共查询到20条相似文献,搜索用时 269 毫秒
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基于建立的舰船大功率多级轴流压气机气动设计体系,开展了舰船用某型大功率燃气轮机压气机设计研究,完成了6级轴流压气机的气动设计。进行了一维反问题设计、一维特性计算分析、S2反问题计算、叶片造型以及三维CFD计算分析。各级载荷分布从前面级到后面级逐渐降低,叶展方向按照等压比分配以避免径向掺混损失过大,S2设计并没有严格遵循传统的设计规律(等环量、等反动度等),而是基于一维设计方案通过不断调整优化获得的。根据CDA的特点,开发了可用于工程应用的叶片造型程序,可实现不同中弧线、不同厚度分布调节,能够实现叶片弯、掠等功能。三维数值模拟结果表明,考虑动叶叶顶具有0. 5 mm间隙的情况下,6级压气机设计点效率达到89. 75%,设计转速下的喘振裕度为22. 5%,同时具有较好的变工况性能。 相似文献
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为缩短燃气轮机低压压气机的设计周期,获取一维设计中各关键设计参数分布规律,同时得到最优的一维设计参数选取方案,采用基于HARIKA算法的压气机一维设计与分析程序对某型船用低压压气机流量系数、载荷系数和反动度的轴向布局方法进行了研究并提炼了各参数分布的数学模型。其中,流量系数和载荷系数沿级分布为近似单峰值的三次多项式曲线,反动度分布为"二段式",通过改变流量系数和载荷系数的峰值点坐标和改变特定级反动度和反动度变化步长的方法,研究了不同布局方式对效率、喘振裕度以及压比的影响,最后结合优化算法得到了最优参数分布方案。结果发现:流量系数峰值位置在第6级,载荷系数在第5级或第6级时效率和喘振裕度性能较好;第四级反动度取值0.5~0.52时效率较高;相比载荷系数和反动度,流量系数对非设计工况性能影响更为显著,优化后的参数分布方案在各转速下喘振裕度均有所提高。 相似文献
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介绍了ZYQJC-1型内燃机车功率、增压器性能随车检测仪的设计和研制。检测数据包括主发电机整流后电流、电压,增压器进排气温度,压气机进出口空气温度,增压器转速等。检测数据可存储在数据盒中,通过地面分析软件对记录数据进行分析。 相似文献
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使用NUMECA软件的FINE/Design3D模块对某型跨音速涡轮叶栅改型前后的导叶进行了单列三维流场计算,并分析了原型与改型叶栅沿叶片型面压力的分布以及叶片吸力面上的静压等值线分布。结果表明,叶片的改型改变了叶片表面的压力场,改善了叶栅内气体的流动。 相似文献
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汽轮机回热抽汽对下游流场影响的数值研究 总被引:1,自引:1,他引:0
针对某型机组高压缸的抽汽结构及抽汽点后叶片流场,采用N-S方程进行全周全三维叶片通道的数值模拟,研究结果表明,抽汽对其下游静叶栅气动参数沿周向和径向的分布均有较大的影响,并且该影响随着向抽汽点的趋近而增大,但抽汽对叶片型面静压分布影响较小,不会影响叶片的加载形式。 相似文献
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This paper deals mainly with pneumatic measurements on a radial turbine nozzle cascade. The fill radial cascade guarantees the exit flow field periodicity downstream of it. A special traversing mechanism with a five - hole conical probe moving along a circular path behind the cascade was used for flow field investigation in this type of cascade with very low aspect ratio. The analyses of results of 2D and 3D pneumatic measurements including loss coefficient values are presented. 相似文献
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通过数值求解基于雷诺时均的三维定常粘性N-S方程,结合RNGk-ε湍流模型和非平衡壁面函数,对一种超微型向心涡轮动叶栅内的流动情况进行了数值模拟。揭示了具有极低展弦比动叶栅叶顶间隙对流场参数分布和气动损失的影响,为超微涡轮的设计和改进提供了理论依据。模拟结果表明,叶顶间隙的大小对通道内马赫数分布有重要影响,其中顶部间隙射流所引发的泄漏涡与主流的掺混是主流马赫数降低的重要原因;叶顶间隙的存在使得总压损失系数均匀化,即近壁区和主流区的总压损失都较高;动叶栅在叶展方向上的载荷分布均匀,弦向载荷主要由接近尾缘的弧段承担;模拟中还解析出三维的尾迹涡,这主要是动叶栅尾缘过厚所导致,应进行叶型改进。 相似文献
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《Journal of power sources》2006,156(2):267-280
The water flooding and two-phase flow of reactants and products in cathode flow channels (0.8 mm in width, 1.0 mm in depth) were studied by means of transparent proton exchange membrane fuel cells. Three transparent proton exchange membrane fuel cells with different flow fields including parallel flow field, interdigitated flow field and cascade flow field were used. The effects of flow field, cell temperature, cathode gas flow rate and operation time on water build-up and cell performance were studied, respectively. Experimental results indicate that the liquid water columns accumulating in the cathode flow channels can reduce the effective electrochemical reaction area; it makes mass transfer limitation resulting in the cell performance loss. The water in flow channels at high temperature is much less than that at low temperature. When the water flooding appears, increasing cathode flow rate can remove excess water and lead to good cell performance. The water and gas transfer can be enhanced and the water removal is easier in the interdigitated channels and cascade channels than in the parallel channels. The cell performances of the fuel cells that installed interdigitated flow field or cascade flow field are better than that installed with parallel flow field. The images of liquid water in the cathode channels at different operating time were recorded. The evolution of liquid water removing out of channels was also recorded by high-speed video. 相似文献
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The flow distribution obtained with three different bipolar plate geometries has been studied, analyzing their fluid dynamic performance. Three plate topologies have been selected in some way representative of different design models commonly used. The configurations tested are a set of parallel diagonal channels, a branching cascade type, and a serpentine distribution of parallel channel blocks. The flow distribution across the plates has been first simulated numerically. To visualize the flow pattern at the plate channels plane, a laser-induced fluorescence (LIF) trace tracking technique has been applied. From experimental and numerical simulations it is concluded that the diagonal topology distributes the flow in a non-uniform way. On the other hand, an inadequately large pressure drop is established along the serpentine-parallel plate. In the cascade case, both velocity and pressure fields are very uniform, and it can be expected to produce a very homogeneous distribution of reactants over the catalyst layer. 相似文献
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