparison of pressure losses confirmed average 71.66% energy dissipation reduction compared to the industry-available analogue valve.     

基于直剪试验的页岩水化作用的强度弱化规律

随着页岩气资源的不断开发,水平井段的硬脆性页岩井壁失稳问题也越来越突出。为此,通过对水基、油基钻井液浸泡后的页岩岩样直剪试验,并结合单组弱面强度理论,分析了内聚力和内摩擦角对页岩强度的影响规律以及不同钻井液浸泡后的页岩强度弱化规律。对试验数据的分析结果表明:①水基、油基钻井液浸泡后内聚力和内摩擦角均下降,其垂直层理面方向的内摩擦角和内聚力均高于平行层理面方向;②页岩强度随钻井液浸泡时长增加而降低,受水化作用影响层理面导致强度降低,微裂缝表现为更易扩展,页岩容易产生破坏;③内聚力控制页岩强度大小,内摩擦角控制页岩沿弱面破坏的范围;④水基钻井液对页岩影响较为明显,页岩受其浸泡后强度下降较快,并随浸泡时间增加页岩强度持续下降,同时沿弱面破坏的角度限明显增大,油基钻井液能较好地保持岩样强度水平。最后,以四川盆地志留系龙马溪组M气藏为例,通过水平井段坍塌压力的计算,认识到水基钻井液基本不能满足钻井要求,而应采用油基钻井液且优先考虑沿最小水平地应力方向钻进。     

Numerical Simulation of Interfacial Closures for 3D Bubble Column Flows

Numerical investigation of flow hydrodynamics in a square cross‐sectioned bubble column was conducted in a transient Euler‐Euler environment by applying the simulation tool Ansys CFX 14.0. The influence of the drag coefficient (C_D) was investigated and the results were also compared with drag force models. Furthermore, three different lift force models and a defined lift coefficient were studied. All results were compared with the available experimental data. All simulations were carried out for a single‐hole sparger with given aspect ratio (H/D) and superficial gas velocity.     

Modeling and simulation of hydrogen production from dimethyl ether steam reforming using exhaust gas

In this paper, hydrogen production from steam reforming of DME (dimethyl ether) has been modeled and simulated using a CFD (computational fluid dynamics) method. The reformation chemistry occurs in a porous catalytic bed where exhaust gas is supplied through the EGR (exhaust gas recycling) valve of the engine to drive the endothermic reaction system. The tightly coupled system of mass, energy, and momentum equations are used to describe the complex physical and chemical process of DME steam reforming. The global reaction kinetics for the reforming is adopted in the CFD model. The mathematical models are introduced into the commercial software Comsol, and then numerical simulations are also performed based on this model. The model predictions are quantitatively validated by experiment data. The simulation results indicate the temperature distribution, mass distribution, DME conversion, and hydrogen production from steam reforming of DME. In addition, the fuel to steam ratio and velocity of exhaust gas are manipulated as operating parameters. These simulation results will provide helpful data to design and operate a bench scale catalytic fluidized bed reactor. Copyright © 2015 John Wiley & Sons, Ltd.     

Computational modeling of heat transfer in magneto-non-Newtonian material in a circular tube with viscous and Joule heating

Numerous industrial and engineering systems, like, heat exchangers, chemical action reactors, geothermic systems, geological setups, and many others, involve convective heat transfer through a porous medium. The diffusion rate, drag force, and mechanical phenomenon are dealt with in the Darcy–Forchheimer model, and hence this model is vital to study the fluid flow and heat transport analysis. Therefore, numerical simulation of the Darcy–Forchheimer dynamics of a Casson material in a circular tube subjected to the energy losses due to the viscous heating and Joule dissipation mechanisms is performed. The novelty of the present investigation is to scrutinize the convective heat transport characteristics in a circular tube saturated with Darcy–Forchheimer porous matrix by utilizing the non-Newtonian Casson fluid. The flow occurs due to the elongation of the surface of a tube with a uniform heat-based source/sink. The similarity solution of the nonlinear problem was obtained using dimensionless similarity variables. The effects of operating parameters related to the flow phenomena are analyzed. Further, the friction factor and Nusselt number are also analyzed in detail. The present flow model ensures no flow reversal and acts as a coolant of the heated cylindrical surface; the existence of the magnetic field, as well as an inertial coefficient, acts as the momentum-breaking forces, whereas Casson fluidity builds it. The Joule heating phenomenon enhances the magnitude of temperature. The thermal field of the Casson fluid is higher at the surface of the circular pipe due to convective thermal conditions.     

Analysis of a magnetic field and Hall effects in nanoliquid flow under insertion of dust particles

In this study, the two‐phase hydromagnetic flow of a viscous liquid through a suspension of dust and nanoparticles is considered. The influence of the Hall current is also taken into account. The similarity variables are utilized to transform the problem into one independent variable. The obtained expressions in one independent variable are solved through the Runge–Kutta–Fehlberg scheme connected with the shooting procedure. The computed results are sketched for employing multiple values of physical constraints on the temperature and velocity of the nanofluid and dust phase. The characterization of various nanoparticles like Cu, Al₂O₃, TiO_2, and Ag on velocities and temperatures of both phases is made through plots. A comparative analysis in the limiting approach is presented to justify the present solution methodology. The range of emerging parameters is taken as 0 ≤ l ≤ 3, 0.1 ≤ β_t ≤ 3, 0 ≤ m ≤ 2.5, 0 ≤ M² ≤ 2, 0.1 ≤ β_v ≤ 3, 0 ≤ ? ≤ 0.4, and ?0.8 ≤ λ ≤ 0.8. From the study, it is revealed that β_t has the opposite effect on the temperature of dust and nanofluid phases. The Hall parameter m raises the profiles of velocities in the nanoliquid and dust phases. Also, it is found that the transverse velocities h(η) and H((η) and temperatures θ(η) and θ_p(η) rise for larger ?.     

考虑流固耦合的Spar型浮式风力机涡激运动特性研究

对弹性支撑单圆柱在均匀流作用下的涡激运动特性进行数值模拟,捕捉到"锁定区"、"拍"、"频率变换"等现象。柱体周围流场采用Fluent求解,将4阶Runge-Kutta方法代码写入用户自定义函数(UDF)求解运动微分方程,运用动网格技术更新流场,实现圆柱与流场的非线性耦合作用。发现随着折合速度的增大,涡激运动响应可分为锁定前支、锁定区、锁定后支3个阶段,在进入锁定区前(折合速度Ur=3)横向运动响应发生拍现象,当跨过锁定区后(折合速度Ur=10)发生频率变换现象。结果表明,横向涡激运动有较大范围的频率锁定现象,频率解锁前后圆柱涡激运动轨迹由"右8字"形变换为"左8字"形。     

竖直提升管内气泡运动状态数值模拟研究

在Einstein制冷循环系统中，气泡泵竖直提升管内为弹状流时效率较高。选取VOF（流体体积函数）模型对其管内气泡的运动状态进行计算流体力学数值模拟。结果表明：当过热度恒定时，随着压力增加，单个气泡的生成时间延长且体积变小，但气泡均匀性提高；当压力恒定时，随着过热度增大，气泡生成速率加快，融合体积增大，易于形成系统所需的弹状流。因此，在Einstein制冷循环系统中，在压力为0.4 MPa的工况下，需采取较高的过热度才能保证气泡泵的正常运转；与水相比，氨水溶液更适合作为气泡泵工质。     

Steady MHD Casson Ohmic heating and viscous dissipative fluid flow past an infinite vertical porous plate in the presence of Soret,Hall, and ion‐slip current

In the present study, the influence of Hall and ion‐slip current on steady magnetohydrodynamics mixed convective, Ohmic heating, and viscous dissipative Casson fluid flow over an infinite vertical porous plate in the presence of Soret effect and chemical reaction are investigated. The modeling equations are transformed into dimensionless equations and then solved analytically through the multiple regular perturbation law. Computations are performed graphically to analyze the behavior of fluid velocity, temperature, concentration, skin friction, Nusselt number, and Sherwood number on the vertical plate with the difference of emerging physical parameters. This study reflects that the incremental values of Casson fluid parameter and Schmidt number lead to reduction in velocity. However, fluid velocity rises due to enhancement of ion‐slip parameter but an opposite effect is observed in case of Hall parameter. In addition, the Sherwood number declines with enhancing dissimilar estimators of the chemical reaction, Schmidt number, as well as Soret number.