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Prediction of the Separation Efficiency of a 10 Mm Hydrocyclone Using Light Liquid Phase Particles. S. Austin, J. Williams, S. Smith and G. D. Wesson. Department of Chemical Engineering FAMU-FSU College of Engineering Tallahassee, FL 32310. Presented at:
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Prediction of the Separation Efficiency of a 10 Mm Hydrocyclone Using Light Liquid Phase Particles S. Austin, J. Williams, S. Smith and G. D. Wesson Department of Chemical Engineering FAMU-FSU College of Engineering Tallahassee, FL 32310 Presented at: 8th Annual International Petroleum and Environmental Conference Houston, TX November 6-9, 2001
Presentation Outline • Motivation • Hydrocyclone principles • Particle separation theory • Hydrocyclone performance measurements • Separation experiments • Results • Conclusions and future work • Acknowledgements
Motivation • Oil production requires water treatment. • Required offshore constraint < 30 ppm of oil in water to environment • Interest in down-hole separation
Hydrocyclone Operation Principles • Tangential feed entry • Creation of core vortex • High local accelerations • Complex internal flows • No moving parts
Liquid Particle -Fluid Interaction • Liquid particles remain spherical • Particle diameter < 50 microns • Rep <0.1 , i.e. creeping flow • Incompressible fluids
Liquid Particle -Fluid Interaction Stokes’ law
Terminal velocity Separation is a function of: Density difference Particle size Continuous phase viscosity Cyclone diameter Local accelerations in 10mm cyclone may approach 10,000 g Particle Motion
Measuring the Performance • Many ways to measure hydrocyclone performance • Due to different applications • “Traditional” separation measurement: QOCOfO(l) QFCF fF(l) QUCU fU(l)
Separation Efficiency • Efficiency based on total fraction of concentration reduction or: • Equivalent to “traditional” efficiency measurement
Separation Theory • Grade underflow purity coefficient-separation efficiency for each particle size • Integrating over sizes yields overall separation efficiency
Grade Efficiency Curve • Continuous function of particles sizes • Hydrocyclone performance is size dependent and GEC varies with particles size • Graphically represented as curve that is usually ‘S’ shaped • “Overall” separation efficiency is a result of the integration of the product of the GPC and the feed distribution
Grade Efficiency Curve Wesson & Petty 1994
10mm Hydrocyclone 2.5 mm 2.5 mm 80 mm 10 mm 1 mm
Experimental Flow Loop hydrocyclone Stirrer Sample Cylinders tank pump
Flow Predictions • Feed pressure varied from 60 - 160 psig • Flow rates determined using stopwatch • Linear regression Qf = f(Po, Pu)
Determine optimum conditions which will give the best separation efficiency Compare concentration separation efficiency with traditional way of determining efficiency. Experiment
Soda Lime Borosilicate Glass glass bubbles and water : r = 0.1 g/cm3 c = 1 cp (Cannon-Fenske viscometer) lmean = 30 mm Model Dispersion
Results Conc vs. oil droplet sizes at 60 psi pressure drop
Results Conc vs. oil droplet sizes at 60 psi pressure drop
Results Grade Purity Function vs. Diameter – 4.85 lpm
Results Overall efficiency vs. Feed flow rate
Conclusions • Glass bubbles-water separation • Best overall efficiency for feed distribution occurs 4.8 lpm feed flow rate (DP=200 psi) • L50 = 10 mm
Vegetable oil dispersion in water: r = 0.1 g/cm3 (pycnometer) d = 50 cp (Cannon-Fenske viscometer) c = 1 cp (Cannon-Fenske viscometer) 30 dynes/cm (Pendant drop method) Model Dispersion
Results Conc vs. oil droplet sizes at 60 psi DP
Results Conc. vs oil droplet sizes at 160 DP
Concentration G-curves Grade Purity Coefficient vs. Oil droplet diameter at various flow rates L/min best GPC-curve “Drop Breakup”
Results The best “overall” efficiency?
Conclusions • Oil-Water separation • Best overall efficiency for feed distribution occurs 3.0 lpm feed flow rate (DP=60 psi) • Best GPC curve occurs at 3.7 lpm feed flow rate (DP=100 psi)
Continued Work • Investigate drop breakup • Investigate source of ‘fish hook” • Investigate use of back pressure to eliminate the air from the core vortex