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基于Fluent多相流液压滑阀阀芯摩擦力仿真分析 被引量:8
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作者 陈大为 万熠 +1 位作者 蔡玉奎 刘战强 《机床与液压》 北大核心 2016年第1期134-139,共6页
采用Euler多相流模型、扩展的k-ε湍流模型和SIMPLE算法,基于Fluent软件对滑阀间隙密封内固液两相颗粒湍流进行了数值分析,分析了不同直径和体积浓度的污染颗粒对滑阀阀芯摩擦力的影响。研究结果表明:摩擦力随着颗粒体积浓度增大而近似... 采用Euler多相流模型、扩展的k-ε湍流模型和SIMPLE算法,基于Fluent软件对滑阀间隙密封内固液两相颗粒湍流进行了数值分析,分析了不同直径和体积浓度的污染颗粒对滑阀阀芯摩擦力的影响。研究结果表明:摩擦力随着颗粒体积浓度增大而近似线性增大;随着颗粒直径的变大,摩擦力先增大后减小,直径与间隙厚度很接近的颗粒即"敏感颗粒",会使阀芯表面产生最大的摩擦力,"敏感颗粒"直径为0.012 mm左右;在液压系统中采用合适尺度的过滤网或过滤芯将"敏感颗粒"附近尺寸的颗粒过滤掉以达到减小阀芯摩擦磨损,提高液压滑阀换向性能,进而提高整个液压系统的使用性能。 展开更多
关键词 固液两相流 阀芯摩擦力 颗粒体积浓度 颗粒直径
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分布板气量分布对CFB上升管流动行为的影响研究 被引量:1
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作者 郭庆杰 Joachim Werther Ernst-Ulrich Hartge 《过程工程学报》 CAS CSCD 北大核心 2004年第z1期578-584,共7页
在高8.5 m大型循环流化床上升管中,使用两种类型的气体分布板,通过双探针电容探头,调查了上升管底部区域和上部稀相区域水平向颗粒浓度和颗粒速度分布.上升管底部,水平方向中心区域颗粒体积浓度较低,颗粒体积浓度在靠近床壁明显增大,最... 在高8.5 m大型循环流化床上升管中,使用两种类型的气体分布板,通过双探针电容探头,调查了上升管底部区域和上部稀相区域水平向颗粒浓度和颗粒速度分布.上升管底部,水平方向中心区域颗粒体积浓度较低,颗粒体积浓度在靠近床壁明显增大,最大颗粒体积浓度接近堆积状态下颗粒浓度值.表观气速相同时,高压降分布板颗粒浓度大于低压降气体分布板颗粒浓度.分布板压降对稀相区颗粒体积浓度和颗粒速度曲线没有影响.研究同时发现,分布板压降对稀相区轴向颗粒浓度和颗粒循环量无影响. 展开更多
关键词 循环流化床 颗粒体积浓度 固体速度 固体循环量
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Correlation of Shear Viscosity of Nanofluids Using the Local Composition Theory 被引量:5
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作者 M.S. Hosseini A. Mohebbi S Ghader 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2010年第1期102-107,共6页
In this study,a new method is presented to correlate the shear viscosity of nanofluids by local composition theory.The Eyring theory and nonrandom two-liquid(NRTL)equation are used for this purpose.The effects of temp... In this study,a new method is presented to correlate the shear viscosity of nanofluids by local composition theory.The Eyring theory and nonrandom two-liquid(NRTL)equation are used for this purpose.The effects of temperature and particle volume concentration on the viscosity are investigated.The adjustable parameters of NRTL equation are obtained by fitting with experimental data.The calculated shear viscosities for nanofluids of CuO/water with 29 nm particle size,Al2O3/water with two different particle diameters,36 nm and 47 nm,and CuO/(ethylene glycol,water)are compared with experimental data and the average absolute deviation(AAD)is 1.2%,while the results from some conventional models yield an AAD of 190%.The results of this study are in excellent agreement with experimental data. 展开更多
关键词 NANOFLUID VISCOSITY local composition theory nonrandom two-liquid equation Eyring theory
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Numerical Simulation of Char Particle Gasification
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作者 Syed Shabbar Raza Isam Janajreh +1 位作者 Rizwan Ahmed Ashjan AlKatheeri 《Journal of Energy and Power Engineering》 2015年第8期679-686,共8页
A first principal modeling of the gasification of a char particle is performed using single step mechanism. The char particle is considered to be spherical in shape and only the physical and chemical properties can ch... A first principal modeling of the gasification of a char particle is performed using single step mechanism. The char particle is considered to be spherical in shape and only the physical and chemical properties can change in the radial direction. The carbon dioxide is used as the gasification agent that reacts with the char and form carbon monoxide. The presence of both solid and gaseous phase species makes the reaction heterogeneous. The char particle is considered with varying porosity that also allows the change in the surface area of the particle. A time invariant temperature and pressure profile is used at which the Arrhenius rate constant and diffusion is calculated. The mass conservation of model results in the form of two coupled partial differential and one ordinary differential equation. The equations are solved with a set of initial and boundary conditions using the bulk species concentration at the particle surface. A second order accurate central differencing scheme is used to discretize space while backward differencing is used to discretize time. Finally, the results are presented for the concentration distribution of CO and CO2 in radial direction with respect to time. It shows that, maximum concentration of CO is present at the center of the particle while the concentration gradient becomes higher near the particle surface. The nonlinear concentration trend due to the diffusion is effectively captured. The results show that, completed conversion of char depend upon the time provided for the reaction which can be reduced by decreasing the size of particle or increasing the reaction temperature. The sensitivity study of temperature and initial porosity also performed and showed that temperature has high impact on char conversion as compare to initial porosity. 展开更多
关键词 COAL particle conversion BIOMASS POROSITY CO2 gasification.
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