FABRICATION AND ANALYSIS OF REYNOLDS EXPERIMENT SETUP Mini Project Report Submitted in partial fulfillment of the requirements for the award of the degree of Bachelor of Technology in Mechanical Engineering by SHRI HARSH (Roll No.: B060278ME) PRABHAKAR (Roll No.: B060264ME) RAVI KUMAR (Roll No.: B060225ME) ASHISH KUMAR (Roll No.: B060205PE) Department of Mechanical Engineering NATIONAL INSTITUTE OF TECHNOLOGY CALICUT CERTIFICATE This is to certify that the report entitled “FABRICATION
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International Journal of the Physical Sciences Vol. 6(33)‚ pp. 7456 - 7470‚ 9 December‚ 2011 Available online at http://www.academicjournals.org/IJPS DOI: 10.5897/IJPS11.1092 ISSN 1992 - 1950 © 2011 Academic Journals Full Length Research Paper Numerical study of laminar mixed convection heat transfer of power-law non-Newtonian fluids in square enclosures by finite volume method Mohammad Reza Safaei1*‚ Behnam Rahmanian2 and Marjan Goodarzi3 1 Young Researchers Club and Department of Mechanical
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pressure changes to model You correctly answered: c. changes in the force of contraction of the heart. Experiment Data: Flow (ml/min) 35.0 70.1 105.1 140.2 175.2 210.3 245.3 280.4 Radius (mm) 5.0 5.0 5.0 5.0 5.0 5.0 5.0 5.0 Viscosity 3.5 3.5 3.5 3.5 3.5 3.5 3.5 3.5 05/23/13 Length (mm) 50 50 50 50 50 50 50 50 page 2 Pressure (mm Hg) 25 50 75 100 125 150 175 200 Post-lab Quiz Results You scored 100% by answering 4 out of 4 questions correctly
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DESIGN CONSIDERATIONS * System: Ethanol – water * Feed rate: 225kmol/h * Feed composition: 28 mol% ethanol * Feed condition: 50% saturated liquid & 50% saturated vapor * 97% of ethanol recovery is required * Operating pressure: 1bar * Distillate composition: 81 mol% ethanol * Column type: Sieve tray column * Operating condition: 70% of flooding Applying material balance to the rectifying section (Eqn 01); V=L+D Applying material balance for the more volatile
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Flow‚ Turbulence and Combustion 63: 269–291‚ 1999. © 2000 Kluwer Academic Publishers. Printed in the Netherlands. 269 Approximate Wall Boundary Conditions in the Large-Eddy Simulation of High Reynolds Number Flow W. CABOT and P. MOIN Center for Turbulence Research‚ Stanford University‚ Bldg. 500‚ 488 Escondido Mall‚ Stanford‚ CA 94305-3030‚ U.S.A. Abstract. The near-wall regions of high Reynolds numbers turbulent flows must be modelled to treat many practical engineering and aeronautical
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Drilling Fluids Physical Properties of Mud PETE 101 Introduction to Petroleum Engineering Submitted to: Dr. Shirish Patil Petroleum Engineering Department University of Alaska Fairbanks By: Me Abstract Drilling fluid (mud) is a mixture of water or oil‚ or emulsion base ‚ clay‚ weighing material and some chemicals. The combination of mud may vary according to the changes in formation. Drilling fluid plays essential role in drilling process. For this experiment we
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Motion in a Viscous Medium Aim The aim of this experiment is to measure the terminal velocity of spherical beads falling under gravity in a liquid determine‚ and hence determine its viscosity using Stoke’s law. Introduction When a stationary solid object is complete or partially immersed in a fluid‚ it experiences an upthrust or buoyant force. According to Archimedes’ principle‚ this buoyant force B is given by where ρ is the density of the fluid‚ Vs is the immersed volume of the
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tube. d) Stopwatch e) Graduated cylinder THEORY Reynolds number is used to distinguish between laminar‚ transitional and turbulent flows. Re = Reynolds number V = Fluid velocity (m/s) d = Pipe diameter (0.012m) v = Kinematic viscosity (0.893 x 10-6m2/s) Laminar Flow‚ Re < 2000 Laminar flow denotes a steady condition where all stream lines follow parallel paths. Under this condition‚ the dye will remain easily identifiable as a solid core. Transitional Flow‚ 2000 <
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The binder is recommended in direct‚ discharge and resist printing. Prints produced with Helizarin Binder UDT have a pleasingly soft handle and are resistant to ageing. Compared to other binders‚ Helizarin Binder UDT only reduces very little the viscosity of synthetic thickeners (e.g. Lutexal HIT) Guideline Recipes Standard recipe for low solvent print . . . g/kg 25 g/kg 50 - 180 g/kg 20 - 25 g/kg 150 - 250 g/kg . . . g/kg 25 g/kg 50 - 180 g/kg 30 - 35 g/kg Water Luprintol MCL Helizarin Binder UDT
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10 MIXING AND AGITATION gitation is a means whereby mixing of phases can be accomplished and by which mass and heat transfer can be enhanced between phases or with external surfaces. In its most general sense‚ the process of mixing is concerned with all combinations of phases of which the most frequently occurring ones are A 7. gases with gases. 2. gases into liquids: dispersion. 3. gases with granular solids: fluidization‚ pneumatic conveying‚ drying. 4. liquids into gases: spraying and atomization
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