Latest Downloads
-
Crane Fluid Flow Examples in MS ExcelArt Montemayor - Jan 31 2012 08:22 PM
-
Surface Tension of Pure Liquidsankur2061 - Jan 24 2012 02:43 PM
-
Filament Yarn Quench Air Systemankur2061 - Jan 18 2012 05:03 PM
-
Gravity Tank Drainage Calculator for Uniform Cross Sectionsstudent88 - Dec 19 2011 03:16 PM
-
Gravity Tank Drainage Calculator for Hemispherical Cross Sectionsstudent88 - Dec 19 2011 03:14 PM
-
Gravity Tank Drainage Calculator for Cylindrical Cross Sectionsstudent88 - Dec 19 2011 03:13 PM
-
Drainage Between Two Reservoirsstudent88 - Dec 19 2011 03:11 PM
-
Cooling Tower Water Loss CalculatorDB Shah - Dec 19 2011 02:24 PM
-
Equivalent Length Calculations for Pipes and Valvesankur2061 - Nov 17 2011 09:00 AM
-
Slurry Pump Calculation 1.1mramono - Nov 10 2011 05:10 PM
Popular Store Titles
Tank Jacket Calculator
Specification Sheet Collection
PIPESIZE
Relief Valve Sizing
Rupture Disc Sizing
Recent Status Updates
-
ChristaSCheck out the latest news headlines in this issue of ChExpress: http://www.cheresources.com/invision/blog/17/entry-206-chexpress-february-7-2012/
-
Chris HaslegoNew blog entry - Revisiting the Reputation System - http://www.cheresources.com/invision/blog/1/entry-205-revisiting-the-reputation-system/
Chemical and Process Engineering Resources
Recent Blog Entries
Centrifugal Pumps: Basic Concepts of Operation, Maintenance, and Troubleshooting
Nov 08 2010 04:50 PM | Mukesh Sahdev in Fluid FlowShare this topic:
Requirements for Consistent Operation
Centrifugal pumps are the ultimate in simplicity. In general there are two basic requirements that have to be met at all the times for a trouble free operation and longer service life of centrifugal pumps. The first requirement is that no cavitation of the pump occurs throughout the broad operating range and the second requirement is that a certain minimum continuous flow is always maintained during operation. A clear understanding of the concept of cavitation, its symptoms, its causes, and its consequences is very much essential in effective analyses and troubleshooting of the cavitation problem.
Just like there are many forms of cavitation, each demanding a unique solution, there are a number of unfavorable conditions which may occur separately or simultaneously when the pump is operated at reduced flows. Some include:
•Cases of heavy leakages from the casing, seal, and stuffing box
•Deflection and shearing of shafts
•Seizure of pump internals
•Close tolerances erosion
•Separation cavitation
•Product quality degradation
•Excessive hydraulic thrust
•Premature bearing failures
Each condition may dictate a different minimum flow low requirement. The final decision on recommended minimum flow is taken after careful "techno-economical" analysis by both the pump user and the manufacturer. The consequences of prolonged conditions of cavitation and low flow operation can be disastrous for both the pump and the process. Such failures in hydrocarbon services have often caused damaging fires resulting in loss of machine, production, and worst of all, human life. Thus, such situations must be avoided at all cost whether involving modifications in the pump and its piping or altering the operating conditions. Proper selection and sizing of pump and its associated piping can not only eliminate the chances of cavitation and low flow operation but also significantly decrease their harmful effects.


FB



