This document contains notes from a training session on pump hydraulics. It discusses key topics like hydraulic theory, types of pumps, pump components, how pumps interact with systems, parallel and series operation, cavitation, net positive suction head (NPSH), minimum flow requirements, effects of viscosity and speed changes, and unstable pump curves. Diagrams illustrate pump curves, system curves, NPSH curves, and how pumps operate at different flows depending on the system.
Basics Fundamentals and working Principle of Centrifugal Pump.SHASHI BHUSHAN
Basics Fundamentals and working Principle of Centrifugal Pump. Centrifugal pumps are the rotodynamic machines that convert mechanical energy of shaft into kinetic and pressure energy of Fluid which may be used to raise the level of fluid. A centrifugal pump is named so, because the energy added by the impeller to the fluid is largely due to centrifugal effects.
Based on the information provided:
- Gage pressure (vacuum) = -20 inches of Hg
- Convert to psi: -20 inches Hg x 0.4912 psi/inch Hg = -9.824 psi
- Atmospheric pressure = 14.7 psi
- Liquid level above pump centerline is not provided
To calculate NPSHA:
- Atmospheric pressure (psi) converted to head = 14.7 psi x 2.31 ft/psi = 34 ft
- Gage pressure (vacuum, psi) converted to head = -9.824 psi x 2.31 ft/psi = -22.7 ft
- Static head = Unknown (not provided)
Centrifugal pumps work by using an impeller to increase the pressure and flow of a liquid. Liquid enters the center of the impeller and is accelerated outward by the curved blades of the impeller. This increases the pressure and flow of the liquid. Calculating the required head of a centrifugal pump involves accounting for static head, pipe friction losses, and adding additional head for safety. Proper pump selection is based on matching the required head and flow rate to the pump performance curves. Cavitation and ensuring adequate Net Positive Suction Head (NPSH) are also important considerations for centrifugal pump operation.
Pumps are used to move liquids through piping systems and raise their pressure by applying energy transformations. There are three main reasons for raising liquid pressure: overcoming static elevation changes, friction losses, and meeting process pressure requirements. Pumps are classified as either kinetic (centrifugal) or positive displacement depending on how energy is added to the liquid. Proper pump selection depends on factors like flow rate and viscosity. Cavitation can occur if the net positive suction head (NPSH) available falls below what is required by the pump.
This document discusses pumps, including their function, principle of operation, types, selection criteria, and engineering design process. The main types of pumps covered are centrifugal pumps and positive displacement pumps. Key factors in pump selection include the nature of the fluid being pumped, system requirements, environmental conditions, and cost. Pump performance is characterized using curves showing head, flow rate, and efficiency. Proper pump sizing and installation are important to avoid issues like cavitation.
1. The document presents information on centrifugal and reciprocating pumps, including their basic workings, components, uses, and efficiencies.
2. Centrifugal pumps use centrifugal force to accelerate and move fluid outwards from the center to increase pressure, while reciprocating pumps use pistons or plungers that move back and forth to displace fluid.
3. Key components of centrifugal pumps include casings, impellers, while reciprocating pumps have cylinders, pistons, valves. Both are used widely for irrigation, industry, buildings and other purposes.
This document provides information on various types of pumps, with a focus on centrifugal pumps. It defines different types of pumps and discusses why centrifugal pumps are commonly used. It then provides details on the components and operating principles of centrifugal pumps. The document also discusses pump performance curves, cavitation, net positive suction head (NPSH), affinity laws, and best practices for pumping systems.
Basics Fundamentals and working Principle of Centrifugal Pump.SHASHI BHUSHAN
Basics Fundamentals and working Principle of Centrifugal Pump. Centrifugal pumps are the rotodynamic machines that convert mechanical energy of shaft into kinetic and pressure energy of Fluid which may be used to raise the level of fluid. A centrifugal pump is named so, because the energy added by the impeller to the fluid is largely due to centrifugal effects.
Based on the information provided:
- Gage pressure (vacuum) = -20 inches of Hg
- Convert to psi: -20 inches Hg x 0.4912 psi/inch Hg = -9.824 psi
- Atmospheric pressure = 14.7 psi
- Liquid level above pump centerline is not provided
To calculate NPSHA:
- Atmospheric pressure (psi) converted to head = 14.7 psi x 2.31 ft/psi = 34 ft
- Gage pressure (vacuum, psi) converted to head = -9.824 psi x 2.31 ft/psi = -22.7 ft
- Static head = Unknown (not provided)
Centrifugal pumps work by using an impeller to increase the pressure and flow of a liquid. Liquid enters the center of the impeller and is accelerated outward by the curved blades of the impeller. This increases the pressure and flow of the liquid. Calculating the required head of a centrifugal pump involves accounting for static head, pipe friction losses, and adding additional head for safety. Proper pump selection is based on matching the required head and flow rate to the pump performance curves. Cavitation and ensuring adequate Net Positive Suction Head (NPSH) are also important considerations for centrifugal pump operation.
Pumps are used to move liquids through piping systems and raise their pressure by applying energy transformations. There are three main reasons for raising liquid pressure: overcoming static elevation changes, friction losses, and meeting process pressure requirements. Pumps are classified as either kinetic (centrifugal) or positive displacement depending on how energy is added to the liquid. Proper pump selection depends on factors like flow rate and viscosity. Cavitation can occur if the net positive suction head (NPSH) available falls below what is required by the pump.
This document discusses pumps, including their function, principle of operation, types, selection criteria, and engineering design process. The main types of pumps covered are centrifugal pumps and positive displacement pumps. Key factors in pump selection include the nature of the fluid being pumped, system requirements, environmental conditions, and cost. Pump performance is characterized using curves showing head, flow rate, and efficiency. Proper pump sizing and installation are important to avoid issues like cavitation.
1. The document presents information on centrifugal and reciprocating pumps, including their basic workings, components, uses, and efficiencies.
2. Centrifugal pumps use centrifugal force to accelerate and move fluid outwards from the center to increase pressure, while reciprocating pumps use pistons or plungers that move back and forth to displace fluid.
3. Key components of centrifugal pumps include casings, impellers, while reciprocating pumps have cylinders, pistons, valves. Both are used widely for irrigation, industry, buildings and other purposes.
This document provides information on various types of pumps, with a focus on centrifugal pumps. It defines different types of pumps and discusses why centrifugal pumps are commonly used. It then provides details on the components and operating principles of centrifugal pumps. The document also discusses pump performance curves, cavitation, net positive suction head (NPSH), affinity laws, and best practices for pumping systems.
T3b - MASTER - Pump flow system - operating point 2023.pptxKeith Vaugh
This document provides information about analyzing a centrifugal pump system, including:
1) The system includes a pump that transfers water from a sump through pipes to a tank, with the goal of developing expressions for pressure at the pump and head required.
2) Governing equations are presented for steady, incompressible flow including the energy equation and equations for head loss.
3) Steps are shown to develop the expressions for total pressure at the pump eye and required head at the pump based on the system dimensions and flow properties.
4) Additional information is provided on cavitation and losses that should be considered in the analysis.
Reciprocating pumps are positive displacement pumps suitable for high heads and low flows. They deliver a pulsed flow that can be smoothed out with accumulators. A reciprocating pump consists of a piston inside a cylinder that moves back and forth, driven by a crankshaft, to draw fluid in through a suction valve and push it out a discharge valve. They are more suitable than centrifugal pumps for high heads, small discharges, and viscous liquids, but require more maintenance due to moving parts. Common applications include oil and gas production, pipelines, refineries, and chemical processing where high pressures are needed.
Centrifugal pumps impart velocity energy to fluid using a rotating impeller, converting it to pressure energy. Positive displacement pumps physically move a fixed volume of fluid using movable boundaries. The main types are centrifugal, reciprocating, and rotary pumps. Centrifugal pumps are best for medium/high flows at low/medium pressures while reciprocating pumps work well for low flows at high pressures. Pump performance is represented through curves showing relationships between flow rate, pressure, and efficiency. Cavitation can damage pumps and occurs when local pressure drops below vapor pressure as bubbles form and violently collapse.
Centrifugal pumps impart velocity energy to fluid using a rotating impeller, converting it to pressure energy. Positive displacement pumps physically move a fixed volume of fluid using movable boundaries. The main types are centrifugal, reciprocating, and rotary pumps. Centrifugal pumps are best for medium/high flows at low/medium pressures while reciprocating pumps work well for low flows at high pressures. Pump performance is represented through curves showing relationships between flow rate, pressure, and efficiency. Cavitation can damage pumps and occurs when local pressure drops below vapor pressure as bubbles form and violently collapse.
Centrifugal pumps impart velocity energy to fluid using a rotating impeller, converting it to pressure energy. Positive displacement pumps physically move a fixed volume of fluid using movable boundaries. The main types are centrifugal, reciprocating, and rotary pumps. Centrifugal pumps are best for medium/high flows at low/medium pressures while reciprocating pumps work well for low flows at high pressures. Pump performance is represented through curves showing relationships between flow rate, pressure, and efficiency. Cavitation can damage pumps and occurs when local pressure drops below vapor pressure as bubbles form and violently collapse.
This document provides an overview of basics of pumps. It defines what a pump is and discusses common pump components, classifications, performance characteristics such as flow rate and head, and curves. It also describes different types of pumps including dynamic pumps like centrifugal pumps, positive displacement pumps such as reciprocating and rotary pumps, and covers specific examples like piston pumps, gear pumps, and diaphragm pumps.
This document discusses different types of hydraulic pumps, including their basic operating principles and comparisons. It provides equations to calculate pump parameters such as theoretical flow rate, volumetric displacement, efficiency, and torque. For example, it defines that positive displacement pumps capture and transfer fixed amounts of fluid, while centrifugal pumps impart velocity to fluid to create pressure. Gear pump displacement can be calculated based on gear dimensions. Pump efficiency is affected by factors like leakage and viscosity.
The document discusses various topics related to pumps, including:
1. Types of rotary pumps like centrifugal and reciprocating pumps, along with their basic operation and characteristics.
2. Key aspects of pump performance like flow rate, head pressure, horsepower requirements, and efficiency. Affinity laws relating changes in speed and impeller size to performance are also covered.
3. Common problems with pumps like low flow, low pressure, excessive power usage, noise, and seal leakage. Potential causes and troubleshooting approaches are provided.
4. Maintenance considerations like inspecting wear parts and monitoring operational parameters are emphasized to prevent problems and improve pump reliability.
The hydraulic machines which convert the mechanical energy into hydraulic energy are called pumps.”
“If the mechanical energy is converted into pressure energy or kinetic energy by means of centrifugal force
acting on the fluid, the hydraulic machine is called Centrifugal pump.”
Pumps convert mechanical energy to fluid energy and come in various types. The main types are positive displacement pumps, centrifugal pumps, axial flow pumps, and mixed flow pumps. Centrifugal pumps are frequently used in water distribution systems and work by spinning an impeller to push water outward. Axial flow pumps have flow entering and leaving along the pump axis. Multiple impellers can be arranged in series for higher head applications. Pump performance is characterized by curves showing how head and efficiency vary with flow. Total dynamic head and net positive suction head are important concepts for pump sizing and operation. Cavitation can occur if net positive suction head drops too low. Pumps can be arranged in series or parallel to meet different flow
Using a Hydraulic Ram to Pump Livestock Water - British Columbia
`
For more information, Please see websites below:
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Organic Edible Schoolyards & Gardening with Children =
http://scribd.com/doc/239851214 ~
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Double Food Production from your School Garden with Organic Tech =
http://scribd.com/doc/239851079 ~
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Free School Gardening Art Posters =
http://scribd.com/doc/239851159 ~
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Increase Food Production with Companion Planting in your School Garden =
http://scribd.com/doc/239851159 ~
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Healthy Foods Dramatically Improves Student Academic Success =
http://scribd.com/doc/239851348 ~
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http://scribd.com/doc/239850440 ~
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Huerto Ecológico, Tecnologías Sostenibles, Agricultura Organica
http://scribd.com/doc/239850233
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Simple Square Foot Gardening for Schools - Teacher Guide =
http://scribd.com/doc/239851110 ~
The document discusses centrifugal pumps, including their working mechanism, operation, advantages, and disadvantages. Centrifugal pumps use a rotating impeller to impart centrifugal force on liquid and increase pressure to pump water from a low point to a higher point. They are simple to operate but work best over a narrow range of conditions and cannot handle highly viscous liquids efficiently.
1. Centrifugal pumps are classified based on their specific speed, with radial flow pumps having a specific speed of 500-800, mixed flow pumps 800-1200, and propeller pumps 1200-3000.
2. A pump's performance is defined by its flow (Q) versus head (H) curve. The specific speed is a dimensionless number calculated from Q, H, and impeller RPM that relates to the pump type.
3. Pump power requirements are calculated using the pump affinity laws relating flow, head changes, and power with changes in impeller RPM. The water horsepower is calculated from flow and pressure increase and the brake horsepower accounts for pump efficiency.
The document discusses pumps and pumping systems. It begins by stating that pumps are the second most common industrial machine and are critical for plant operations. It then describes the typical components of a pumping system and different types of pumps. The document emphasizes that systems should be properly sized for efficiency and lists signs of an oversized system. It provides options for controlling flow without wasting energy, such as adjusting valves, impeller trimming, variable speed drives, and multiple pumps. Finally, it stresses the importance of considering total system efficiency and layout rather than just individual components.
Coconut water extraction mass production machineLuis Cabrera
Coconut water extraction mass production machine, design production line for 500,000 coconuts per day, including production lines, factory layout, utilities, CIP, waste water plant
Turbo machines are those mechanical devices which either extract energy from or impart energy to, a continuous moving stream of fluid. Pump is one of the most important and widely used turbo machines which basically impart energy to a moving fluid. Mechanical energy developed inside the pump is transferred to the moving fluid as hydraulic energy.
This document provides an overview of centrifugal pumps and reciprocating pumps. It defines key components of centrifugal pumps like impellers and casings, and describes how they work by imparting centrifugal force to increase fluid pressure. It also defines important pump parameters like head, efficiency, specific speed, and NPSH. Cavitation in pumps and methods to prevent it are explained. Performance curves for pumps are introduced. Finally, the working principle and equations for reciprocating pumps are outlined.
The document provides information about pumps, including their basic functions, main components, classifications, and examples of applications. It discusses how pumps work to increase the energy of liquids and move fluids through mechanical action. Pumps are classified as centrifugal or rotodynamic pumps, which use a rotating impeller to increase fluid velocity, and positive displacement pumps, which work by filling and emptying cavities. Examples of positive displacement pump types include reciprocating, power, and steam pumps. The document also outlines the basic working procedure of a centrifugal pump and provides diagrams to illustrate pump components and operation.
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Slides from talk presenting:
Aleš Zamuda: Presentation of IEEE Slovenia CIS (Computational Intelligence Society) Chapter and Networking.
Presentation at IcETRAN 2024 session:
"Inter-Society Networking Panel GRSS/MTT-S/CIS
Panel Session: Promoting Connection and Cooperation"
IEEE Slovenia GRSS
IEEE Serbia and Montenegro MTT-S
IEEE Slovenia CIS
11TH INTERNATIONAL CONFERENCE ON ELECTRICAL, ELECTRONIC AND COMPUTING ENGINEERING
3-6 June 2024, Niš, Serbia
T3b - MASTER - Pump flow system - operating point 2023.pptxKeith Vaugh
This document provides information about analyzing a centrifugal pump system, including:
1) The system includes a pump that transfers water from a sump through pipes to a tank, with the goal of developing expressions for pressure at the pump and head required.
2) Governing equations are presented for steady, incompressible flow including the energy equation and equations for head loss.
3) Steps are shown to develop the expressions for total pressure at the pump eye and required head at the pump based on the system dimensions and flow properties.
4) Additional information is provided on cavitation and losses that should be considered in the analysis.
Reciprocating pumps are positive displacement pumps suitable for high heads and low flows. They deliver a pulsed flow that can be smoothed out with accumulators. A reciprocating pump consists of a piston inside a cylinder that moves back and forth, driven by a crankshaft, to draw fluid in through a suction valve and push it out a discharge valve. They are more suitable than centrifugal pumps for high heads, small discharges, and viscous liquids, but require more maintenance due to moving parts. Common applications include oil and gas production, pipelines, refineries, and chemical processing where high pressures are needed.
Centrifugal pumps impart velocity energy to fluid using a rotating impeller, converting it to pressure energy. Positive displacement pumps physically move a fixed volume of fluid using movable boundaries. The main types are centrifugal, reciprocating, and rotary pumps. Centrifugal pumps are best for medium/high flows at low/medium pressures while reciprocating pumps work well for low flows at high pressures. Pump performance is represented through curves showing relationships between flow rate, pressure, and efficiency. Cavitation can damage pumps and occurs when local pressure drops below vapor pressure as bubbles form and violently collapse.
Centrifugal pumps impart velocity energy to fluid using a rotating impeller, converting it to pressure energy. Positive displacement pumps physically move a fixed volume of fluid using movable boundaries. The main types are centrifugal, reciprocating, and rotary pumps. Centrifugal pumps are best for medium/high flows at low/medium pressures while reciprocating pumps work well for low flows at high pressures. Pump performance is represented through curves showing relationships between flow rate, pressure, and efficiency. Cavitation can damage pumps and occurs when local pressure drops below vapor pressure as bubbles form and violently collapse.
Centrifugal pumps impart velocity energy to fluid using a rotating impeller, converting it to pressure energy. Positive displacement pumps physically move a fixed volume of fluid using movable boundaries. The main types are centrifugal, reciprocating, and rotary pumps. Centrifugal pumps are best for medium/high flows at low/medium pressures while reciprocating pumps work well for low flows at high pressures. Pump performance is represented through curves showing relationships between flow rate, pressure, and efficiency. Cavitation can damage pumps and occurs when local pressure drops below vapor pressure as bubbles form and violently collapse.
This document provides an overview of basics of pumps. It defines what a pump is and discusses common pump components, classifications, performance characteristics such as flow rate and head, and curves. It also describes different types of pumps including dynamic pumps like centrifugal pumps, positive displacement pumps such as reciprocating and rotary pumps, and covers specific examples like piston pumps, gear pumps, and diaphragm pumps.
This document discusses different types of hydraulic pumps, including their basic operating principles and comparisons. It provides equations to calculate pump parameters such as theoretical flow rate, volumetric displacement, efficiency, and torque. For example, it defines that positive displacement pumps capture and transfer fixed amounts of fluid, while centrifugal pumps impart velocity to fluid to create pressure. Gear pump displacement can be calculated based on gear dimensions. Pump efficiency is affected by factors like leakage and viscosity.
The document discusses various topics related to pumps, including:
1. Types of rotary pumps like centrifugal and reciprocating pumps, along with their basic operation and characteristics.
2. Key aspects of pump performance like flow rate, head pressure, horsepower requirements, and efficiency. Affinity laws relating changes in speed and impeller size to performance are also covered.
3. Common problems with pumps like low flow, low pressure, excessive power usage, noise, and seal leakage. Potential causes and troubleshooting approaches are provided.
4. Maintenance considerations like inspecting wear parts and monitoring operational parameters are emphasized to prevent problems and improve pump reliability.
The hydraulic machines which convert the mechanical energy into hydraulic energy are called pumps.”
“If the mechanical energy is converted into pressure energy or kinetic energy by means of centrifugal force
acting on the fluid, the hydraulic machine is called Centrifugal pump.”
Pumps convert mechanical energy to fluid energy and come in various types. The main types are positive displacement pumps, centrifugal pumps, axial flow pumps, and mixed flow pumps. Centrifugal pumps are frequently used in water distribution systems and work by spinning an impeller to push water outward. Axial flow pumps have flow entering and leaving along the pump axis. Multiple impellers can be arranged in series for higher head applications. Pump performance is characterized by curves showing how head and efficiency vary with flow. Total dynamic head and net positive suction head are important concepts for pump sizing and operation. Cavitation can occur if net positive suction head drops too low. Pumps can be arranged in series or parallel to meet different flow
Using a Hydraulic Ram to Pump Livestock Water - British Columbia
`
For more information, Please see websites below:
`
Organic Edible Schoolyards & Gardening with Children =
http://scribd.com/doc/239851214 ~
`
Double Food Production from your School Garden with Organic Tech =
http://scribd.com/doc/239851079 ~
`
Free School Gardening Art Posters =
http://scribd.com/doc/239851159 ~
`
Increase Food Production with Companion Planting in your School Garden =
http://scribd.com/doc/239851159 ~
`
Healthy Foods Dramatically Improves Student Academic Success =
http://scribd.com/doc/239851348 ~
`
City Chickens for your Organic School Garden =
http://scribd.com/doc/239850440 ~
`
Huerto Ecológico, Tecnologías Sostenibles, Agricultura Organica
http://scribd.com/doc/239850233
`
Simple Square Foot Gardening for Schools - Teacher Guide =
http://scribd.com/doc/239851110 ~
The document discusses centrifugal pumps, including their working mechanism, operation, advantages, and disadvantages. Centrifugal pumps use a rotating impeller to impart centrifugal force on liquid and increase pressure to pump water from a low point to a higher point. They are simple to operate but work best over a narrow range of conditions and cannot handle highly viscous liquids efficiently.
1. Centrifugal pumps are classified based on their specific speed, with radial flow pumps having a specific speed of 500-800, mixed flow pumps 800-1200, and propeller pumps 1200-3000.
2. A pump's performance is defined by its flow (Q) versus head (H) curve. The specific speed is a dimensionless number calculated from Q, H, and impeller RPM that relates to the pump type.
3. Pump power requirements are calculated using the pump affinity laws relating flow, head changes, and power with changes in impeller RPM. The water horsepower is calculated from flow and pressure increase and the brake horsepower accounts for pump efficiency.
The document discusses pumps and pumping systems. It begins by stating that pumps are the second most common industrial machine and are critical for plant operations. It then describes the typical components of a pumping system and different types of pumps. The document emphasizes that systems should be properly sized for efficiency and lists signs of an oversized system. It provides options for controlling flow without wasting energy, such as adjusting valves, impeller trimming, variable speed drives, and multiple pumps. Finally, it stresses the importance of considering total system efficiency and layout rather than just individual components.
Coconut water extraction mass production machineLuis Cabrera
Coconut water extraction mass production machine, design production line for 500,000 coconuts per day, including production lines, factory layout, utilities, CIP, waste water plant
Turbo machines are those mechanical devices which either extract energy from or impart energy to, a continuous moving stream of fluid. Pump is one of the most important and widely used turbo machines which basically impart energy to a moving fluid. Mechanical energy developed inside the pump is transferred to the moving fluid as hydraulic energy.
This document provides an overview of centrifugal pumps and reciprocating pumps. It defines key components of centrifugal pumps like impellers and casings, and describes how they work by imparting centrifugal force to increase fluid pressure. It also defines important pump parameters like head, efficiency, specific speed, and NPSH. Cavitation in pumps and methods to prevent it are explained. Performance curves for pumps are introduced. Finally, the working principle and equations for reciprocating pumps are outlined.
The document provides information about pumps, including their basic functions, main components, classifications, and examples of applications. It discusses how pumps work to increase the energy of liquids and move fluids through mechanical action. Pumps are classified as centrifugal or rotodynamic pumps, which use a rotating impeller to increase fluid velocity, and positive displacement pumps, which work by filling and emptying cavities. Examples of positive displacement pump types include reciprocating, power, and steam pumps. The document also outlines the basic working procedure of a centrifugal pump and provides diagrams to illustrate pump components and operation.
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Presentation of IEEE Slovenia CIS (Computational Intelligence Society) Chapte...University of Maribor
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Presentation at IcETRAN 2024 session:
"Inter-Society Networking Panel GRSS/MTT-S/CIS
Panel Session: Promoting Connection and Cooperation"
IEEE Slovenia GRSS
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2. Page 2
St Mkt, Irfan ul Haq
Pump training
KSB pump training at KSB Works
3rd April 2006
1. Hydraulic theory
2. “Ten ways to murder a pump”
3. Installation, commissioning, maintenance
3. Page 3
St Mkt, Irfan ul Haq
Pump training
1. Hydraulic theory
2. “Ten ways to murder a pump”
3. Installation, commissioning, maintenance
KSB pump training at KSB Works
3rd April 2006
5. Page 5
St Mkt, Irfan ul Haq
Pump hydraulics, impeller
inlet
outlet
rotation
6. Page 6
St Mkt, Irfan ul Haq
Pump hydraulics, main parts
A centrifugal pump consists of 4 main elements:
1 Impeller which rotates
The impeller has vanes which transfer
kinetic energy into the liquid pumped
2 Pump casing to convert kinetic energy
into potential energy and also contain
the liquid
3 Shaft to support the impeller
4 Generally a seal around the shaft to
contain the liquid
7. Page 7
St Mkt, Irfan ul Haq
Pump hydraulics, principles
A centrifugal pump:
Does not generate a vacuum, i.e. it cannot suck.
The impeller therefore has to be flooded in some way.
The flow and head developed are independent of the liquid
pumped, apart from effects of viscosity
Centrifugal Pumps deliver volumetric flow and head. All
curves are therefore expressed in m3/h and m (or equivalent
units)
Viscous liquids reduce the flow and head of the pump. More
later on this issue
1
2
3
4
E.g.: pump design 100 m3/h 102 m
on water sg 1.0 100.000 kg/h 10 Bar
on liquid sg 0.8 80.000 kg/h 8 Bar
8. Page 8
St Mkt, Irfan ul Haq
Pump hydraulics, head curve
0
10
20
30
40
50
60
70
80
90
100
0 20 40 60 80 100 120
flow
head
head
9. Page 9
St Mkt, Irfan ul Haq
Pump hydraulics, head + efficiency
0
10
20
30
40
50
60
70
80
90
100
0 20 40 60 80 100 120
flow
head
/
efficiency head
efficiency
Q
opt
Q opt is the point at which a pump has the highest efficiency, also
known as BEP (= best efficiency point)
10. Page 10
St Mkt, Irfan ul Haq
Pump hydraulics, head + efficiency
0
10
20
30
40
50
60
70
80
90
100
0 20 40 60 80 100 120
flow
head
/
efficiency
head
efficiency
Q
opt
Desirable operating range
Q min > 30% BEP Q max < 110% BEP
11. Page 11
St Mkt, Irfan ul Haq
Curve from book
Operating limits
Impeller diameters
Efficiencies
NPSH R
Power absorbed on water
12. Page 12
St Mkt, Irfan ul Haq
Pump hydraulics, system
Delivery head (pump system) consists of various parts
Static head on discharge side Hd
Friction loss on the discharge side
Pressure in system,
i.e. at the discharge vessel Pd
Friction loss on the suction side
Static head on suction side Hs
+
+
+
-
Hs
Hd
Pd
13. Page 13
St Mkt, Irfan ul Haq
Pump interaction with system
0
10
20
30
40
50
60
70
80
90
100
0 20 40 60 80 100 120
flow
head
/
efficiency
head
efficiency
system
Pump operates where pump and system curve intersect
14. Page 14
St Mkt, Irfan ul Haq
Pump hydraulics, system change
0
10
20
30
40
50
60
70
80
90
100
0 20 40 60 80 100 120
flow
head
/
efficiency
head
efficiency
system
system, lower friction losses
Note, with lower system curve, pump now delivers more flow
15. Page 15
St Mkt, Irfan ul Haq
Pump hydraulics, system change
0
10
20
30
40
50
60
70
80
90
100
0 20 40 60 80 100 120
flow
head
/
efficiency
head
efficiency
system
system, lower static
Note, with lower static curve, pump now delivers more flow
16. Page 16
St Mkt, Irfan ul Haq
Pump hydraulics, single operation
single inlet
single outlet
17. Page 17
St Mkt, Irfan ul Haq
Pump hydraulics, parallel operation
common
inlet
common
outlet
Valves etc. excluded for
clarity
18. Page 18
St Mkt, Irfan ul Haq
Pump hydraulics, pumps in parallel
0
10
20
30
40
50
60
0 10 20 30 40 50 60 70
flow
head
0
10
20
30
40
50
60
0 10 20 30 40 50 60 70
flow
head
+
0
10
20
30
40
50
60
0 20 40 60 80 100 120 140
flow
head
=
19. Page 19
St Mkt, Irfan ul Haq
Pump hydraulics, single + dual pump
0
10
20
30
40
50
60
70
80
90
100
0 20 40 60 80 100 120 140 160 180 200 220 240
flow
head
/
efficiency
head 1 pump
efficiency
system
head 2 pumps
Example
1 pump
running:
total flow =
120 m3/h
2 pumps
running:
total flow =
160 m3/h
flow per pump
= 80 m3/h
Note with 1 pump running, flow is more than 1/2 of 2 pumps running
20. Page 20
St Mkt, Irfan ul Haq
Pump hydraulics, Parallel operation
Issues to be considered:
Both pumps need to have similar shaped curves
Therefore check that:
power of motor is adequate
NPSH a is adequate for the larger flow
the pump flow does not exceed the design limits
typically Q < 125% Q opt 4pole
Q< 110% Q opt 2 pole
Flow per pump will always be lower than when operating on their
own.
21. Page 21
St Mkt, Irfan ul Haq
Pump hydraulics, series operation
single inlet
single outlet
22. Page 22
St Mkt, Irfan ul Haq
Pump hydraulics, pumps in series
0
10
20
30
40
50
60
0 10 20 30 40 50 60 70
flow
head
0
10
20
30
40
50
60
0 10 20 30 40 50 60 70
flow
head
+
0
20
40
60
80
100
120
0 10 20 30 40 50 60 70
flow
head
=
23. Page 23
St Mkt, Irfan ul Haq
Pump hydraulics, Cavitation
It’s this bubble collapse that causes the pump damage. This often sounds like
the pump is handling gravel. Continued cavitation will eventually destroy the
pump.
To avoid cavitation, the npsh a > npsh r of the pump
Cavitation is caused by vapour bubbles forming in the
pump.
A bubble is formed in the impeller at a point where the
‘local’ pressure is lower than the vapour pressure.
As the local pressure drops, more vapour bubbles
will form in the pump.
As the liquid flows further through the pump into a higher
pressure area the bubble collapses
26. Page 26
St Mkt, Irfan ul Haq
Pump hydraulics, NPSH available
NPSH available consists of various parts:
Static head on suction side
Velocity head in the pipework
This is normally ignored
Vapour pressure expressed in metres of
liquid, at the pumped temperature
+
+
-
NPSH stands for : net positive suction head
Friction losses in the suction line
-
Hs
Pe
V2/2g
Hvap
Hs
Absolute pressure expressed in metres of
liquid
Pe
NPSH available : npsh from the plant / system in which the pump operates
NPSH required : npsh that the pump needs to stop cavitation
27. Page 27
St Mkt, Irfan ul Haq
What does this mean?
So in practice this means: in the following example, we’ve ignored the
losses in the suction line
Pump with static suction head of + 5 m (Hs)
Drawing from an open tank + 10 m (Pe) atmospheric pressure is
roughly 10m with water
Handling water at 10 °C - 0.125m (Hvap) this equates to the vapour
pressure of water at 10 °C
However, contrast this with the same system at 90 Deg C:
Pump with static suction head of + 5 m (Hs)
Drawing from an open tank + 10 m (Pe) atmospheric pressure is
roughly 10m with water
Handling water at 90 °C - 7.41m (Hvap) this equates to the vapour
pressure of water at 90 °C
So NPSH available is 5 + 10 - 0.125 = 14.875 m
So NPSH available is 5 + 10 - 7.41 = 7.59 m
28. Page 28
St Mkt, Irfan ul Haq
Suction head not the same as NPSH
Therefore you can see from the previous slide that suction head is not
the same as NPSH.
The vapour pressure of the pumped liquid must be taken into account.
All pumps have an NPSH required curve. This is largely independent of
the pumped liquid, so the NPSH available and NPSH required need to
be compared to ensure that the pump will run properly.
The NPSH r curve of the pump generally indicates the value at which
the pump will cavitate. Therefore it’s important to have a margin
between the NPSH available and the NPSH required to prevent
cavitation.
29. Page 29
St Mkt, Irfan ul Haq
NPSH required
3% head drop
0% head drop
Note, when NPSH test is made, head drop is measured (3%)
31. Page 31
St Mkt, Irfan ul Haq
Pump hydraulics, NPSH required
0
10
20
30
40
50
60
70
80
90
100
0 2 4
NPSH
head
25% Qopt
100% Qopt
125% Qopt
A number of tests will be carried out to find
the NPSH r of a pump.
These are carried out by keeping the flow
constant and gradually reducing the NPSH
until the generated head drops.
NPSH r normally classed as the point when the head drops by 3% from the
‘non cavitating’ head
32. Page 32
St Mkt, Irfan ul Haq
Pump hydraulics, minimum flow
Why min flow?
Kettle: 2kW
Capacity: 1.5 l
Time to boil: 4.5 min
Pump
Power at Q=0: 8kW
Pump volume: 2.5 l
0
10
20
30
40
50
60
70
80
90
100
0 20 40 60 80 100 120
flow
head
/
power
head
power absorbed
Minimum permissible flow prevents pump from overheating
Min
flow
33. Page 33
St Mkt, Irfan ul Haq
Pump hydraulics, minimum flow
Other considerations for minimum flow:
Heat Temperature rise in the pump as losses in
the pump heat up the pumped liquid.
Pump curve Flat or unstable curve. At low flow there is
a risk of ‘hunting’
Radial loads These increase at low flow, shortening
bearing and seal life through increased shaft
deflection
NPSH req Generally increases at very low flow
Power On side channel pumps, power increases
as the flow reduces
Guideline Qmin > 15% of Q opt
34. Page 34
St Mkt, Irfan ul Haq
Pump hydraulics, speed changes
Affinity laws govern all centrifugal pumps:
Flow is proportional to Speed
Head is proportional to Speed 2
Power is proportional to Speed 3
This means for doubling the speed of a pump:
Pump speed 1450 rpm 2900 rpm
Flow 50 m3/h 100 m3/h
Head 50 m 200 m
Power 9 kW 72 kW
35. Page 35
St Mkt, Irfan ul Haq
Pump hydraulics,viscosity
0
20
40
60
80
100
120
140
0 20 40 60 80 100 120
flow
head
/
efficiency
head
viscous head
efficiency
viscous efficiency
viscosity correction factors fQ, fH, feta
36. Page 36
St Mkt, Irfan ul Haq
Pump hydraulics, casings
Diffuser + double volute
Volute
Circular Casing
Special Circular Volute
Flow Rate (Q)
BEP
Radial
Load
(F)
Double Volute
Single Volute
Diffuser
37. Page 37
St Mkt, Irfan ul Haq
Pump hydraulics, enquiry data
Capacity (Flow) m3/h l/s gpm
Pump head or diff. pressure m (bar) ft (psi)
Liquid including specific gravity
Temperature °C °F
Suction head or pressure bar psi
Materials of construction
Sealing requirements
Environment / area of use
Electrical supply V/phase/cycles
Factors for (hydraulic) pump selection:
38. Page 38
St Mkt, Irfan ul Haq
Pump hydraulics, wear ring clearances
Flow between
wear rings
Increased wear ring clearance reduces efficiency
39. Page 39
St Mkt, Irfan ul Haq
Pump hydraulics, specific speed
Radial Mixed flow Propeller
Note, units must be specified in quoting specific speed
increasing specific speed
1/2
speed x (flow )
3/4
(head)
specific speed =
40. Page 40
St Mkt, Irfan ul Haq
Pump hydraulics, suction recirculation
Suction recirculation
at low flow
1/2
speed x (flow )
3/4
(NPSH)
suction specific speed =
higher nss = lower NPSH r
but suction recirculation
more likely
41. Page 41
St Mkt, Irfan ul Haq
Pump hydraulics, Unstable curves
0
10
20
30
40
50
60
0 10 20 30 40 50 60 70
flow
head
head
The generated head does not fall continuously as the flow increases
42. Page 42
St Mkt, Irfan ul Haq
Unstable curves, “flat” system
0
10
20
30
40
50
60
0 10 20 30 40 50 60 70
flow
head
head
For a flat system curve, the pump could operate at one of two
flows, or hunt between the two
43. Page 43
St Mkt, Irfan ul Haq
Unstable pump curve, “steep” system
0
10
20
30
40
50
60
0 10 20 30 40 50 60 70
flow
head
head
system
For a steep system curve, the pump can still only operate at one flow
44. Page 44
St Mkt, Irfan ul Haq
Pump hydraulics, Speed change
For a steep system curve, the pump flow will change with speed
0
10
20
30
40
50
60
0 20 40 60 80
low speed
high speed
system
45. Page 45
St Mkt, Irfan ul Haq
Pump hydraulics, Speed change, flat curve
For a flatter system curve, at low speed the pump flow may be zero.
0
10
20
30
40
50
60
0 20 40 60 80
low speed
high speed
system