Numerical Simulation of Low Specific Speed American Petroleum Institute Pumps in Part-Load Operation and Comparison With Test Rig Results

Author:

Benigni Helmut1,Jaberg Helmut1,Yeung Hoi2,Salisbury Tony3,Berry Owen3,Collins Tim3

Affiliation:

1. Institute for Hydraulic Fluidmachinery,University of Technology, Graz 8010, Austria

2. Department of Offshore, Process and Energy Engineering,Process Systems Engineering Group, Cranfield University, Bedfordshire MK 43 0AL, United Kingdom

3. Amarinth Ltd.,Bentwater Parks,Rendelesham, Woodbridge, Suffolk IP12 2TW, United Kingdom

Abstract

A low specific speed centrifugal pump is investigated by means of numerical simulation, especially in deep part-load operation. The 3D computational fluid dynamics (CFD) model includes the front and back cavities, a 360 deg impeller and a double volute, as well as suction and pressure pipes. Stationary calculations show a strong clocking effect and lead to an overprediction of the head close to zero flow rate. A one-dimensional estimation of the head at the closed valve operation point is compared to the 3D CFD results and also a series of test rig results. In a second step, the whole head curve is calculated by a fully transient calculation using the shear stress transport–scale-adaptive simulation (SST–SAS) turbulence model. For the net positive suction head (NPSH) estimation, the histogram method is applied providing good correlation to the test rig measurement—as do the head curve and the efficiency.

Publisher

ASME International

Subject

Mechanical Engineering

Reference33 articles.

1. “Centrifugal Pumps for Petroleum, Petrochemical and Natural Gas Industries,” International Standard ISO 13709, 2003.

2. Hydrodynamics of Pumps

3. Impeller Volute and Diffusor Interaction;Pavesi;Design Anal. High Speed Pumps

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