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991.
With the development of both optical fiber-based communication and sensation, one interesting topic has been pointed out. How to connect those mountains of sensors to detect the signal in a large area, and how to make the cost of sensing system lower enough should be studied. A network of sensors is a good option. All sensing equipments, including the interrogators and the sensors, will be internetworking together. However, fiber optic communication networks have been developed very well over the past two decades. Is it necessary to rebuild a new network for sensors? In this paper, some new technologies in the two areas of fiber optic sensors and fiber optic communication will be addressed. Then, the available overlay architecture of a fiber optic sensors network will be presented. Finally, a polymorphous optical burst switching (POBS)-based architecture will be proposed, which can support all kinds of services, including digital data optical circuit/burst/packet switching and analog fiber optic sensor signal circuit/burst switching, etc. 相似文献
992.
为了研究不同天顶角、传输距离、光源相干性以及湍流外尺度对接收面光束空间相干度的影响,采用广义惠更斯-菲涅耳原理和相位结构函数的平方近似,并运用张量积分的方法,得到了部分相干平顶光束通过斜程湍流大气传输后接收面光束空间相干度的解析表达式。结果表明,传输距离较短时,该光束空间相干度随两点距离的增加出现振荡现象,而传输距离较长时振荡现象消失;当传输距离给定时,天顶角越大,光束空间相干度的有效宽度相对较短。初始相干长度较短的该类光束其空间相干度的宽度不随传输距离的增加而减小;长距离传输后,光束空间相干性与光束初始相干长度不再有关。 相似文献
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996.
基于大涡模拟的发动机缸内湍流流动及拟序结构 总被引:2,自引:0,他引:2
应用大涡模拟方法对发动机缸内湍流流场进行了三维瞬态数值分析.主要从湍流脉动、湍动能和缸内拟序结构演变等方面考察了发动机缸内流场特性.计算结果表明:相比雷诺平均模型,大涡模拟方法可以更真实地反映发动机循环过程中缸内气体流动的细节和规律.利用大涡模拟结合Q准则判别法可以较好地识别缸内大尺度湍流拟序结构;拟序结构对于缸内大尺度动能的产生及湍流的维持具有关键的作用.RANS类模型则不具备充分捕获大尺度拟序结构的能力.湍流脉动与活塞平均运行速度接近于成正比. 相似文献
997.
参考现有某重型燃气轮机环型燃烧室,运用FLUENT软件对其喷嘴结构及燃烧室部分进行三维数据模拟及分析,通过数值模拟分析燃烧过程速度、压力、温度等变量的分布规律,以及对燃烧室不同截面的流场分布规律的分析,特别是对主要区域各关键截面的流场分析,从而判断出燃烧室设计的合理性,为进一步优化燃烧室的结构设计、改善流场结构奠定基础. 相似文献
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根据岩爆发生判别准则的4个指标,在利用收集到的岩爆资料数据的基础上,采用SVM方法对岩爆的等级进行了预测分析.通过对冬瓜山矿的应用分析,表明该岩爆分级方法是可行的. 相似文献
999.
Kent E. Wardle Todd R. Allen Mark H. Anderson Ross E. Swaney 《American Institute of Chemical Engineers》2009,55(9):2244-2259
The annular centrifugal contactor is a compact mixer/centrifuge developed for solvent extraction processes for recycling used nuclear fuel. This research effort couples computational fluid dynamics (CFD) modeling with a variety of experimental observations to provide a valid detailed analysis of the flow within the centrifugal contactor. CFD modeling of the free surface flow in the annular mixing zone using the volume-of-fluid method combined with large eddy simulation of turbulence was found to have very good agreement with the experimental measurements. A detailed comparative analysis of the flow and mixing with different housing vane geometries (four straight vanes, eight straight vanes, and curved vanes) was performed. Two additional variations on the eight straight vane geometry were also simulated. This analysis determined that at the simulated moderate flow rate the four straight mixing vane geometry has greater mixing and fluid residence time as compared to the other mixing vane configurations. © 2009 American Institute of Chemical Engineers AIChE J, 2009 相似文献
1000.
Transient flow behaviors in a novel circulating‐turbulent fluidized bed (C‐TFB) were investigated by a multifunctional optical fiber probe, that is capable of simultaneously measuring instantaneous local solids‐volume concentration, velocity and flux in gas‐solid two‐phase suspensions. Microflow behavior distinctions between the gas‐solid suspensions in a turbulent fluidized bed (TFB), conventional circulating fluidized bed (CFB), the bottom region of high‐density circulating fluidized bed (HDCFB), and the newly designed C‐TFB were also intensively studied. The experimental results show that particle‐particle interactions (collisions) dominate the motion of particles in the C‐TFB and TFB, totally different from the interaction mechanism between the gas and solid phases in the conventional CFB and the HDCFB, where the movements of particles are mainly controlled by the gas‐particle interactions (drag forces). In addition, turbulence intensity and frequency in the C‐TFB are significantly greater than those in the TFB at the same superficial gas velocity. As a result, the circulating‐turbulent fluidization is identified as a new flow regime, independent of turbulent fluidization, fast fluidization and dense suspension upflow. The gas‐solid flow in the C‐TFB has its inherent hydrodynamic characteristics, different from those in TFB, CFB and HDCFB reactors. © 2009 American Institute of Chemical Engineers AIChE J, 2009 相似文献