Abstract
In order to investigate the characteristics of particle-induced pressure loss in the solid–liquid lifting pipe, a series of experiments were conducted in 200 mm diameter lifting pipe. Simulation manganese nodules with five different mean diameters of 10 mm, 20 mm, 30 mm, 40 mm and 50 mm were used, both in isolation and a combination in equal fraction by mass. The flow velocities in the lifting pipe ranged from 0.12 m/s to 1.61 m/s, and the mass of particles employed was 10 kg for each particle diameter. Three regimes, wavy bed, partly fluidization, and fully fluidization, were observed over the flow velocity. The solid–liquid pressure drop data were measured by differential pressure transmitter, and pressure drop caused by the solid particles was calculated and analyzed. The results show that the evolutions of the pressure loss due to solid particles are relevant to the solid–liquid flow regimes, and they are distinctly influenced by fluid velocity and particle size.
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References
AZIZ A I, MOHAMED H I. A study of the factors affecting transporting solid-liquid suspension through pipelines [J]. Open Journal of Fluid Dynamics, 2013, 3(3): 152–162.
LAHIRI S K, GHANTA K C. Prediction of pressure drop of slurry flow in pipeline by hybrid support vector regression and genetic algorithm model [J]. Chinese Journal of Chemical Engineering, 2008, 16(6): 841–848.
KAUSHAL D R, SATO K, TOYOTA T, FUNATSU K, TOMIT Y. Effect of particle size distribution on pressure drop and concentration profile in pipeline flow of highly concentrated slurry [J]. International Journal of Multiphase Flow, 2005, 31(7): 809–823.
OZBELGE T A, CAMCIUNAL G. A new correlation for two-phase pressure drops in fully developed dilute slurry up-flows through an annulus [J]. Chemical Engineering Communications, 2009, 196(4): 491–498.
KAUSHAL D R, TOMITA Y. Solids concentration profiles and pressure drop in pipeline flow of multisized particulate slurries [J]. International Journal of Multiphase Flow, 2002, 28(10): 1697–1717.
XU Hai-liang, XIE Qiu-min, WU Bo, ZHAO Hai-ming, XU Shao-jun. Numerical simulation and analysis of gas hydrate mining pipe hydraulic lifting [J]. Journal of Central South University, 2015, 46(11): 4062–4069. (in Chinese)
JANA A K, DAS G, DAS P K. Flow regime identification of two-phase liquid–liquid upflow through vertical pipe [J]. Chemical Engineering Science, 2006, 61(5): 1500–1515.
CHENG Li-xin, RIBATSKI G, THOME J R. Two-phase flow regimes and flow-regime maps: Fundamentals and applications [J]. Applied Mechanics Reviews, 2008, 61(5): 1239–1249.
DIDWANIA A K, HOMSY G M. Flow regimes and flow transitions in liquid fluidized beds [J]. International Journal of Mutiphase Flow, 1981, 7(6): 563–58.
LIU Zhong-liang, SHI Ming-heng, DAI Guo-sheng. Mechanism analysis of non-uniform distribution for solid-liquid flow in vertical pipe [J]. Journal of China University of Petroleum, 1997, 21(5): 56–60. (in Chinese)
SOTGIA G, TARTARINI P, STALIO E. Experimental analysis of flow regimes and pressure drop reduction in oil-water mixtures [J]. International Journal of Multiphase Flow, 2008, 34(12): 1161–1174.
SUN Zhi-qiang, SHAO Shuai, GONG Hui. Gas-liquid flow regime recognition based on wavelet packet energy entropy of vortex-induced pressure fluctuation [J]. Measurement Science Review, 2013, 13(2): 83–88.
PIETRZAK M. Flow regimes and volume fractions of phases during liquid–liquid two-phase flow in pipe bends [J]. Experimental Thermal and Fluid Science, 2014, 54(4): 247–258.
XIA J X, NI J R. MENDOZA C. Hydraulic lifting of manganese nodules through a riser [J]. Offshore Mechanics and Arctic Engineering, 2004, 126(1): 72–77.
TOKANAI H, HARADA E, HASEGAWA J, KURIYAMA M. Turbulent transition and pressure drop in solid-high viscosity liquid upward flow through vertical pipe [J]. Chemical Engineering, 2004, 30(4): 509–514.
MATOUSEK V. Pressure drops and flow regimes in sand-mixture pipes [J]. Experimental Thermal and Fluid Science, 2002, 26(6, 7): 693–702.
NEWITT D M, RICHARDSON J F, GLIADON, B J. Hydraulic conveying of solids in vertical pipes [J]. Transactions of the Institution of Chemical Engineers, 1961, 39: 93–100.
DOBRNJAC M. Determination of friction coefficient in transition flow region for waterworks and pipelines calculation [J]. International Journal of Engineering, 2012, 10(3): 137–142.
PINKER R A, HERBERT M V. Pressure loss associated with compressible flow through square-mesh wire gauzes [J]. Journal of Mechanical Engineering and Sciences, 1967, 9(1): 11–23.
KIM S M, KIM J, MUDAWAR I. Flow condensation in parallel micro-channels–Part 1: Experimental results and assessment of pressure drop correlations [J]. International Journal of Heat and Mass Transfer, 2012, 55(4): 971–983.
KIM S M, MUDAWAR I. Flow condensation in parallel microchannels–Part 2: Heat transfer results and correlation technique [J]. International Journal of Heat and Mass Transfer, 2012, 55(4): 984–994.
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Foundation item: Projects(51174037, 51339008) supported by the National Natural Science Foundation of China
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Song, Yw., Zhu, Xj., Sun, Zq. et al. Experimental investigation of particle-induced pressure loss in solid–liquid lifting pipe. J. Cent. South Univ. 24, 2114–2120 (2017). https://doi.org/10.1007/s11771-017-3620-8
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DOI: https://doi.org/10.1007/s11771-017-3620-8