Method of optical fiber measurement for local particle flux and velocity in riser

被引:0
|
作者
Wang F. [1 ]
E C. [1 ]
Zhao A. [1 ]
Lu C. [1 ]
机构
[1] State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing
来源
E, Chenglin (ecl510@126.com) | 1600年 / Materials China卷 / 67期
关键词
Optical fiber probe; Particle flux; Particle velocity; Riser; Volumetric method;
D O I
10.11949/j.issn.0438-1157.20160393
中图分类号
学科分类号
摘要
A new method was proposed in a cold riser experimental apparatus with height of about 18 m and inner diameter of 100 mm according to the result measured by PV-6D optical fiber to calculate the local particle flux and velocity based on all the sampling time. The new method was compared with the method used in the referring paper. The results showed that the values of local particle flux and velocity calculated by the two methods had a great discrepancy. The maximum, minimum and mean relative errors between the cross-sectional mean particle flux and the measured value calculated by this paper and the referring paper were 606.9%, 241.3%; 221.4%, 89.5% and 388.9%, 145.6%, respectively. Thus, the value of particle flux measured by this paper was relatively low. The cross-sectional mean particle velocity calculated by the referring paper was higher than the operating gas velocity, and the gas-solid slip velocity and slip coefficient respectively varied from -1.6 to -4.7 m·s-1 and 0.56 to 0.90, respectively, and thus there was a great difference to the actual gas-solid flow in riser. The cross-sectional mean particle velocity calculated by this paper was lower than the operating gas velocity. The gas-solid slip velocity and slip coefficient varied from 0.6 to 9.6 m·s-1 and 1.11 to 2.14, respectively. There were some problems when using the reflecting optical fiber to measure the particle concentration and it was the main reason that resulted in the higher particle flux, slip velocity and slip coefficient measured by this paper. Furthermore, two fitting functions were come up with to calculate the particle circulation in the riser according to the measuring result by the optical fiber, substituting for the recent volumetric method. © All Right Reserved.
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页码:3209 / 3223
页数:14
相关论文
共 34 条
  • [1] Lu C.X., Wang Z.A., Fluidized Catalytic Cracking Process, (2002)
  • [2] Jin Y., Zhu J.X., Wang Z.W., Et al., Fluidization Engineering Principles, (2001)
  • [3] Wu C., Gao Y.X., Gao X., Et al., Particle velocity measurements in transition section of turbulent fluidized beds using optical fiber probe and CFD simulation, Journal of Chemical Engineering of Chinese Universities, 29, 1, pp. 11-18, (2015)
  • [4] Basu P., Large J.F., Circulating Fluidized Bed Technology II, pp. 155-164, (1988)
  • [5] Wei F., Lu F.B., Jin Y., Et al., Mass flux profiles and flow regimes in a high density circulating fluidized bed, Journal of Chemical Industry and Engineering (China), 47, 3, pp. 346-351, (1996)
  • [6] Zhu H.Y., Zhu J., Li G.Z., Et al., Detailed measurements of flow structure inside a dense gas-solids fluidized bed, Powder Technol., 180, 3, pp. 339-349, (2008)
  • [7] Zhu J.X., Li G.Z., Qin S.Z., Et al., Direct measurements of particle velocities in gas-solids suspension flow using a novel five-fiber optical probe, Powder Technol., 115, 2, pp. 184-192, (2001)
  • [8] Kwauk M., Li H.Z., Manual of Fluidization, pp. 862-871, (2008)
  • [9] Andreux R., Gauthier T., Chaouki J., Et al., New description of fluidization regimes, AIChE J., 51, 4, pp. 1125-1130, (2005)
  • [10] Wu C., Gao X., Cheng Y.W., Et al., Experimental and numerical study of solids concentration distribution intransition section of turbulent fluidized bed, CIESC Journal, 64, 3, pp. 858-866, (2013)