共查询到20条相似文献,搜索用时 140 毫秒
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对某台300 MW W火焰锅炉进行超低排放改造,改造采用新型低NOx燃烧系统,采用数值模拟方法研究了不同周界风及油风风率对锅炉燃烧特性影响。数值模拟结果表明:随着周界风/油风比率的减小,拱上煤粉气流下冲深度增大,炉内火焰充满程度变好;煤粉气流着火距离变短,燃尽率提高,飞灰含碳量降低,炉膛出口NOx浓度降低。优化的技术方案实施后,第三方试验结果表明各负荷下锅炉NOx排放质量浓度均在700 mg/m3以内,飞灰可燃物含量均在4%以内,高负荷下减温水量虽高于保证值,但较改造前大幅度下降。 相似文献
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在600 MW对冲旋流燃烧锅炉上进行了侧墙缝隙式贴壁风系统改造后的工业试验,对比分析了缝隙式贴壁风的效果,评估了其对锅炉运行和NOx排放的影响,并对贴避风运行方式进行了优化。研究结果表明:侧墙缝隙式贴壁风系统可以改善对冲旋流燃烧锅炉两侧墙贴壁烟气还原性气氛,提高贴壁烟气中O2体积分数,降低H2S体积分数;由于贴壁风风率较低,投运侧墙缝隙式贴壁风对锅炉氮氧化物排放、主蒸汽温度、减温水量及飞灰大渣可燃物含量无明显的影响;贴壁风的效果受机组负荷、运行氧量、煤质含硫量等影响,不同运行工况下应设置合理的贴壁风风门开度,以保证获得最佳的效果。 相似文献
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对一台660 MW旋流对冲锅炉在不同层燃烧器组合运行工况下进行了炉内流动、燃烧和NOx排放特性的数值模拟,模拟结果与试验值相对误差小于10%。模拟结果表明:额定负荷时,5层燃烧器运行,停前墙和停后墙同层燃烧器时NOx排放和飞灰含碳量基本相同;停上层燃烧器相比于停中层燃烧器,空气分级效果强化,煤粉颗停留时间增加,NOx和飞灰含碳量分别降低9.5%和9.8%,在锅炉实际运行过程中,停上层燃烧器更有利于降低NOx排放和提高燃烧效率。 相似文献
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C.C. Chen Y.L. Tsai C.W. Lan 《International Journal of Heat and Mass Transfer》2009,52(5-6):1158-1166
Two- and three-dimensional (3D) adaptive phase field simulations of dendritic crystal growth in a forced flow are presented. The simulations are based on an adaptive finite volume mesh for a better resolution on the dendrite morphology. It also allows the simulation in a large domain without much additional computing cost, so that the boundary effect can be neglected for the comparison with classic solutions. With the efficient simulations, the effect of forced convection on the growth behavior at high undercooling is discussed, and the results agree well with Oseen–Ivantsov solution and the reported results. For the case of low undercooling, the simulated tip radius and speed are also consistent with the experimental ones. As compared with 2D morphologies, side branches are easily induced in 3D dendrites, and the dramatic difference can be explained through the simulated flow structures and temperature fields. The effect of the flow on the side branching for different undercoolings is also illustrated. 相似文献
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A telescopic local grid refinement technique is developed in order to enhance the accuracy level of wind field predictions in a subregion of a complex topography. A 3D simulation of the wind flow field over complex terrains has been carried out. The governing Navier–Stokes conservation equations of the flow field are solved numerically in a three‐dimensional generalized curvilinear non‐orthogonal grid, using Cartesian velocity components, following the finite volume approximation and a pressure correction method. Turbulence is simulated by a two‐equation transport model. The reliability of the general flow solver is first tested by simulating the flow past a cube. The second test case simulated is the flow over the Askervein hill, with a detailed comparison of predicted and measured velocities. The third case presented concerns flow field simulation over a complete island. Comparison with measurements reveals the significance of the accurate discretization of the topography and the use of telescopic meshes on the results. Copyright © 2001 John Wiley & Sons, Ltd. 相似文献
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基于CFX的混流泵内流场数值模拟 总被引:2,自引:0,他引:2
基于三维不可压缩流体的N-S方程和RNGκ-ε湍流模型,采用流体计算软件ANSYS-CFX计算了额定转速下190~300L/s流量范围内9个工况点的某混流泵内部流动,研究了小流量工况、最优工况和大流量工况等工况下叶片压力面、吸力面的静压分布及各断面翼型附近的相对流速分布;通过分析混流泵内部流动速度和叶片表面静压分布,揭示了其内部流动的主要特征。预测了泵的水力性能,并与泵模型性能试验结果进行了对比。结果表明,最优工况时数值模拟与试验结果吻合较理想,满足工程实际的需要。 相似文献
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为了研究下击暴流作用下塔式太阳能定日镜表面的风压分布特征,文章采用计算流体动力学方法对下击暴流作用下,不同径向位置和不同工作俯仰角的定日镜表面风压进行了数值模拟,并将模拟结果与大气边界层近地风作用下定日镜表面的风压特性进行了比较分析。分析结果表明:当定日镜正常工作时,下击暴流作用下,迎风面风压呈现出中间高两边低的分布趋势,风压峰值位于定日镜中部,背风面风压中间低两边高;随着俯仰角逐渐增大,下击暴流作用下,定日镜迎风面压力峰值中心从定日镜下边缘逐渐上移,最大压力值和高压区范围也逐渐增大,背风面负压值逐渐减小且谷值中心逐渐下移;与常规风相比,下击暴流作用下,定日镜表面风压受径向距离影响明显,当镜面垂直于地面时,定日镜迎风面和背风面表面风压随着定日镜与下击暴流风暴中心之间径向距离的增大而减小;在定日镜抗雷暴下击暴流强风的设计过程中,须要考虑下击暴流和常规风的速度场、气压场的不同,及其所导致的定日镜表面风压分布特征的变化。 相似文献
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以VD炉底吹氩精炼过程中钢包钢液流场为研究对象,建立了其CAE仿真模型;并将该模型用于某钢厂230 tVD炉钢液流场的研究分析中,其计算结果与生产现场情况基本吻合,从而进一步证明了该CAE仿真模型的正确性;也为VD炉的研制和改进提供了可靠的理论依据. 相似文献
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《International Journal of Hydrogen Energy》2019,44(21):10207-10217
The potential of the silica membrane reactors for use in the decomposition of hydrogen iodide (HI) was investigated by simulation with the aim of producing CO2-free hydrogen via the thermochemical water-splitting iodine-sulfur process. Simulation model validation was done using the data derived from an experimental membrane reactor. The simulated results showed good agreement with the experimental findings. The important process parameters determining the performance of the membrane reactor used for HI decomposition, namely, reaction temperature, total pressures on both the feed side and the permeate side, and HI feed flow rate were investigated theoritically by means of a simulation. It was found that the conversion of HI decomposition can be improved by up to four times (80%) or greater than the equilibrium conversion (20%) at 400 °C by employing a membrane reactor equipped with a tubular silica membrane. The features to design the membrane reactor module for HI decomposition of the thermochemical iodine-sulfur process were discussed under a wide range of operation conditions by evaluating the relationship between HI conversion and number of membrane tubes. 相似文献
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无节流器轴流旋风气液分离器性能研究 总被引:1,自引:0,他引:1
采用数值模拟方法对无节流器轴流旋风气液分离器的内部流场状态进行了预测,得到不同壁面开槽尺寸无节流器轴流旋风分离器内部的流场特性,通过试验研究获取了分离器的阻力特性与效率特性,并对数值模拟结果进行了验证.结果表明:数值计算获得的阻力特性曲线与试验得到的阻力特性曲线基本重合,数值计算方法在获取旋风气液分离器阻力特性方面具有较高的精度;开槽尺寸对无节流器轴流旋风气液分离器的阻力特性影响不大,但对分离器的分离效率影响较大;在入口气流平均速度为3 m/s和4 m/s的条件下,当外壁开槽尺寸为30 mm时,分离器的平均分离效率最高,均在97.3%以上. 相似文献