二维孔口紊动射流流场特性的实验研究

对一定水深下的孔口射流流场进行了一系列测试，研究了轴对称流动下轴心流速衰减和横断面上流速分布等特性，并总结归纳出其变化规律。     

晋城矿区综采放顶煤工作面顶煤冒放性分析

根据晋城煤业集团综采放顶煤开采实际情况,从影响顶煤冒放性的煤体裂隙、开采工艺和支架与围岩关系3个方面进行分析,对综放工作面的布置、采放比、放煤步距、支架架型与工作阻力提出了建议.     

复杂外形火箭导弹三维绕流与喷流干扰流场的数值模拟

该文基于雷诺平均三维Navier-Stokees方程及k—ε模型，采用高精度的有限体积TVD格式以及多重网格Runge-Kutta时间推进算法对在超声速有攻角条件下带尾翼／弹翼的弹箭绕流与喷流干扰流场进行了数值模拟。获得了绕流和喷流相互干扰的波系结构，以及弹翼与尾翼、弹翼／尾翼与弹体相互作用的复杂流场，分析其流动现象，揭示了流动规律，为火箭导弹合理的气动布局提供依据。     

新型Al-Mg-Si-Cu合金热压缩流变应力研究

在Gleeble 1500热模拟机上对一种新型Al-Mg-Si-Cu合金热压缩流变应力行为进行了研究,应变速率为 0.005~5 s-1、变形温度为350~550 ℃.结果表明:在较小应变(<0.15)出现一峰值后流变应力随应变的增加有所降低,表现出较明显的动态软化;在实验范围内,流变应力值随着应变速率减少和变形温度升高而降低,可用Zener-Hollomon参数的幂指数关系描述合金的流变应力行为,其变形激活能Q为236 kJ/mol.图5,参11.     

入渗、蒸发条件下土壤水分运动的数值模拟

应用特征有限元法，对以含水率θ为因变量的一维非饱和土壤水分运动模型在入渗、蒸发条件下进行离散化，得到了该模型的特征有限元数值模型，所得数值模型形式简单、计算精度高、用时少，符合实际工作要求。     

冲击破煤过程中能量耗散的理论分析

介绍了能量在冲击式破煤过程中的产生、传递和耗散过程以及能量最终的分布范围;运用应力波的方法分析了应力波在煤体中传播过程,并得出能量在衰减过程中衰减率的计算方法;还分析了剥落厚度的计算方法,并得出正弦应力波在煤体中传播时的冲劈厚度和最大煤块尺寸的关系;根据冲击规律和能量的传递特征对能量的传递过程进行了分析,并求出冲击消耗能量和最小散逸能之间的关系,指出了要使煤块破碎必须满足冲击消耗能量要大于最小散逸能。     

复合材料风机叶轮内流场数值模拟

应用粘性流体力学的基本原理,采用专业流体力学软件对复合材料风机叶轮内气流流动进行数值模拟,发现叶轮内气流流动状况不理想,据此对叶轮的叶片进行改进设计,得到了改进叶片设计后叶轮内的流场,改进了复合材料风机叶轮的结构,改善了叶轮内部气流的流动状况,提高了叶轮的气动性能,为研制出高性能的新型复合材料风机叶轮奠定了基础。     

煤与生物质共超临界水催化气化制氢的实验研究

在压力为20～25MPa、停留时间为15～30s、：NaOH添加量(质量分数)为0．1％、反应器外壁温度为650℃的条件下，对煤与生物质的模型化合物羧甲基纤维素钠(CMC)在超临界水环境中的催化气化制氢性能进行了研究，探讨了物料浓度、压力以及停留时间对煤与CMC共气化制氢的影响．实验结果表明：煤与CMC二共超临界水催化气化制氢的主要气体产物是H2、CO2和CH4，H2的体积分数可高达60％以上；增加物料浓度、升高压力有利于提高产氢率，但延长停留时间不利于氢气的制取．     

Computational fluid dynamics for dense gas-solid fluidized beds

Many computational fluid dynamics (CFD) models for describing the hydrodynamics of dense gas-solid flows in fluidized beds have been put forward in the past few decades. These models treat the solid phase as continuum or discrete particles, which leads to Eulerian-Eulerian or Eulerian-Lagrangian formulations, respectively. Different governing equations and closure relations essentially result from an insufficient understanding of the complex gas?particle and particle?particle interactions for gas?solid flows. The current status of these models is discussed briefly in this paper. All the approaches in the literature modify only the solid phase momentum balance equation introducing various forms of the solid phase stress tensor and the solid phase pressure drop in the Eulerian-Eulerian models. Taking them into consideration, a new model for predicting the fluid behavior of dense gas?solid flows in fluidized beds has been developed, which contains new terms in both the particle and gas phase momentum balance equations and requires only the use of an experimental drag force correlation. Several results are shown to verify the model’s reliability, which include the homogeneous fluidization of Geldart type A particles, the bubbling and jetting fluidization of Geldart type B particles in rectangular beds, and fluid dynamics in a complicated geometry for a bubbling?bed of a fast internally circulating fluidized?bed biomass gasifier.     

The fate of injectant coal in blast furnaces: The origin of extractable materials of high molecular mass in blast furnace carryover dusts

The aim of the work was to investigate the fate of injectant coal in blast furnaces and the origin of extractable materials in blast furnace carryover dusts. Two sets of samples including injectant coal and the corresponding carryover dusts from a full sized blast furnace and a pilot scale rig have been examined. The samples were extracted using 1-methyl-2-pyrrolidinone (NMP) solvent and the extracts studied by size exclusion chromatography (SEC). The blast furnace carryover dust extracts contained high molecular weight carbonaceous material, of apparent mass corresponding to 10⁷?10⁸ u, by polystyrene calibration. In contrast, the feed coke and char prepared in a wire mesh reactor under high temperature conditions did not give any extractable material. Meanwhile, controlled combustion experiments in a high-pressure wire mesh reactor suggest that the extent of combustion of injectant coal in the blast furnace tuyeres and raceways is limited by time of exposure and very low oxygen concentration. It is thus likely that the extractable, soot-like material in the blast furnace dust originated in tars is released by the injectant coal. Our results suggest that the unburned tars were thermally altered during the upward path within the furnace, giving rise to the formation of heavy molecular weight (soot-like) materials.