This document discusses cavitation in centrifugal pumps. It defines cavitation as the formation of vapor bubbles when liquid pressure drops below vapor pressure. Cavitation can cause damage, noise, vibration and efficiency losses in pumps. To avoid cavitation, the pump inlet pressure must exceed the net positive suction head required by the pump. Proper pump submergence, suction piping design and avoidance of air in the line can also prevent cavitation. Cavitation reduces pump head and efficiency according to the specific speed of the pump. Higher specific speed pumps are less susceptible to cavitation issues.
This document provides an overview of centrifugal pumps. It defines a pump and discusses the main components and classifications of centrifugal pumps. The key components of a centrifugal pump are the impeller, casing, suction pipe, and delivery pipe. Centrifugal pumps are classified based on impeller design and casing shape. The document also covers topics such as work done by the centrifugal pump, head of a pump, losses and efficiencies, and minimum speed for starting a centrifugal pump. Several example problems are provided to calculate values like inlet vane angle, work done, and minimum starting speed.
Pump Cavitation & Net Positive Suction HeadHasnaın Sheıkh
This document summarizes key concepts related to pump cavitation and net positive suction head (NPSH). It defines cavitation as the formation of vapor bubbles when local pressure inside a pump drops below the vapor pressure of the liquid. Repeated cavitation can damage impeller blades through pitting and erosion. NPSH is introduced to quantify the pressure required to avoid cavitation. NPSH available considers the inlet pressure accounting for piping losses, while NPSH required is provided by pump manufacturers as the minimum pressure needed. The document outlines how NPSH available and required values vary with flow rate and other variables like liquid temperature.
The document provides information about pumps, including:
1) Pumps are mechanical devices that use rotation or reciprocation to move fluid from one place to another by converting energy into hydraulic energy.
2) The main purposes of pumps are to transfer fluid from low to high pressure areas, from low to high elevations, and from local to distant locations.
3) There are two main types of pumps - positive displacement pumps which move a fixed volume of fluid with each cycle, and centrifugal pumps which use centrifugal force to move fluid by spinning an impeller.
The document discusses how centrifugal pumps work. It explains that fluid enters the impeller axially and is accelerated radially by centrifugal force, gaining pressure and velocity. The kinetic energy is partly converted to pressure energy in the volute casing. A centrifugal pump has a rotating impeller and stationary volute casing. Impellers can be open, semi-open, or enclosed, and pumps are classified by flow as radial, axial, or mixed. Multi-stage pumps contain multiple impellers to achieve higher pressures.
This document discusses pump selection and applications. It begins by outlining the chapter, which covers introductory concepts in pump selection, parameters to consider, types of pumps including positive displacement and kinetic pumps, and performance data for centrifugal pumps. The affinity laws relating speed, impeller diameter, capacity, head, and power for centrifugal pumps are also described. The chapter provides examples of pump performance curves and works through an example problem applying the affinity laws.
This document discusses cavitation in centrifugal pumps. It defines cavitation as the formation of vapor bubbles when liquid pressure drops below vapor pressure. Cavitation can cause damage, noise, vibration and efficiency losses in pumps. To avoid cavitation, the pump inlet pressure must exceed the net positive suction head required by the pump. Proper pump submergence, suction piping design and avoidance of air in the line can also prevent cavitation. Cavitation reduces pump head and efficiency according to the specific speed of the pump. Higher specific speed pumps are less susceptible to cavitation issues.
This document provides an overview of centrifugal pumps. It defines a pump and discusses the main components and classifications of centrifugal pumps. The key components of a centrifugal pump are the impeller, casing, suction pipe, and delivery pipe. Centrifugal pumps are classified based on impeller design and casing shape. The document also covers topics such as work done by the centrifugal pump, head of a pump, losses and efficiencies, and minimum speed for starting a centrifugal pump. Several example problems are provided to calculate values like inlet vane angle, work done, and minimum starting speed.
Pump Cavitation & Net Positive Suction HeadHasnaın Sheıkh
This document summarizes key concepts related to pump cavitation and net positive suction head (NPSH). It defines cavitation as the formation of vapor bubbles when local pressure inside a pump drops below the vapor pressure of the liquid. Repeated cavitation can damage impeller blades through pitting and erosion. NPSH is introduced to quantify the pressure required to avoid cavitation. NPSH available considers the inlet pressure accounting for piping losses, while NPSH required is provided by pump manufacturers as the minimum pressure needed. The document outlines how NPSH available and required values vary with flow rate and other variables like liquid temperature.
The document provides information about pumps, including:
1) Pumps are mechanical devices that use rotation or reciprocation to move fluid from one place to another by converting energy into hydraulic energy.
2) The main purposes of pumps are to transfer fluid from low to high pressure areas, from low to high elevations, and from local to distant locations.
3) There are two main types of pumps - positive displacement pumps which move a fixed volume of fluid with each cycle, and centrifugal pumps which use centrifugal force to move fluid by spinning an impeller.
The document discusses how centrifugal pumps work. It explains that fluid enters the impeller axially and is accelerated radially by centrifugal force, gaining pressure and velocity. The kinetic energy is partly converted to pressure energy in the volute casing. A centrifugal pump has a rotating impeller and stationary volute casing. Impellers can be open, semi-open, or enclosed, and pumps are classified by flow as radial, axial, or mixed. Multi-stage pumps contain multiple impellers to achieve higher pressures.
This document discusses pump selection and applications. It begins by outlining the chapter, which covers introductory concepts in pump selection, parameters to consider, types of pumps including positive displacement and kinetic pumps, and performance data for centrifugal pumps. The affinity laws relating speed, impeller diameter, capacity, head, and power for centrifugal pumps are also described. The chapter provides examples of pump performance curves and works through an example problem applying the affinity laws.
The document discusses nozzle thermodynamics. Some key points:
1. A nozzle is a duct with varying cross-sectional area used to accelerate fluid flow through a pressure drop. Common applications include jet engines, rockets, and flow measurement.
2. Nozzle shape is determined using the steady flow energy equation. For an ideal, frictionless case the process is isentropic. Area varies to maintain constant mass flow rate.
3. The throat is the minimum cross-sectional area point. Flow is sonic at the throat for designed operating conditions. Critical pressure ratio is when sonic velocity is first reached.
4. Nozzle performance is affected by operating above or below design back pressure. Maximum
Pumps are mechanical devices that use external power to transfer fluids from one point to another. There are two main types of pumps: positive displacement pumps and rotodynamic pumps. Positive displacement pumps include reciprocating pumps, rotary lobe pumps, progressing cavity pumps, piston/plunger pumps, dosing pumps, and vacuum pumps. Rotodynamic pumps include centrifugal pumps. Each pump type has different characteristics that make it suitable for various fluid transfer applications.
The document provides an introduction to pump analysis. It discusses that the purpose of a pump is to increase the mechanical energy in a fluid by transporting it from a lower elevation to a higher elevation. It then covers key pumping concepts like capacity, head, efficiency, and power input. Specific types of pumps are defined, including centrifugal pumps which are most commonly used for wastewater applications. Methods for analyzing pump performance including head-capacity curves and affinity laws are also introduced.
A pump is a mechanical device that transfers rotational energy to liquid to move it from one place to another. There are two main types of pumps: dynamic and positive displacement. A reciprocating pump is a type of positive displacement pump that uses a piston or plunger to trap and move liquid. A rotary pump also positively displaces liquid but does so continuously rather than reciprocating. A centrifugal pump is a type of dynamic pump that uses a rotating impeller to accelerate liquid and convert kinetic energy to pressure energy to move the liquid.
This Presentation is about working principle of Pumps.Basic Presentation regarding pumps , will definitely help beginners to learn pump types , their working , their parts etc.
This document discusses centrifugal pumps. It begins by defining pumps and their purpose of increasing fluid velocity, pressure, or elevation. It then classifies centrifugal pumps and describes their operation of converting motor energy into kinetic and potential energy of fluid flow using a rotating impeller. The key parts of centrifugal pumps are identified as the impeller, casing, suction pump, and discharge pump. The working principle is explained as fluid being accelerated outward by centrifugal force when the impeller rotates. Centrifugal pumps are commonly used for water supply, industry, and domestic applications due to their simplicity, low cost, and efficiency.
The document discusses different types of compressors used to increase air pressure. It describes reciprocating compressors which use pistons to compress air inside cylinders. Rotary compressors like screw, vane, and lobe compressors compress air using rotating elements. Centrifugal and axial compressors accelerate air to increase pressure, with centrifugal compressors using impellers and axial using rotating and stationary blades in stages. The document provides details on components and operating principles of these compressor types.
Pumps are used to deliver hydraulic fluid throughout a hydraulic circuit. There are two main types of pumps - positive displacement pumps and non-positive displacement pumps. Positive displacement pumps precisely regulate fluid output with each cycle, while non-positive displacement pumps like centrifugal pumps rely on fluid velocity to move fluid and output varies with pressure. Common positive displacement pump designs include gear pumps, vane pumps, and piston pumps which use rotating gears, vanes, or pistons to draw fluid in and push it out in fixed volumes. Selection of the appropriate pump type depends on factors like operating pressure, flow requirements, drive type, and tolerance to contamination.
Positive displacement pumps move fluids by trapping a fixed volume and forcing that volume from the suction to discharge side. Reciprocating pumps, like piston pumps, use reciprocating motion powered by engines while rotary pumps use rotating components like gears or lobes. Piston pumps have two check valves and a reciprocating piston powered by translating rotary motion into linear motion. They can be direct or indirect acting, simplex or duplex, and single or double acting. Diaphragm pumps use a flexible diaphragm instead of pistons. Rotary pumps have gears, lobes, screws, cams, or vanes that rotate to trap and move fluid and include gear, lobe, screw, vane, and cam pumps
When altitude increases, water's boiling point decreases as pressure drops. For every 27mmHg increase in pressure, boiling point rises 1°C. Water vaporizes based on temperature and pressure. NPSHa is the available positive suction head, calculated as total suction head minus vapor pressure. NPSHR is the required positive suction head to avoid cavitation. Cavitation can damage pumps when NPSHa is less than NPSHR. Engineers must ensure sufficient margin between liquid and vapor states.
1. The document discusses various topics related to hydraulic turbines including their classification, selection, design principles of Pelton, Francis and Kaplan turbines, draft tubes, surge tanks, governing, unit quantities, characteristic curves, similitude analysis and cavitation.
2. Hydraulic turbines are classified based on the type of energy at the inlet, direction of flow through the runner, head at the inlet, and specific speed. Pelton wheels are impulse turbines suitable for high heads while Francis and Kaplan turbines are reaction turbines for lower heads.
3. The design of each turbine type involves guidelines related to jet ratio, speed ratio, velocities, discharge, power and efficiency calculations. Characteristic curves show the performance of a
This project document describes the design, installation, and testing of a reciprocating pump. A team of engineering students constructed a demonstration pump facility under the guidance of Dr. Manoj Kumar Barai. The document outlines the objectives, classification, construction details, drawings, working principle, performance parameters, material selection, maintenance requirements, installation process, discharge calculations, characteristics, efficiencies, advantages, disadvantages, and applications of reciprocating pumps. References are provided at the end.
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.
This document provides an overview of reciprocating pumps. It begins by defining a reciprocating pump as a hydraulic machine that converts mechanical energy to hydraulic energy by sucking liquid into a cylinder using a reciprocating piston. It then covers the main parts of reciprocating pumps, classifications of piston and plunger pumps, the significance of air vessels, and provides examples of single and double acting pump working principles. The document also discusses discharge calculations, work done, power required and sources of slip. It concludes with advantages like high pressure delivery and disadvantages like high maintenance costs.
This document discusses laminar and turbulent fluid flow in pipes. It defines the Reynolds number and explains that laminar flow occurs at Re < 2000, transitional flow from 2000 to 4000, and turbulent flow over 4000. The entrance length for developing pipe flow profiles is discussed. Fully developed laminar and turbulent pipe flows are compared. Equations are provided for average velocity, shear stress at the wall, and pressure drop based on conservation of momentum and energy analyses. The Darcy friction factor is defined, and methods for calculating it for laminar and turbulent flows are explained, including the Moody chart. Types of pipe flow problems and accounting for minor losses and pipe networks are also summarized.
Pumps are devices that use mechanical energy to increase the velocity, pressure, or elevation of liquids and gases. There are two main types of pumps: positive displacement pumps and dynamic pumps. Positive displacement pumps apply direct pressure on a liquid using a reciprocating piston or rotating components. Dynamic pumps use centrifugal force to generate high rotational velocities and convert the kinetic energy of liquids into pressure energy. Common positive displacement pump types include piston pumps, plunger pumps, and diaphragm pumps. Common dynamic pump types include centrifugal pumps which contain an impeller and casing. Proper consideration of factors like net positive suction head are important for pump selection and operation.
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
Pumps, Types of Pumps, Classification of Pumps and Characteristics of Pumps.Talal Khan
This Presentation Discus Pumps(Centrifugal and Positive Displacement) Also it Discusses other properties of pumps.
It also consists of Images and animations of the Pumps.
Surging is associated with sudden drop in delivery pressure & with violent aerodynamic pulsation which is transmitted throughout the machine
the position is reached where no further increase in mass flow can be obtained no matter how wide open the control valve is ‐ CHOKING
The document discusses various topics related to continuous distillation processes including:
1) Material balance diagrams for continuous distillation columns and individual plates within the column. Different sections of the column like the rectifying and stripping sections are identified.
2) Common tray designs for distillation columns including bubble cap trays and sieve trays. Operation of these trays and factors influencing liquid-vapor contact are explained.
3) Operating parameters that can impact column performance are reviewed such as feed conditions, pressure drop across the column, flooding, weeping, entrainment, reboiler temperature control and vacuum maintenance. Column diameter is also noted as an important design factor.
The document discusses nozzle thermodynamics. Some key points:
1. A nozzle is a duct with varying cross-sectional area used to accelerate fluid flow through a pressure drop. Common applications include jet engines, rockets, and flow measurement.
2. Nozzle shape is determined using the steady flow energy equation. For an ideal, frictionless case the process is isentropic. Area varies to maintain constant mass flow rate.
3. The throat is the minimum cross-sectional area point. Flow is sonic at the throat for designed operating conditions. Critical pressure ratio is when sonic velocity is first reached.
4. Nozzle performance is affected by operating above or below design back pressure. Maximum
Pumps are mechanical devices that use external power to transfer fluids from one point to another. There are two main types of pumps: positive displacement pumps and rotodynamic pumps. Positive displacement pumps include reciprocating pumps, rotary lobe pumps, progressing cavity pumps, piston/plunger pumps, dosing pumps, and vacuum pumps. Rotodynamic pumps include centrifugal pumps. Each pump type has different characteristics that make it suitable for various fluid transfer applications.
The document provides an introduction to pump analysis. It discusses that the purpose of a pump is to increase the mechanical energy in a fluid by transporting it from a lower elevation to a higher elevation. It then covers key pumping concepts like capacity, head, efficiency, and power input. Specific types of pumps are defined, including centrifugal pumps which are most commonly used for wastewater applications. Methods for analyzing pump performance including head-capacity curves and affinity laws are also introduced.
A pump is a mechanical device that transfers rotational energy to liquid to move it from one place to another. There are two main types of pumps: dynamic and positive displacement. A reciprocating pump is a type of positive displacement pump that uses a piston or plunger to trap and move liquid. A rotary pump also positively displaces liquid but does so continuously rather than reciprocating. A centrifugal pump is a type of dynamic pump that uses a rotating impeller to accelerate liquid and convert kinetic energy to pressure energy to move the liquid.
This Presentation is about working principle of Pumps.Basic Presentation regarding pumps , will definitely help beginners to learn pump types , their working , their parts etc.
This document discusses centrifugal pumps. It begins by defining pumps and their purpose of increasing fluid velocity, pressure, or elevation. It then classifies centrifugal pumps and describes their operation of converting motor energy into kinetic and potential energy of fluid flow using a rotating impeller. The key parts of centrifugal pumps are identified as the impeller, casing, suction pump, and discharge pump. The working principle is explained as fluid being accelerated outward by centrifugal force when the impeller rotates. Centrifugal pumps are commonly used for water supply, industry, and domestic applications due to their simplicity, low cost, and efficiency.
The document discusses different types of compressors used to increase air pressure. It describes reciprocating compressors which use pistons to compress air inside cylinders. Rotary compressors like screw, vane, and lobe compressors compress air using rotating elements. Centrifugal and axial compressors accelerate air to increase pressure, with centrifugal compressors using impellers and axial using rotating and stationary blades in stages. The document provides details on components and operating principles of these compressor types.
Pumps are used to deliver hydraulic fluid throughout a hydraulic circuit. There are two main types of pumps - positive displacement pumps and non-positive displacement pumps. Positive displacement pumps precisely regulate fluid output with each cycle, while non-positive displacement pumps like centrifugal pumps rely on fluid velocity to move fluid and output varies with pressure. Common positive displacement pump designs include gear pumps, vane pumps, and piston pumps which use rotating gears, vanes, or pistons to draw fluid in and push it out in fixed volumes. Selection of the appropriate pump type depends on factors like operating pressure, flow requirements, drive type, and tolerance to contamination.
Positive displacement pumps move fluids by trapping a fixed volume and forcing that volume from the suction to discharge side. Reciprocating pumps, like piston pumps, use reciprocating motion powered by engines while rotary pumps use rotating components like gears or lobes. Piston pumps have two check valves and a reciprocating piston powered by translating rotary motion into linear motion. They can be direct or indirect acting, simplex or duplex, and single or double acting. Diaphragm pumps use a flexible diaphragm instead of pistons. Rotary pumps have gears, lobes, screws, cams, or vanes that rotate to trap and move fluid and include gear, lobe, screw, vane, and cam pumps
When altitude increases, water's boiling point decreases as pressure drops. For every 27mmHg increase in pressure, boiling point rises 1°C. Water vaporizes based on temperature and pressure. NPSHa is the available positive suction head, calculated as total suction head minus vapor pressure. NPSHR is the required positive suction head to avoid cavitation. Cavitation can damage pumps when NPSHa is less than NPSHR. Engineers must ensure sufficient margin between liquid and vapor states.
1. The document discusses various topics related to hydraulic turbines including their classification, selection, design principles of Pelton, Francis and Kaplan turbines, draft tubes, surge tanks, governing, unit quantities, characteristic curves, similitude analysis and cavitation.
2. Hydraulic turbines are classified based on the type of energy at the inlet, direction of flow through the runner, head at the inlet, and specific speed. Pelton wheels are impulse turbines suitable for high heads while Francis and Kaplan turbines are reaction turbines for lower heads.
3. The design of each turbine type involves guidelines related to jet ratio, speed ratio, velocities, discharge, power and efficiency calculations. Characteristic curves show the performance of a
This project document describes the design, installation, and testing of a reciprocating pump. A team of engineering students constructed a demonstration pump facility under the guidance of Dr. Manoj Kumar Barai. The document outlines the objectives, classification, construction details, drawings, working principle, performance parameters, material selection, maintenance requirements, installation process, discharge calculations, characteristics, efficiencies, advantages, disadvantages, and applications of reciprocating pumps. References are provided at the end.
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.
This document provides an overview of reciprocating pumps. It begins by defining a reciprocating pump as a hydraulic machine that converts mechanical energy to hydraulic energy by sucking liquid into a cylinder using a reciprocating piston. It then covers the main parts of reciprocating pumps, classifications of piston and plunger pumps, the significance of air vessels, and provides examples of single and double acting pump working principles. The document also discusses discharge calculations, work done, power required and sources of slip. It concludes with advantages like high pressure delivery and disadvantages like high maintenance costs.
This document discusses laminar and turbulent fluid flow in pipes. It defines the Reynolds number and explains that laminar flow occurs at Re < 2000, transitional flow from 2000 to 4000, and turbulent flow over 4000. The entrance length for developing pipe flow profiles is discussed. Fully developed laminar and turbulent pipe flows are compared. Equations are provided for average velocity, shear stress at the wall, and pressure drop based on conservation of momentum and energy analyses. The Darcy friction factor is defined, and methods for calculating it for laminar and turbulent flows are explained, including the Moody chart. Types of pipe flow problems and accounting for minor losses and pipe networks are also summarized.
Pumps are devices that use mechanical energy to increase the velocity, pressure, or elevation of liquids and gases. There are two main types of pumps: positive displacement pumps and dynamic pumps. Positive displacement pumps apply direct pressure on a liquid using a reciprocating piston or rotating components. Dynamic pumps use centrifugal force to generate high rotational velocities and convert the kinetic energy of liquids into pressure energy. Common positive displacement pump types include piston pumps, plunger pumps, and diaphragm pumps. Common dynamic pump types include centrifugal pumps which contain an impeller and casing. Proper consideration of factors like net positive suction head are important for pump selection and operation.
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
Pumps, Types of Pumps, Classification of Pumps and Characteristics of Pumps.Talal Khan
This Presentation Discus Pumps(Centrifugal and Positive Displacement) Also it Discusses other properties of pumps.
It also consists of Images and animations of the Pumps.
Surging is associated with sudden drop in delivery pressure & with violent aerodynamic pulsation which is transmitted throughout the machine
the position is reached where no further increase in mass flow can be obtained no matter how wide open the control valve is ‐ CHOKING
The document discusses various topics related to continuous distillation processes including:
1) Material balance diagrams for continuous distillation columns and individual plates within the column. Different sections of the column like the rectifying and stripping sections are identified.
2) Common tray designs for distillation columns including bubble cap trays and sieve trays. Operation of these trays and factors influencing liquid-vapor contact are explained.
3) Operating parameters that can impact column performance are reviewed such as feed conditions, pressure drop across the column, flooding, weeping, entrainment, reboiler temperature control and vacuum maintenance. Column diameter is also noted as an important design factor.
Hydrodynamic cavitation reactor theory.pptMuruganandam L
This document provides an introduction to cavitation for engineers, covering key topics in 3 lectures. It defines cavitation as a phase change from liquid to vapor due to low pressure, not temperature. The lectures cover: 1) cavitation inception due to pressure drops below vapor pressure per Bernoulli's equation, 2) types of cavitation patterns like attached and vortex cavities, 3) cavitation nuclei in the form of microbubbles, and 4) developed cavitation characterized by the cavitation number. Control valve and pump cavitation are discussed as practical examples. Diagrams illustrate concepts like pressure profiles and cavitation indices.
This document provides information about the boiler drum and its functions:
1. The boiler drum separates steam and water mixtures, stores water, and reduces dissolved solids in steam through blowdown. It contains internals like turbo separators and screen dryers for separation.
2. The drum connects to downcomers, risers, feed lines, and superheater lines. Auxiliary lines include blowdown, chemical dosing, and instrumentation.
3. Proper fitting and alignment of internals is important for efficient steam separation and prevention of impurity carryover into steam.
This document provides information on various types of pumps and piping systems. It describes the main types of pumps as centrifugal, rotary, reciprocating, and deep well pumps. It also discusses the classification and basic operating principles of centrifugal and reciprocating pumps. Additionally, it covers topics such as pipe sizes, fittings, valves, head losses, cavitation, affinity laws, and equations for calculating pump parameters.
The document discusses the design of horizontal kettle reboilers. It describes the different types of reboilers used in distillation columns, including forced circulation, thermosyphon, and kettle reboilers. It focuses on the design of horizontal kettle reboilers, explaining that boiling occurs on submerged tubes in a pool of liquid with no liquid circulation. The key factors in designing a horizontal kettle reboiler are selecting appropriate boiling heat transfer coefficients, ensuring the heat flux does not exceed the critical heat flux, sizing the tube bundle for adequate vapor disengagement, and maintaining a proper tube pitch and liquid level.
Instrumentation deals with measuring process variables like flow, pressure, temperature and level during operations. An instrument is a device that measures these variables. Common primary elements for flow measurement include orifice plates, venturi tubes and pitot tubes. Orifice plates come in different types like concentric, eccentric and segmental for different applications. Differential pressure transmitters are calibrated and their impulse lines are checked for proper filling and venting of air.
This document discusses fluid mechanics topics including airfoil theory, reciprocating pumps, indicator diagrams, and examples. It covers how airfoil shape affects lift to drag ratio, how reciprocating pump discharge is calculated, factors that cause slip in pumps, how pressure varies in pump sections and pipes due to piston acceleration, and examples calculating pump parameters and pressure heads on pistons.
The document discusses various flow measurement techniques used in instrumentation. It describes differential pressure flow meters including orifice plates, venturi tubes, and flow nozzles. It explains how these instruments work by creating a differential pressure through an obstruction in the flow that is measured to calculate flow rate. Key factors discussed include the relationship between flow rate and pressure drop, tapping locations, beta ratios, advantages and disadvantages of different designs, and applications of each type of differential pressure flow meter.
The document discusses condensers used in thermal power plants. It describes the functions of a condenser as condensing exhaust steam from turbines to be reused in the steam cycle, creating a vacuum to improve turbine efficiency, and removing non-condensable gases. Key aspects covered include the condenser's role in the Rankine cycle, operation, materials used for tubes, sources of air leakage, methods for detecting water leakage into tubes, and cleaning and testing of condenser tubes.
This document discusses control valves used in thermal power plants. It covers topics such as control valve sizing, construction, types including top-guided, cage-guided and double-seated valves. It also discusses trim, materials, cavitation prevention, leakage classification, fail-safe design, noise control, testing and standards. The document aims to provide an overview of key considerations for control valves used in critical applications in thermal power generation.
Flowmeters indicate the rate of gas flow and have an accuracy of ±2.5%. They contain a tapered tube, lightweight bobbin that floats based on gas flow, and scale. Only the correct tube and bobbin can be used for each gas. They require vertical orientation and cracks compromise function. Safety features include oxygen placement, antistatic materials, and stops. Proper care involves ensuring floats spin freely and flowmeters are monitored, maintained, and turned off during cylinder changes.
The document summarizes the components and functions of a Boyle's anesthesia machine. It describes the machine's low pressure system including flowmeters, vaporizers, and safety devices. Flowmeters measure gas flow and contain a bobbin indicator that rises based on the size of the annular orifice between it and the glass tube. Proper oxygen concentrations are maintained through proportioning systems that link oxygen and nitrous oxide flows. Outlet check valves and relief valves protect the system from back pressure issues.
This document discusses several topics related to fluid mechanics including:
1. Airfoil theory explains how providing curvature to the bottom of a flat plate and a sharp edge at the end can increase the ratio of lift to drag force compared to a flat plate at an angle of attack.
2. Reciprocating pumps work by using the length and area of the piston stroke along with revolutions per minute to calculate discharge, with double acting pumps discharging twice as much water.
3. The difference between actual and theoretical discharge of a pump is known as slip, and pump performance is affected by factors like suction head, delivery head, and piston acceleration.
This document discusses several topics related to fluid mechanics including:
1. Airfoil theory explains how providing curvature to the bottom of a flat plate and a sharp edge at the end can increase the ratio of lift to drag force compared to a flat plate at an angle of attack.
2. Reciprocating pumps work by using the length and area of the piston stroke along with revolutions per minute to calculate discharge, with double acting pumps discharging twice as much water.
3. The difference between actual and theoretical discharge of a pump is known as slip, and pump performance is affected by factors like suction head, delivery head, and piston acceleration.
Low pressure system in anaesthesia machineSwadheen Rout
This document provides information about Boyle's anesthesia machine. It discusses the components and functions of an anesthesia machine, including the pneumatic and electrical systems. It describes the different parts of the machine like the flowmeters, vaporizers, check valves, and safety features. The document explains how flowmeters work using the Hagen-Poiseuille equation and factors like viscosity, density, and laminar vs turbulent flow. It discusses temperature and pressure effects on flowmeters as well as protections against delivering a hypoxic gas mixture to the patient.
it speaks about the differential head flow meters. its different types. their principle of operation, venturi meter, orifice plate, rotameters, it also covers discussion on open channel flow meter. it covers the different application domains of the different types of flow meters and their advantages and disadvantages.
This document appears to be a lab manual for experiments in fluid mechanics. It includes objectives, outcomes, a list of 10 experiments, and details on several experiments including calibration of pressure gauges, determining friction factor in pipes, calibration of a venturi meter, and verifying Bernoulli's theorem. The experiments are mapped to course outcomes and involve determining coefficients, losses, flow rates, and verifying principles of fluid mechanics. Precautions, observations tables, and evaluation criteria are provided for selected experiments.
Download Link (Copy URL):
https://sites.google.com/view/varunpratapsingh/teaching-engagements
This PPT contained slides for Steam distribution system, which is a third unit in Energy Conservation subject of final year in Mechanical Engineering Branch.
The content of PPT are mentioned below:
Steam Distribution System, Thermodynamics, Heat, Properties of steam, steam, steam system, PDRS, Steam pipe installation, Dryers, Operation and maintenance of steam traps, Condensate Recovery System, Flash Recovery System, Energy Conservation Opportunity in Steam Distribution System.
We are all familiar with the production systems through which reservoir fluids flow to reach our processing facilities. This is a journey characterized by complex multiphase flow phenomena that govern pressure and temperature changes along the way. A monumental amount of research and development work has been invested towards better understanding multiphase flow behavior over the past fifty years. Yet, many challenges remain as we strive to optimize ever more complex production systems fraught with difficult flow assurance issues. Just how good is the science? And more importantly, how does this impact our bottom line? This lecture will discuss key concepts of multiphase flow leading to the current “state-of-the-art” models used today. Looking towards the future, the science must be advanced to address areas of greatest uncertainty and align with trends in field development strategies. Recommendations will be presented covering the top 5 areas of research necessary for these purposes. The economic impact of multiphase operations will be illustrated using two examples that provide insight towards maximizing asset value.
Mack Shippen is a Principal Engineer with Schlumberger in Houston, where he is responsible for the global business of the PIPESIM multiphase flow simulation software. He has extensive experience in well and network simulation studies, ranging from flow assurance to dynamic coupling of reservoir and surface simulation models. He has served on a number of SPE committees and chaired the SPE Reprint Series on Offshore Multiphase Production Operations. He holds BS and MS degrees in Petroleum Engineering from Texas A&M University, where his research focused on multiphase flow modelling.
An improved modulation technique suitable for a three level flying capacitor ...IJECEIAES
This research paper introduces an innovative modulation technique for controlling a 3-level flying capacitor multilevel inverter (FCMLI), aiming to streamline the modulation process in contrast to conventional methods. The proposed
simplified modulation technique paves the way for more straightforward and
efficient control of multilevel inverters, enabling their widespread adoption and
integration into modern power electronic systems. Through the amalgamation of
sinusoidal pulse width modulation (SPWM) with a high-frequency square wave
pulse, this controlling technique attains energy equilibrium across the coupling
capacitor. The modulation scheme incorporates a simplified switching pattern
and a decreased count of voltage references, thereby simplifying the control
algorithm.
Software Engineering and Project Management - Introduction, Modeling Concepts...Prakhyath Rai
Introduction, Modeling Concepts and Class Modeling: What is Object orientation? What is OO development? OO Themes; Evidence for usefulness of OO development; OO modeling history. Modeling
as Design technique: Modeling, abstraction, The Three models. Class Modeling: Object and Class Concept, Link and associations concepts, Generalization and Inheritance, A sample class model, Navigation of class models, and UML diagrams
Building the Analysis Models: Requirement Analysis, Analysis Model Approaches, Data modeling Concepts, Object Oriented Analysis, Scenario-Based Modeling, Flow-Oriented Modeling, class Based Modeling, Creating a Behavioral Model.
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Electric vehicle and photovoltaic advanced roles in enhancing the financial p...IJECEIAES
Climate change's impact on the planet forced the United Nations and governments to promote green energies and electric transportation. The deployments of photovoltaic (PV) and electric vehicle (EV) systems gained stronger momentum due to their numerous advantages over fossil fuel types. The advantages go beyond sustainability to reach financial support and stability. The work in this paper introduces the hybrid system between PV and EV to support industrial and commercial plants. This paper covers the theoretical framework of the proposed hybrid system including the required equation to complete the cost analysis when PV and EV are present. In addition, the proposed design diagram which sets the priorities and requirements of the system is presented. The proposed approach allows setup to advance their power stability, especially during power outages. The presented information supports researchers and plant owners to complete the necessary analysis while promoting the deployment of clean energy. The result of a case study that represents a dairy milk farmer supports the theoretical works and highlights its advanced benefits to existing plants. The short return on investment of the proposed approach supports the paper's novelty approach for the sustainable electrical system. In addition, the proposed system allows for an isolated power setup without the need for a transmission line which enhances the safety of the electrical network
Comparative analysis between traditional aquaponics and reconstructed aquapon...bijceesjournal
The aquaponic system of planting is a method that does not require soil usage. It is a method that only needs water, fish, lava rocks (a substitute for soil), and plants. Aquaponic systems are sustainable and environmentally friendly. Its use not only helps to plant in small spaces but also helps reduce artificial chemical use and minimizes excess water use, as aquaponics consumes 90% less water than soil-based gardening. The study applied a descriptive and experimental design to assess and compare conventional and reconstructed aquaponic methods for reproducing tomatoes. The researchers created an observation checklist to determine the significant factors of the study. The study aims to determine the significant difference between traditional aquaponics and reconstructed aquaponics systems propagating tomatoes in terms of height, weight, girth, and number of fruits. The reconstructed aquaponics system’s higher growth yield results in a much more nourished crop than the traditional aquaponics system. It is superior in its number of fruits, height, weight, and girth measurement. Moreover, the reconstructed aquaponics system is proven to eliminate all the hindrances present in the traditional aquaponics system, which are overcrowding of fish, algae growth, pest problems, contaminated water, and dead fish.
2. DEFINITION:
It is formation and subsequent collapse of vapor bubbles in the pump.
WHY IS THAT SO:
It is due to decrease in the pressure of liquid or increase in temperature in
different sections of pumps
TYPES OF CAVITATION:
1. VAPORIZATION CAVITATION:
2. RE-CIRCULATION CAVITATION
3. VANE PASSING SYNDROME CAVITATION
4. AIR ASPIRATION CAVITATION
5. TURBULENCE CAVITATION
3. 1-VAPORIZATION CAVITATION:
• Covers 70% of all cavitation (main part)
• Decrease in pressure
• Can be prohibited when
NPSH(A) is greater than NPSH(R) + 3 ft
2-RE-CIRCULATION CAVITATION:
• Due to low flow rate of fluid or in case of closed discharge conditions
• Continuously in contact with impeller vanes
• Fluid overheat due to resistance
• Can be prohibited by keeping discharge fully open.
3-VANE PASSING SYNDROME cavitation:
• Between the blade tip of OD of impeller and
cut water on the pump casing
• Temperature increases
• Free space should be 4% of impeller diameter
4. 4-Air aspiration:
• Due to involvement of air in pump
• Only in vacuum case
• Mostly in lift pumps
• Air enters through different joints, seals, shaft packings etc
• Could be resolved with tighten all flanges, packing rings etc
5-TURBULENCE CAVITATION:
• Due to formation of eddies.
• Eddied can be formed due to sharp elbows, restrictions, strainers, filters in the
suction
5. Disadvantages of cavitation:
1. Reduction in pressure at suction nozzle
2. Creates noise
3. Removal of metal in internal casing
4. Increase in velocity
5. Increase in temperature
6. Reduced efficiency
7. Undesirable flow conditions
Solution:
There are two basic solution to solved these problems:
By increasing the external pressure:
• Increasing the pressure at the pump suction
• Reducing the energy losses at the entrance to the pump
• Using a larger pump
By decreasing the vapor pressure:
• Changing to a fluid of lower vapor pressure