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Numerical investigations of the four-path separator

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Wybrane pełne teksty z tego czasopisma
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Języki publikacji
EN
Abstrakty
EN
In the pneumatic conveying systems of large power boilers, the required separation of the dust-air mixture to particular burners has to be obtained. This problem is very important in consideration of limitation of losses connected with incomplete combustion, life of many elements of the furnace system and NOx emission. The realized design works on dust pipes are usually based on the assumption that dust concentration in the section is approximately the same and there is no segregation of dust particles. However, in many cases in the pneumatic conveying systems for coal dust, diversified concentration and out-of-control segregation of particles take place. Such segregation leads to diversification of propagation, disturbance in the combustion process and accelerated erosion of the installation elements. This paper presents numerical investigations on the air-coal dust mixture flow through the four-path separator system. Diversification of concentration and particle segregation behind the separator are determined by the elbow presence just before the inlet to the separator. The elbow presence causes diversification of concentration on the mixture silt to the four-path separator located directly over the elbow. It is a reason of the diversified silt of the dust on the boiler corners and the accelerated erosion of separators. The author tried to assess influence of configuration of the pipe delivering the medium to the separator on uniformity of dust separation behind the separator. Numerical investigations were performed for six positions of the inlet interval before the separator at different velocities and dimensions of the dust particles. In order to realize calculations for three-dimensional geometry, the Euler model was selected for description of the gaseous phase motion, and the Lagrange model was used for description of the particle motion. From analysis of the performed calculations it appears that the inlet configuration in relation to the separator strongly influences the proper dust separation to outlets. The best dust separation can be observed for the inlet location angle in the range 60÷90°.
Rocznik
Strony
201--225
Opis fizyczny
Bibliogr. 18 poz., tab., rys.
Twórcy
autor
  • Opole University of Technology, Department of Thermal Engineering and Industrial Facilities, Mikołajczyka 5, 45-271 Opole, j.wydrych@po.opole.pl
Bibliografia
  • [1] BORSUK G., DOBROWOLSKI B. and WYDRYCH J., Gas - solids mixture flow through a two - bend system, Chemical and Process Engineering, vol. 27, nr 3/1, (2006), 645-656.
  • [2] DOBROWOLSKI B. and WYDRYCH J., Evaluation of numerical models for prediction of areas subjected to erosion wear, Int. J. of Applied Mechanics and Engineering, vol.11, No.4 (2006), 735-749.
  • [3] DONG K.J., GUO B.Y., CHU K.W., YU A.B. and BRAKE I., Simulation of liquid–solid flow in a coal distributor, Minerals Engineering, 21 (2008), 789–796.
  • [4] FIDAROS D.K., BAXEVANOU C.A., DRITSELIS C.D. and VLACHOS N.S., Numerical modelling of flow and transport processes in a calciner for cement production, Powder Technology, 171 (2007), 81–95.
  • [5] GIDDINGS D., AROUSSI A., PICKERING S.J. and MOZAFFARI E., A 1/4 scale test facility for PF transport in power station pipelines, Fuel, 83 (2004), 2195–2204.
  • [6] RAJENDRAN S., NARASIMHA M., DUTTA A., SINHA M.K. and MISRA A., Modelling of feed distributor at coal washeries, Int. J. Miner. Process., 81 (2006), 178–186.
  • [7] SAKAI M. and KOSHIZUKA S., Large-scale discrete element modeling in pneumatic conveying, Chemical Engineering Science, 64 (2009), 533 – 539.
  • [8] SCHNEIDER H., FRANK Th., PACHLER K. and BER K., A Numerical Study of the Gas- Particle Flow in Pipework and Flow Splitting Devices of Coal-Fired Power Plant, 10th Workshop on Two-Phase Fow Predictions, 9-12 April 2002, Martin-Luther-Universität Halle-Wittenberg, Halle (Saale), Germany, pp. 227-236.
  • [9] SZMOLKE N. and WYDRYCH J., Badania przepływowe kotła małej mocy na ziarno energetyczne, In: Termodynamika w nauce i gospodarce, Politechnika Wrocławska, Wrocław, 2008, pp. 384-389.
  • [10] VUTHALURU H.B., PAREEK V.K. and VUTHALURU R., Multiphase flow simulation of a simplified coal pulveriser, Fuel Processing Technology, 86 (2005), 1195– 1205.
  • [11] WYDRYCH J. and SZMOLKE N., Numerical simulation of fluidization between the tubes, Archives of thermodynamics, vol. 27, No. 4, (2006), 245-253.
  • [12] WYDRYCH J. and SZMOLKE N., Reciprocal correlation in fluid flows, International Conference of Modeling and Simulation – Virtual Forum, Italy , Napoli, 12-26.07.2010.
  • [13] WYDRYCH J., Computational and experimental analysis of gas-particle flow in furnance power boiler instalations with respect to erosion phenomena, Journal of theoretical and applied mechanics, vol.45, No.3 (2007), 513-538.
  • [14] WYDRYCH J., DOBROWOLSKI B. and SKULSKA M., Numerical modelling of erosion wear of components of cyclone separators, Archives of Energetics, vol.XXXVIII, nr 2 (2008), 63-70.
  • [15] YILMAZ A. and LEVY E.K., Formation and dispersion of ropes in pneumatic conveying, Powder Technology, 114 (2001), 168–185.
  • [16] ZHANG J. and COUTHARD J., Theoretical and experimental studies of the spatial sensitivity of an electrostatic pulverised fuel meter, Journal of Electrostatics, 63 (2005), 1133-1149.
  • [17] ZHANG Y, CHEN L., ZHANG C., YU L., WEI X., MAB L. and GUAN C., CFD analysis of pneumatic conveying in a double-tube-socket (DTS_) pipe, Applied Mathematical Modelling, 34 (2010), 3085–3097.
  • [18] ZHU H.P., ZHOU Z.Y., YANG R.Y. and YU A.B., Discrete particle simulation of particulate systems: A review of major applications and findings, Chemical Engineering Science, 63 (2008), 5728 – 5770.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPW8-0019-0088
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