<p>ME3280 / ME6160 Turbines and Centrifugal Machinery Fall 2017 Dr. T. J. Barber</p><p>Problem 4.1: Nondimensionalization</p><p>Suppose one know that the force F on a particular body immersed in a stream of fluid depended only on body length, L stream velocity, U fluid density, fluid viscosity, that is F f L, U , , Suppose further that the geometry and flow conditions are so complicated that integral or differential theories fail to yield the solution for the force F.</p><p>Reduce the number of dimensional variables using Buckingham’s pi theorem, where each pi = is the product of a number of dimensional variables.</p><p>Problem 4.2: Scaling</p><p>The design point of a compressor is defined as follows: Inlet total pressure=1.5 bars Inlet total temperature=345K Mass flow rate=3.8 kg/s Physical speed=45,000 rpm Total temperature rise=320 K</p><p>These operating conditions are tested using air under standard sea-level conditions on 1 bars and 288K, respectively, using the full-scale compressor. Calculate the mass flow rate, speed and total temperature rise during the test.</p><p>Problem 4.3: Centrifugal Compressor</p><p>Given a centrifugal compressor with the following operating and geometric conditions:</p><p> Flow 5 lb/sec Pt1 14.7 psia Tt1 519 °R</p><p>N a1 30° N 20,000 RPM h 82%</p><p> rtip = 5.35"</p><p> rod = 3.192"</p><p> rid = 1.596"</p><p>Assume radial exit flow in rotating frame of reference, ie, b2 = 0°</p><p>1. Sketch inlet & exit velocity diagram 2. Calculate impeller pressure ratio</p>
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