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Response of energy-size reduction to the control of circulating load in vertical spindle pulverizer

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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
In the vertical spindle pulverizer (VSP), the large circulation ratio and high ash and sulfur contents in circulating load would result in intensive energy consumption and low grinding efficiency. Although the control of circulating load would help increase the energy efficiency, no quantitative study has been conducted due to the high temperature and pressure in the closed VSP. In this study, response of energy-size reduction to the control of circulating load was studied by the experimental simulation method. Coal mixtures with fine/coarse ratio of 11:1, 8:1 and 6:1 were ground by a lab-scale roller mill. Energy-size reductions of the coarse coal were compared to evaluate the influence of circulating load control. Results showed that the product with the coarse coal increased by 30% when the specific breakage energy was 1.0 kWht–1 as the circulation ratio decreased from 11 to 6. Meanwhile, a breakage characteristic index of the coarse coal was two times higher due to the cushioning effect of fines. Besides, decrease of circulation ratio led to increase of the breakage rate of coarse coal, and the energy saving improved by 57%. With the same energy input of 2.0 kWht-1, the yield of –0.09 mm pulverized fuel (PF) increased from 22 to 43%. Therefore, controlling the circulating load is an effective method to improve the breakage rate of coarse coal and energy efficiency for PF generation.
Rocznik
Strony
793--801
Opis fizyczny
Bibliogr. 22 poz., rys., tab.
Twórcy
autor
  • School of Chemical Engineering and Technology, China University of Mining & Technology, Xuzhou, Jiangsu 221116, China
autor
  • School of Chemical Engineering and Technology, China University of Mining & Technology, Xuzhou, Jiangsu 221116, China
  • Advanced Analysis & Computation Center, China University of Mining & Technology, Xuzhou, Jiangsu 221116, China
autor
  • School of Chemical Engineering and Technology, China University of Mining & Technology, Xuzhou, Jiangsu 221116, China
autor
  • School of Chemical Engineering and Technology, China University of Mining & Technology, Xuzhou, Jiangsu 221116, China
autor
  • School of Chemical Engineering and Technology, China University of Mining & Technology, Xuzhou, Jiangsu 221116, China
autor
  • Advanced Analysis & Computation Center, China University of Mining & Technology, Xuzhou, Jiangsu 221116, China
autor
  • School of Chemical Engineering and Technology, China University of Mining & Technology, Xuzhou, Jiangsu 221116, China
Bibliografia
  • AUSTIN L.G., BAGGA P., 1981. An analysis of fine dry grinding in ball mills, Powder Technol., 28, 83-90.
  • CELIK M.S., 1988. Acceleration of breakage rates of anthracite during grinding in a ball mill, Powder Technol., 54, 227-233.
  • FUERSTENAU D.W., ABOUZEID A.Z.M., 1991. Effect of fine particles on the kinetics and energetics of grinding coarse particles, Int. J. Miner. Process, 31, 151-162.
  • FUERSTENAU D.W., ABOUZEID A.Z.M., PHATAK P.B., 2010. Effect of particulate environment on the kinetics and energetics of dry ball milling, Int. J. Miner. Process, 97, 52-58.
  • FUERSTENAU D.W., PHATAK P.B., KAPUR P.C., ABOUZEID A.Z.M., 2011. Simulation of the grinding of coarse/fine (heterogeneous) systems in a ball mill, Int. J. Miner. Process, 99, 32-38.
  • KOJOVIC T., SHI F., BRENNAN M., 2015. Modelling of vertical spindle mills. Part 2: Integrated models for E-mill, MPS and CKP mills, Fuel, 143, 602-611.
  • NAPIER-MUNN T.J., MORRELL S., MORRISON R.D., KOJOVIC T., 1996. Mineral comminution circuits: their operation and optimisation. ISBN 064628861x. Julius Kruttschnitt Mineral Research Centre, Chapter 4.
  • SHI F., 2014a. Coal breakage characterization-Part 2: Multi-component breakage modeling, Fuel, 117, 1156-1162.
  • SHI F., 2014b. Coal breakage characterisation-Part 3: Applications of the multi-component model for HGI prediction and breakage simulations, Fuel, 117, 1163-1169.
  • SHI F., HE Y.Q., 2011, April. Efficiency improvements in coal fired utilities, Asia-Pacific Partnership on Clean Development and Climate. Julius Kruttschnitt Mineral Research Centre and China University of Mining & Technology.
  • SHI F., KOJOVIC T., 2007. Validation of a model for impact breakage incorporating particle size effect, Int. J. Miner. Process, 82, 156-163.
  • SHI, F., KOJOVIC, T., BRENNAN, M., 2015. Modelling of vertical spindle mills. Part 1: Sub-models for comminution and classification, Fuel, 143, 595-601.
  • SHI F., ZUO W.R., 2014. Coal breakage characterization-Part 1: Breakage testing with the JKFBC, Fuel, 117, 1148-1155.
  • VERMA R., RAJAMANI R.K., 1995. Environment-dependent breakage rates in ball milling, Powder Technol., 84, 127-137.
  • WANG S., 2013. Particle separation behavior of recirculating load of power station pulverizer in the dilute phase vibrated gas-solid fluidized bed, PhD Thesis, Xuzhou: China University of Mining and Technology.
  • WANG S., HE Y.Q., HE J.F., GE L.H., LIU Q., 2013a. Experiment and simulation on the pyrite removal from the recirculating load of pulverizer with a dilute phase gas-solid fluidized bed, Inter. J. Min. Sci. Technol., 23, 301-305.
  • WANG S., HE Y.Q., WANG H.F., HE J.F., CAI B., 2013b. Study on recirculating loads of power plant pulverizer separated by dilute gas-solid fluidized bed, J. China Coal Soc, 38(3), 480-486. (In Chinese)
  • WEI H., HE Y.Q., SHI F.N., ZHOU N.X., WANG S., GE L.H., 2014. Breakage and separation mechanism of ZGM coal mill based on parameters optimization model, Inter. J. Min. Sci. Technol., 24, 285-289.
  • WOODBURN E.T., KALLIGERIS S.A., 1987. The investigation of the kinetics of breakage as a first step towards the assessment of the economics of ultra-Fine grinding of a British low-rank coal, Powder Technol, 53,137-143.
  • XIE W.N., HE Y.Q., LUO C., ZHANG X., LI H., WANG H.F., SHI F.N., 2015b. Energy-Size Reduction of Coals in the Hardgrove Machine, Inter. J. Coal Prep. Util., 35(2), 51-62.
  • XIE W.N., HE Y.Q., ZHANG Y.H., HUANG Y., LI H., WEI H., WANG H.F., 2015a. Simulation study of the energy-size reduction of MPS vertical spindle pulverizer, Fuel, 139, 180-189.
  • ZUO W., 2013. Mathematic modeling and optimization on the process of MPS coal mill, PhD Thesis, Xuzhou: China University of Mining and Technology.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-cfbfbe8e-e85b-4b28-810f-e5f0712acf7f
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