5 An alternative method for mapping solids holdup in CFB riser
5.4 Conclusions 98
In this work, solids holdup of FCC particles with a Sauter mean diameter of 67 µm and a particle density of 1877 kg/m3 are measured by an alternative image calibration method
and the optical fiber probe respectively. Both methods are taken in the riser of a rectangular CFB with a cross section of 0.019×0.114 m2 and at two axial positions (5.33
and 3.60 m) under different operating conditions with Ug and Gs in the range of 3.0-12.0
m/s and 50-150 kg/m2s, respectively.
Using the image calibration method, the obtained radial distribution profiles of the solids holdup exhibit similar trends with that of previous research, which reflects the feasibility of the newly developed method. The direct comparing of solids holdup data obtained between the image calibration method and the optical fiber probe under identical operating conditions shows excellent agreement, which clearly verifies the accuracy of the image calibration method.
Further comparing between the image calibration method results from the current study and the measurement results of the optical fiber probe from other researchers also shows an excellent agreement under the same operating condition. These comparisons verify that the image calibration methods is a good alternative method in measuring the solids holdup in the rectangular riser.
Acknowledgements
The authors acknowledge with gratitude the financial support of the National Science and Engineering Research Council of Canada (NSERC) and the China Scholarship Council (CSC).
References
Arena, U., Cammarota, A., Marzocchella, A., Massimilla, L., 1989. Solids flow structures in a two-dimensional riser of a circulating fluidized bed. Journal of Chemical Engineering Japan 22 (3), 236-241.
Casleton, D. K., Shadle, L. J., Ross, A. A., 2010. Measuring the voidage of a CFB through image analysis. Powder Technology 203, 12-22.
Cocco, R., Shaffer, F., Hays, R., Karri, S. B. R., Knowlton, T., 2010. Particle clusters in and above fluidized beds. Powder Technology 203, 3-11.
Hartge, E. –U., Rensner, D., Werther, J., 1988. Solids concentration and velocity patterns in circulating fluidized beds. In: Basu, P., Large, J. F., (Eds.), Circulating Fluidized Bed Technology II, Pergamon Press, Oxoford, pp. 165-180.
Herbert, P. M., Gauthier, T. A., Briens, C. L., Bergougnou, M. A., 1994. Application of fiber optic reflection probes to the measurement of local particle velocity and concentration in gas-solid flow. Powder Technology 80, 243-252.
Issangya, A. S., Bai, D., Bi, H. T., Lim, K. S., Zhu, J., Grace, J. R., 1999. Suspension densities in a high-density circulating fluidized bed riser. Chemical Engineering Science 54, 5451-5460.
Kato, K., Takarada, T., Tamura, T., Nishino, K., 1990. Particle holdup distribution in a circulating fluidized bed. In: Basu, P., Horio, M., Hasatani, M., (Eds.), Circulating Fluidized Bed Technology III, Pergamon Press, Oxoford, pp. 145-150.
Lackermeier, U., Rudnick, C., Werther, J., Bredebusch, A., Burkhart, H., 2001. Visualisation of flow structures inside a circulating fluidized bed by means of laser sheet and image processing. Powder Technology 114, 71– 83.
Liu, J., Grace, J. R., Bi, X., 2003a. Novel multifunctional optical-fiber probe I. AIChE Journal 49, 1405-1420.
Liu, J., Grace, J. R., Bi, X., 2003b. Novel multifunctional optical-fiber probe II. AIChE Journal 49, 1421-1432.
McMillan, J., Shaffer, F., Gopalan, B., Chew, J. W., Hrenya, C., Hays, R., Karri, S. B. R., Cocco, R., 2013. Particle cluster dynamics during fluidization. Chemical Engineering Science 100, 39-51.
Oki, K., Akehata, T., Shirai, T., 1975. A new method for evaluating the size of moving particles with a fiber optic probe. Powder Technology 11, 51-57.
Oki, K., Walawender, W. P., Fan, L. T., 1977. The measurement of local velocity of solid particles. Powder Technology 18, 171-178.
Pallares, D., Johnsson, F., 2006. A novel technique for particle tracking in cold 2- dimensional fluidized beds-simulating fuel dispersion. Chemical Engineering Science 61, 2710-2720.
Park, A. –H., Bi, H., Grace, J. R., 2002. Reduction of electrostatic charges in gas-solid fluidized beds. Chemical Engineering Science 57, 153-162.
Parssinen, J. H., Zhu, J. X., 2001a. Axial and radial solids distribution in a long and high- flux CFB riser. AIChE Journal 47 (10), 2197-2205.
Parssinen, J. H., Zhu, J., 2001b. Particle velocity and flow development in a long and high-flux circulating fluidized bed riser. Chemical Engineering Science 56, 5259-5303.
Patrose, B., Caram, H. S., 1982. Optical fiber probe transit anemometer for particle velocity measurements in fluidized beds. AIChE Journal. 28, 604-609.
Qin, S., Liu, D., 1982. Application of optical fibers to measurement and display of fluidized systems. In: Kwauk, M., Kunii, D., (Eds.), Fluidization’82: Science and Technology, Science Press, Beijing, pp. 258-266.
Shaffer, F., Gopalan, B., Breault, R. W., Cocco, R., Karri, S. B. R., Hays, R., Knowlton, T., 2013. High speed imaging of particle flow fields in CFB risers. Powder Technology 242, 86-99.
Werther, J., Hage, B., Rudnick, C., 1996. A comparison of laser Doppler and single-fibre reflection probes for the measurement of the velocity of solids in a gas-solid circulating fluidized bed. Chemical Engineering and Processing 35, 381-391.
Xu, J., Zhu, J. X., 2010a. Experimental study on solids concentration distribution in a two-dimensional circulating fluidized bed. Chemical Engineering Science 65, 5447-5454.
Xu, J., 2010b. Hydrodynamics studies on macro- and micro-flow structure with effects of particle properties in a circulating fluidized bed. In: Chemical and Biochemical Engineering. The University of Western Ontario, London.
Xu, J., Zhu, J. X., 2011. Visualization of particle aggregation and effects of particle properties on cluster characteristics in a CFB riser. Chemical Engineering Journal 168, 376-389.
Xu, J., Zhu, J. X., 2012. A new method for the determination of cluster velocity and size in a circulating fluidized bed. Industrial & Engineering Chemistry Research 51, 2143- 2151.
Yan, A., Zhu, J. X., 2004. Scale-up effect of riser reactors (1): Axial and radial solids concentration distribution and flow development. Industrial & Engineering Chemistry Research 43, 5810-5819.
Yan, A., Ball, J., Zhu, J. X., 2005. Scale-up effect of riser reactors (3) axial and radial solids flux distribution and flow development. Chemical Engineering Journal 109, 97- 106.
Yan, A., Huang, W., Zhu, J. X., 2008. The influence of distributor structure on the solids distribution and flow development in circulating fluidized beds. The Canadian Journal of Chemical Engineering 86, 1023-1031.
Yang, J. S., Zhu, J. X., 2013. A novel method based on image processing to visualize clusters in a rectangular circulating fluidized bed riser. Powder Technology (Accepted). POWTEC-D-13-01489.
Zhang, H., Johnston, P. M., Zhu, J. –X., de Lasa, H. I., Bergougnou, M. A., 1998. A novel calibration procedure for a fiber optic solids concentration probe. Powder Technology 100, 260-272.