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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Transient Behavior of Extruders by Rajath Mudalamane, Dr. David I. Bigio University of Maryland at College Park
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND INTRODUCTION: Research goals STAGE-I: Robust screw design- ‘Minimize variations/fluctuations in the process by using the inherent damping nature of transient behavior of extruders’ STAGE-II: Unsteady state extrusion process ‘Design for the manufacture of materials with engineered variations in quality (based on performance requirements of the material)’
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Research goals contd Knowledge of transient behavior of extruders Experimental observations [1,2,3,4,5,6,7] Extrusion Process Q N Temperatures d1d1 d2d2 d3d3 d4d4 ? Theoretical modeling [8,9,10]
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND INTRODUCTION: Schematic of an Extruder FEEDER MELTING PARTIALLY FILLED, MELT CONVEYING MIXING DIE PRESSURE GENERATION Downstream Processing Feeder Dynamics Feed stock variations Bed instability Die flow instability: Spurt flow, shark skin surface roughness
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND INTRODUCTION: Disturbance rejecting characterisics of partly filled extruders
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Introduction contd. Q in Q out Q in Q out
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Transient model: Extruder Geometry Kneading block / restrictive element Starved region Fill length (L f ) Filled region Conveying section FLOW DIRECTION Control Volume (dotted lines) H
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Flow into Control Volume, supplied by starved regions (1) Apply law of conservation of mass to control volume : Rate of change of accumulation of material in Control Volume =- Flow out of Control Volume driven by pressurization in filled region = Macroscopic material balance Modified White et al approach
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND V f - volume in the filled region Q st - flow in the starved regions Q fl - flow in the filled region L f - length of the filled region – Fill fraction in starved region
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND L is the total length of the extruder section and L= L st +L f For a given geometry and fluid:
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Simulation results: Step response
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Frequency response
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Sinusoidal disturbance in feedrate
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Sinusoidal disturbance in feedrate
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Effect of fill level in extruder
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Effect of Depth
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Step change in screw speed
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Sinusoidal disturbance in N
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Conclusions Critical Frequency: –All higher frequencies are damped out and lower frequencies experience little damping –Function of Screw geometry and operating conditions Critical frequency decreases with increasing fill level and vice versa Self-leveling response by output rate to changes in screw speed Screw speed CAN be used to control output rate with limitations on frequency
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND Bibliography 1.Tadmor, Z., Klein, I., Van Nostrand Reinhold Co., N.Y., 1976. 2.White, F.M.,’Viscous Flow’, McGraw-Hill, 1997. 3.Bird, B.S., Stewart, Lightfoot, ‘Transport Phenomena’, McGraw-Hill, 1986
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND 8.White, J.L. and Kim, E.K., SPE ANTEC, 2000. 9.White, J.L. and Kim, E.K., Poly. Eng. & Sci., Vol. 41, n 2, 2001. 10.Rauwendaal, C., ‘Polymer Extrusion’, Hanser, 1994. 11.Booy, M.L., Poly. Eng. & Sci., Vol. 20, 1980. Bibliography (contd.)
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POLYMER PROCESSING LABORATORY UNIVERSITY OF MARYLAND INTRODUCTION contd.
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