An experimental testing rig is built to study the performance of a centrifugal pump used in medium consistency technology (MC technology). Pump performances are tested in different pulp concentration, degas pressure differential, and tip clearance ratio. The results show that in medium concentration, pump head and efficiency decreases with increase of pulp concentration. There is a critical concentration above which pump performance drops. Gas separation effect is influenced by the pressure differential over the degas system and the air content in the pulp suspension. In high concentration and small tip clearance conditions, friction loss increases a great deal and results in an efficiency reduction.
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Technical Briefs
References
1.
Duffy
, G. G.
, 2003
, “The Significance of Mechanistic-Based Models in Fiber Suspension Flow
,” Nord. Pulp Pap. Res. J.
, 18
, pp. 74
–80
.10.3183/NPPRJ-2003-18-01-p074-0802.
Mason
, S. G.
, 1990
, “The Flocculation of Pulp Suspensions and the Formation of Paper
,” Tappi J.
, 33
, pp. 440
–444
.3.
Gullichsen
, J.
, and Harkonen
, E.
, 1981
, “Medium Consistency Technology 1: Fundamental Data
,” Tappi J.
, 64
(6
), pp. 69
–72
.4.
Gullichsen
, J.
, and Harkonen
, E.
, 1981
, “Medium Consistency Technology 2: Storage Dischargers and Centrifugal Pumps
,” Tappi J.
, 64
(9
), pp. 113
–116
.5.
Cao
, S.
, and Risaburo
, O.
, 1998
, “Performance Study of Medium Consistency Centrifugal Stock Pumps
,” J. Tsinghua Univ. (Sci & Tech)
, 38
(1
), pp. 5
–9
.10.3321/j.issn:1000-0054.1998.01.0026.
Derakhshandeh
, B.
, Hatzikiriakos
, S. G.
, and Bennington
, C. P. J.
, 2010a
, “The Apparent Yield Stress of Pulp Fiber Suspensions
,” J. Rheol.
, 54
(5
), pp. 1137
–1154
.10.1122/1.34739237.
Derakhshandeh
, B.
, Hatzikiriakos
, S. G.
, and Bennington
, C. P. J.
, 2010b
, “Rheology of Pulp Fibre Suspensions Using Ultrasonic Doppler Velocimetry
,” Rheol. Acta.
, 49
, pp. 1127
–1140
.10.1007/s00397-010-0485-28.
Gandhi
, B. K.
, Singh
, S. N.
, and Seshadri
, V.
, 2001
, “Performance Characteristics of Centrifugal Slurry Pumps
,” ASME J. Fluids Eng.
, 123
, pp. 271
–280
.10.1115/1.13663229.
Gahlot
, V. K.
, Seshadri
, V.
, and Malhotra
, R. C.
, 1992
, “Effect of Density, Size Distribution, and Concentration of Solid on the Characteristics of Centrifugal Pumps
,” ASME J. Fluids Eng.
, 114
, pp. 386
–389
.10.1115/1.291004210.
Murakami
, M.
, and Minemura
, K.
, 1974
, “Effects of Entrained Air on the Performance of a Centrifugal Pump
,” Bull. JSME
, 17
(110
), pp. 1047
–1055
.10.1299/jsme1958.17.104711.
Duffy
, G. G.
, 1995
, “Flow of Medium Consistency Wood Pulp Fiber Suspensions
,” Appita J.
, 48
(1
), pp. 51
–55
.12.
Moller
, K.
, 1976
, “A Correlation of Pipe Friction Data for Paper Pulp Suspensions
,” Ind. Eng. Chem., Process Des. Dev.
, 15
(1
), pp. 16
–19
.10.1021/i260057a00413.
Kerekes
, R. J.
, and Schell
, C. J.
, 1995
, “Effects of Fiber Length and Coarseness on Pulp Flocculation
,” Tappi J.
, 78
(2
), pp. 133
–139
.14.
Engeda
, A.
, and Rautenberg
, M.
, 1987
, “Comparisons of the Relative Effect of Tip Clearance on Centrifugal Impellers
,” ASME J. Turbomach.
, 109
, pp. 545
–549
.10.1115/1.326214615.
Inoue
, M.
, and Furukawa
, M.
, 2002
, “Physics of Tip Clearance Flow in Turbomachinery
,” Proceedings of ASME 2002 Fluids Engineering Division Summer Meeting
, Montreal, Quebec
, Paper No. FEDSM2002-31184.16.
Shyam
, N. S.
, and Kshirsagar
, J.
, 2007
, “Numerical Simulation of Tip Clearance Flow in Semi-Open Impeller Pump
,” Proceedings of FEDSM 2007 5th Joint ASME/JSME Fluids Engineering Conference
, San Diego, CA
, Paper No. FEDSM2007-37355.17.
Engine
, T.
, and Gur
, M.
, 2001
, “Performance Characteristics of a Centrifugal Pump Impeller With Running Tip Clearance Pumping Solid-Liquid Mixtures
,” ASME J. Fluids Eng.
, 123
(9
), pp. 532
–538
.10.1115/1.137903418.
Engine
, T.
, Gur
, M.
, and Calli
, I.
, 2001
, “Slurry and Tip Clearance Effects on the Performance of an Open Impeller Centrifugal Pump
,” Handb. Power Tech.
, 10
, pp. 499
–504
.10.1016/S0167-3785(01)80052-XCopyright © 2013 by ASME
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