water & wastewaterif there were a hole in the bucket, the water would fly out ---a centrifugal...
TRANSCRIPT
Water & Wastewater Pumping Systems
An MWEA Maintenance Committee Seminar
Fall 2017
Centrifugal & Positive Displacement
Pumps
Ken ColstonKDC Educational Consulting
40 Years in Water & Wastewater
Retired Director of Maintenance Operations, Ypsilanti Community Utilities Authority
PUMP AND SYSTEM BASICS
WHAT’S A PUMP?
What is a Pump?
A Pump is a Machine Which Adds
Energy to a Fluid for the Purpose of
Increasing the Pressure or Moving it
along a Pipeline.
A Pump, in fact, Doesn’t Create
Anything.
It Doesn’t Make Water
It Doesn’t Make Pressure
THERE ARE TWO BASIC TYPES OF PUMPS
• Positive displacement pump, AKA Force Pump, which adds energy directly to a movable boundary, which imparts the energy to the fluid.
• Examples include screw pumps, piston pumps, gear pumps.
ONE TYPE IS THE:
THERE ARE TWO BASIC TYPES OF PUMPS:
• Dynamic pump, AKA Kinetic Pump, which adds the energy indirectly through a rotating part in the form of velocity, and subsequently converts the velocity to pressure.
• These pumps are commonly referred to as Centrifugal pumps.
THE OTHER TYPE IS THE:
Imagine That You Fill A Bucket With Water.
• The water stays in the bucket (as long as there aren’t holes in it)
• If you take the bucket and turn it over, the water will pour out.
• However.....
If you spin the bucket, and ADD
ENERGY in the form of centrifugal
force...
The energy you add overcomes the force
of gravity, and the water is forced to the
outer part of the bucket.
The harder you spin the bucket, or the longer your arms, the more centrifugal force is generated. If there were a hole in the bucket, the water would fly out ---
A CENTRIFUGAL PUMP
WORKS THE SAME
WAY.
The Fluid Enters The
Pump Through The
Inlet Or Suction Eye,
Where The Impeller
Adds Energy (In The
Form Of Velocity)
Through Centrifugal
Force, And Forces The
Fluid Out The Edges
Of The Impeller To The
Discharge.
When the fluid leaves
the impeller, there is a
decrease in velocity.
Velocity and pressure
are inversely
proportional.
The decrease in
velocity results in an
increase in pressure
as the fluid leaves
the pump.
The Pump Can’t Do Its Job Until The Fluid Enters The
Impeller.
General Pump Classification
Kinetic
Pumps
Vertical Turbine
Lineshaft Submersible Axial Flow
Centrifugal
Split CaseOverhung Impeller
Kinetic Pumps
General Pump Classification
Axial Split Case vs. Overhung Impeller
Typical Overhung Impeller Pump Types
Frame Mounted
Close Coupled
Submersible
Basic Overhung Impeller Types
Enclosed Semi-Open
Open
Special Impeller/Pump Types
Centrifugal
Screw
Vortex
Special Impeller/Pump Types
Self Priming
“Trash”
Chopper
Basic Considerations
Flow and head conditions (avg, min, max)
Current vs. projected future flows
Liquid being pumped (rags, grit, grease,
chemical additives?)
Site constraints (space, power
availability, aesthetics)
Other challenges (retrofit, forcemain
network, terrain)
Important Details
Look closely at suction and discharge conditions
NPSHa > NPSHr
Potential for hydraulic transients
Pump speed (1200-1800 rpm)
Motor selection
Continuous vs. intermittent duty
Inverter duty (if VFDs are to be used)
Size motor for run-out condition
Packing vs. mechanical seals
Discuss/consider hardened materials?
An Overview of the Basic Centrifugal Pump Types
• General Purpose
• Overhung Impeller
• Thought of generally for flows less than 1000 GPM (Not Necessarily a good “end point”)
End Suction Pumps
An End Suction Pump Cross Section
• Basically same as End suction
• Big Difference between “circulators” and In-Line pumps
• An excellent choice when space is at a premium
In-Line Pumps
• DOUBLE SUCTION, SINGLE AND DOUBLE DISCHARGE
• Support Between Bearings
• Thought of as a “Cadillac”
• To 30,000 GPM
• The “devil’s in the details”
Split Case Pumps
A double suction impeller is really just
two end suction impellers, back to
back, with a common discharge.
Double Suction Split Case
TYPICAL SPLIT CASEPUMP
• Vertically suspended lineshaft driven non-clogs and Sump Pumps
• Good choice in mechanical rooms, where presence above cover is acceptable.
• Sump depths to 6-7’
• 1-1/2” TO 4” SOLIDS HANDLING in Non Clogs, ¼” in Sump Pumps. (Watch the Specs.)
Column Pumps
• CENTERLINE DISCHARGE, UL EXPLOSION PROOF Or Non-EXPLOSION PROOF.
• SLIDE RAIL SUBMERSIBLE NON-CLOGS
• Best for deeper sumps, or where above cover is unacceptable.
• (Except for elevator Pit, I’d go with Tandem Seals)
Submersible Pumps (Slide Rail Shown)
Submersible
Typically Central Plant in Municipal Wastewater Treatment.
A lot of details to pay attention to.
Dry Pit Non Clogs
CONFIGURATIONS
CHOPPER PUMPS
Externally adjustable
back pull-out design
All hardened
chopper
components
Oil lubricated
Ball bearings
Flushless
mechanical seal
BACK PULL-OUT DESIGN
No need to disconnect
from piping
Externally adjustable
back pull-out
Adjust ALL cutting
clearances externally
FLUSHLESS SEAL OPTION
Grinder/Chopper (Not a Pump)
Positive Displacement Pumps:
• Advantages
• Disadvantages
Positive Displacement Pumps:
•Models/styles•Rotary Lobe•Plunger/Piston•Peristaltic/Hose •Diaphragm•Disc Pumps•Progressive Cavity•Metering
Rotary Lobe
Plunger/Piston
Peristaltic/Hose
Diaphragm
Disc Pumps… A Type Of Diaphragm Pump
Progressive Cavity
Metering
Positive Displacement Pumps:
• Characteristics
• Maintenance
Questions?
•Kinetic – Dynamic – Centrifugal ???
•Force – Positive Displacement ???