Contents Prologue About the Authors 1 Basic Pump Principles Introduction How do pumps work?. Pressure measurement Atmospheric pressure ATM Absolute pressure psia Gauge pressure psig Vac
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CUSTODIO
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Pumps
by Larry Bachus and Angel Custodio
ELSEVIER
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USA
JAPAN
Elsevier Ltd, The Boulevard, Langford Lane, Cdlington, Oxford OX5 l G B , UK
Elsevier Inc, 360 Park Avenue South, New York, NY 1001 0- 171 0, USA
Elsevier Japan, Tsunashima Building Annex, 3-20- 1 2 Yushima, Bunkyo-ku, Tokyo 11 3, Japan
Copyright 0 2003 Bachus Company, Inc
Published by Elsevier Ltd
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British Library Cataloguing in Publication Data
Bachus, Larry
Know and understand centrifugal pumps
1 Centrifugal pumps
I.Title II.Custodio, Angel
6 2 1.6’7
ISBN 1856174093
N o responsibility is assumed by the Publisher for any injury and/or damage to
persons or property as a matter of products liability, negligence or otherwise, or from any use or operation of any methods, products, instructions or ideas contained in the material herein
Published by
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Trang 8Contents
Prologue
About the Authors
1 Basic Pump Principles
Introduction
How do pumps work?
Pressure measurement
Atmospheric pressure (ATM)
Absolute pressure (psia)
Gauge pressure (psig)
Vacuum
Pump head
Specific gravity
Pressure measurement
Pressures inside the pump
2 NPSH, Net Positive Suction Head
Introduction
Definition of NPSHr (required)
Definition NPSHa (available)
3 Cavitation
Introduction
Vapor pressure
Cavitation
The effects of vapor pressure o n pump performance
Cavitation: A practical discussion
Review for preventing cavitation
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Cavitation review
4 The Affinity Laws
Introduction
The Laws
The Affinity Laws and the impeller diameter
What’s the practical application of these laws?
5 Useful Work and Pump Efficiency
Useful work from a pump
Flow determination
Pump efficiency
Factors that affect the efficiency
Calculating pump efficiency
6 Pump Classification
Introduction
Positive displacement pumps
Centrifugal pumps
Conceptual difference
Centrifugal volute pumps
Types of centrifugal pumps
Overhung impeller
Impeller between the bearings
Turbine pumps
Specific duty pumps
API (American Petroleum Institute) pumps
Vertical turbine pumps
Non-metallic pumps
Magnetic drive pumps
Canned motor pumps
Pump impellers
Turbine impellers
Conventional impellers
Suction specific speed, Nss
Open impellers
Semi open impeller
Totally enclosed impeller
Wear bands
Specific speed, Ns
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7 Understanding Pump Curves
Pump performance curves
History
Head versus pressure
H-Q
Pump efficiency
The energy (BHp) curve
The pump’s minimum requirements (NPSH)
Special design pumps
Family curves
The system controls the pump
The elements of the Total Dynamic Head ( T D H )
Determining the Hs
Determining the H p
Calculating the H f and Hv
The dynamic system
Variable elevations
The happy zone
Dynamic pressures
Variable resistances
Short term resistance changes
Long term resistance changes
Pumps in parallel and pumps in series
Pumps in parallel
Three tips
Pumps running in series
Combined parallel and series pump operation
9 Shaft Deflection
Introduction
Operation, design and maintenance
Signs of shaft deflection
Interpreting the evidence
The sweet zone
The dual volute pump
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10 Pump and Motor Alignment
Introduction
Types of misalignment
Alignment techniques
Equipment alignment sequence
Coupling alignment
11 Bearings
Introduction
Bearing lubrication
Bearing failure
Bearing maintenance
Bearing seals
12 Pump Shaft Packing
History
Vegetable fibers
Reciprocating action
Packing
Rotary action
Synthetic fibers
Compression packing
The lantern ring
The packing lubricant
Stages in the life of packing
13 Mechanical Seals
Pump packing
History
The mechanical seal
The single, unbalanced, inside mounted mechanical seal
The single, outside-mounted, unbalanced seal
The single, balanced, internal mechanical seal
The single, balanced, external mechanical seal
Advantages of O-rings
The balance effect
Advantages of balance
Balance explained by math
Cartridge mechanical seals
Double seals
The tandem dual seal
The back-to-back double seal
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The face-to-face dual seal
Support systems for dual seals
The thermal convection tank
The pumping unit
14 Failure Analysis of Mechanical Seals
Causes of premature seal failure
O-ring (the elastomer) failure
The elastomer sticks to the shaft
The shaft frets under the shaft seal
Incorrect installation dimension
Environmental controls for difficult sealing applications
Difficult pumping applications for mechanical seals
Environmental controls
Proper pump repair alignment methods
15 Common Sense Failure Analysis
Pump maintenance files
Failure analysis on centrifugal pumps
Why is this pump in the shop?
16 Avoiding Wear in Centrifugal Pumps
Introduction
Erosion
Corrosion
Wear rings
Fluid velocity accelerates wear
Turbulence
Throttling
17 Pump Piping
Introduction
The Submergence Laws
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Index
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Trang 14Prologue
Trang 15About the Authors
Angel specializes in the installation and imple- mentation of Preventive Maintenance Systems through his consulting engineering company formed
in 1987 in Puerto Rico His installations have given
approaches to hands-on maintenance and operator
Engineers
Trang 16Know and Understand Centrifugal Pumps
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suction piping The fluid must be available to the pump with sufficient energy so that the pump can work with the fluid’s energy The pump cannot suck on or draw the liquid into the pump The concept of the fluid being available to the pump is discussed in detail in Chapter 2 of this book
Positive displacement (I’D) pumps take the fluid at the suction nozzle and physically capture and contain the fluid in some kind of moveable enclosure The enclosure may be a housing with a pulsing diaphragm,
or between the teeth of rotating gears There are many designs The
the fluid into the pump The captured fluid is physically transported
Inside the pump, the expanded moveable enclosure then contracts or the available space compresses This generates a zone of high pressure inside the pump, and the fluid is expelled into the discharge piping,
that a PD pump can generate is mostly a function of the size of the pump housing, the speed of the motor or driver, and the tolerances between the parts in relative motion The pressure or head that a PD pump can develop is mostly a function of the thickness of the casing
diaphragm, or meshed gear teeth As these parts wear, the pump will
changed with a degree of frequency based on time and the abrasive and lubricating nature of the fluid Changing these parts should not be
Trang 17Basic Pump Principles
- ROTATION
Fiaure 1-3
viewed as breakdown maintenance Nothing is broken This periodic servicing is actually a production function to return the pump to its best or original efficiency
Centrifugal pumps also require that the fluid be available to the pump’s suction nozzle with sufficient energy Centrifugal pumps cannot suck or draw the liquid into the pump housing The principal pumping unit of
The impeller is attached to a shaft The shaft spins and is powered by the motor or driver We use the term driver because some pumps are
impeller and is trapped between the impeller blades The impeller blades contain the liquid and impart speed to the liquid as it passes from the impeller eye toward the outside diameter of the impeller As the fluid accelerates in velocity, a zone of low pressure is created in the
the pump with sufficient energy
The liquid leaves the outside diameter of the impeller at a high rate of speed (the speed of the motor) and immediately slams into the internal casing wall of the volute At this point the liquid’s centrifugal velocity
Bernoulli Principle in reverse) Because the motor is spinning, there is also rotary velocity The fluid is conducted from the cutwater around
pathway increases, the rotary velocity decreases and even more energy