共查询到19条相似文献,搜索用时 62 毫秒
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旋风分离器减阻杆对流场的影响 总被引:1,自引:0,他引:1
在研究发现旋风分离器减阻杆的基础上,研究了减阻杆对流场的影响,发现了减阻杆使切向速度分布趋于平缓,轴向速度上升峰值内移,径向上压力梯度减小,轴处中心区从逆压梯度变为顺压梯度等重要规律,从而为分析旋风分离器减振阻杆的减阻机理提供了依据。同时本文还首次发现旋风分离器入口附近有近24%的短路流量,提出设法减小这部位短流流量是提高分离效率的一个研究方向。 相似文献
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利用计算流体动力学软件FLUENT对旋风分离器内气固两相流动特性进行三维数值模拟,模拟气相流场采用雷诺应力模型,应用随机轨道模型模拟湍流流场中颗粒的运动轨迹,同时给出了不同抽气率下旋风分离器的速度、压力分布,计算出旋风器分级效率,模拟结果与文献实验数据吻合较好.结果表明,灰斗抽气可以提高锥体内旋转气流切向速度,轴向速度减少能够降低气流携带颗粒返混能力,并减小排气芯管下口短路流,提高旋风分离器分离效率.对于给定的旋风分离器,抽气率应有一最优值. 相似文献
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在研究发现旋风分离器减阻杆的基础上,研究了减阻杆对流场的影响,发现了减阻杆使切向速度分布趋于平缓、轴向速度上升峰值内移、径向上压力梯度减小、轴向上中心区从逆压梯度变为顺压梯度等重要规律,从而为分析旋风分离器减阻杆的减阻机理提供了依据。同时本文还首次发现旋风分离器入口附近有近24%的短路流量,提出设法减小这部分短路流量是提高分离效率的一个研究方向。 相似文献
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Influence of inlet angle on flow pattern and performance of gas-liquid cylindrical cyclone separator
Le Van Sy 《Particulate Science and Technology》2017,35(5):555-564
Gas-liquid cylindrical cyclone (GLCC) separator is widely used in the petroleum industry with potential field applications. Its performance is strongly influenced by the inlet configuration. The 27° optimal inclined inlet angle has been experimentally observed for GLCC with the same diameter of body and inlet. For other GLCCs, the effect of inlet angle on flow pattern and their performances have not been investigated. The main target of the current study is to deeply understand the changes of flow pattern with respect to different inclined angles and flow conditions. Twelve GLCCs with different inclined angles were numerically investigated by using the Reynold stress turbulence model to predict the flow pattern with GLCC. The distribution of radial, axial, and tangential velocity profiles and their maximum magnitudes with respect to the change of inlet angle were carefully considered in this study. 相似文献
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Shuyan Wang Haolong Li Ruichen Wang Xu Wang Ruichao Tian Qiji Sun 《Advanced Powder Technology》2019,30(2):227-239
Hydrodynamic characteristics in a cyclone separator are simulated by means of DEM-CFD. Reynolds stress turbulence model (RSM) is used to capture gas turbulence. By changing the inlet angle, the distributions of pressure drop, tangential and axial velocity of gas phase are obtained within the cyclone. Simulated results indicate that the flow pattern consists of two regions: loss-free vortex region and forced vortex region. The negative inlet angle brings about a larger pressure drop comparing to positive inlet angle. The separation efficiency and trajectory of particles from simulation are obtained. The effects of inlet angle and particle size on separation efficiency are quantified. The separation efficiency is increased with an increase of particle size, while the separation efficiency firstly increases and then declined as inlet angle changes from negative to positive. An agreement between the numerical simulation and experimental results has been achieved in a cyclone separator. 相似文献
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Jianping Zhang Zhenting Zha Peng Che Honglei Ding Weiguo Pan 《Particulate Science and Technology》2019,37(6):665-672
Aiming at improving collection efficiency in the cyclone separator, the effects of inlet height and velocity on tangential velocity, static pressure and collection efficiency were studied. A three-dimensional model including gas-flow, and particle-dynamics fields was built by the Reynolds stress turbulence model, and the numerical simulation was achieved using the FLUENT software. The static pressure distribution, tangential velocity distribution, and particle trajectory of the cyclone were obtained, and the variation law of the collection efficiency with inlet height and velocity as well as particle diameter was analyzed. Numerical results indicate that both the static pressure and the tangential velocity in the cyclone basically present the axial symmetrical distribution, the static pressure shows a nonlinear increasing trend in the radius direction and the distribution of the tangential velocity is in the shape of a “hump.” The increase of inlet height in a certain range reduces the rotation numbers of particles in the cyclone and shortens the residence time, which results in the improvement of trapping performance. Furthermore, the appropriately increasing inlet velocity in a reasonable range can make the collection efficiency increased. 相似文献
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V. N. Dolgov A. P. Baskalov Yu. M. Goldobin 《Journal of Engineering Physics and Thermophysics》1981,41(4):1133-1136
Results are presented from an experimental study of heat exchange in a TsN-II cyclone processing combustion products at temperatures up to 400°C.Translated from Inzhenerno-Fizicheskii Zhurnal, Vol. 41, No. 4, pp. 690–694, October, 1981. 相似文献
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《Advanced Powder Technology》2022,33(11):103791
The effect of the operation temperature on the cyclone hydrodynamics and performances is numerically investigated by Computational Fluid Dynamics (CFD). When increasing the temperature, the separation efficiency decreases and the separation quality improves due to the weakened double layer swirling flow structure. The radial drag and centrifugal forces exerted on 0.1 μm and 1 μm particles are recorded. A large radial drag force to centrifugal force ratio is required for escape: a ratio larger than 104. When the radial drag force to centrifugal force ratio is in the range of 101 to 103, it is the temperature-dependent flow field which determines the submicron particle separation. While the locus of gas zero vertical velocity is closely related to the particle’s separation, the gas turbulence intensity distribution also contributes the capture of the particles. 相似文献
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《Advanced Powder Technology》2021,32(12):4779-4787
In this study, a cyclone separator that can be used as a sampling inlet for portable black carbon (BC) monitors operating at a flow rate of less than 200 mL/min was developed. A prototype was fabricated to evaluate its performance by experiments, and the cut-off size of the cyclone separator was predicted through numerical analysis by applying various turbulence models. The RNG k–ε model was found to be suitable for the analysis of the cyclone separator operating at Reynolds numbers of less than 1000. Cyclone separators were designed through simulation and fabricated for each operating flow rate (50, 100, 150, and 200 mL/min) of a BC monitor, and their performances were experimentally verified. Meanwhile, when the non-dimensional analysis method of the previous study conducted at Reynolds numbers of 1000 or higher was used, the cyclone separator operating at Reynolds numbers of less than 1000 also exhibited a similar linear tendency. 相似文献
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《Advanced Powder Technology》2023,34(1):103929
This study aimed to investigate the separation performance of a cyclone separator after reshaping its cylindrical body by installing the helical triangular fins. A numerical simulation based on Fluent was adopted to perform an orthogonal test to optimise the structure of the cyclone separator with helical triangular fins. Three structural parameters of the helical triangular fins were selected as optimisation variables: base width, fin size, and fin pitch, and their influences on the evaluation indices of the cut-off diameter were investigated. The optimal combination scheme was determined by range analysis, and the cyclone separator performances before and after optimisation were compared and analysed. The significant influence of the structural parameters on the cut-off diameter was in descending order as the fin pitch, fin size, and base width. For particles with diameter of 0.1, 0.5, 1, 2, and 3 μm, the separation efficiency of the cyclone separator with optimized helical triangular fins increased by 7.4 %, 15.9 %, 20.1 %, 10.9 % and 14.8 % respectively. Moreover, the cut-off diameter of the finned cyclone separator is reduced by 30.7 %, while the pressure drop is only increased by 6.6 %. The short circuit flow and back-mixing were alleviated, thereby considerably enhancing the stability of the flow field. Therefore, the finned cyclone separator was found to play a critical role in increasing the separation of fine particulate matter. 相似文献