Download PDF by Europump (Auth.): NPSH for Rotodynamic Pumps. a Reference Guide

By Europump (Auth.)

ISBN-10: 1856173569

ISBN-13: 9781856173568

Content material:
Preface

, Page vii
1 - Introduction

, Pages 1-3
2 - the concept that of NPSH

, Pages 5-12
3 - Governing parameters

, Pages 13-19
4 - Suction particular speed

, Pages 21-23
5 - protection margins among NPSHR and NPSHA

, Pages 25-29
6 - useful decision of NPSHR

, Pages 31-32
7 - decision of NPSHA

, Pages 33-37
8 - Examples of calculation of NPSHA

, Pages 39-45
9 - different phenomena

, Pages 47-50
10 - Conclusions

, Page 51
11 - phrases, symbols and units

, Pages 53-56
Appendix A - features of water

, Pages 57-58
Appendix B - NPSH relief for pumps dealing with hydrocarbon drinks and hot temperature water

, Pages 59-61
Appendix C - summary from ISO/CD 9906

, Pages 63-65
Appendix D - Definition of the full suction head HA (abstract from ISO 2548)

, Pages 67-70
Appendix E - desk of conversion for pressure

, Pages 71-72

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Additional resources for NPSH for Rotodynamic Pumps. a Reference Guide

Example text

Air or gas entrainment If a high volumetric content of air or gas is present in the pumped liquid, this may cause a deterioration of the pump performance that must not be confused v^ith cavitation. It is generally agreed that, starting from ~ 2 % of gas content by volume, some deterioration of the pump performance starts to appear and that the maximum possible air or gas content that a conventional centrifugal pump can handle is typically betw^een 5% and 10%, beyond v^hich it v^ill progressively lose prime and stop pumping.

2 m of H2O at 15°C. Appendix E can also be used when pressure values must be converted into different units. 37 8. Examples of calculation of N P S H A The following examples are representative for most situations likely to occur. 1. 322 = 100 000Pa. The head loss at the outlet from the pond and in the conduit is v P amb - — I Head losses — Zo>0 - AH 0-1 W Figure 14 ) Reference level Pump under positive head and liquid under atmospheric pressure. 5 m. TTA . 2. 023 bar or 2340 Pa, p = 999kg/m^. Atmospheric pressure: pamb = 1020 mbar x 100 = 102 000 Pa.

By contrast, the vapour pressure of a liquid is alw^ays expressed as absolute pressure. Since NPSH is the margin or difference betv^een the actual static pressure and the vapour pressure, these must be brought to the same form if an incorrect - usually unnecessarily \ow value of NPSHA is to be avoided. The correction is best made by adding atmospheric pressure to the static pressure gauge reading and then deducting the vapour pressure. All heights must be expressed by using the correct density of the liquid, and the atmospheric pressure must be corrected for the altitude of the site.

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NPSH for Rotodynamic Pumps. a Reference Guide by Europump (Auth.)


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