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![The amount of fluid power that a
system consumes is a product of head
and flow, according to this equation:
Fluid power = HQ (s.g.)
3,960
where
H = head (ft)
Q = flow rate (gallons per minute [gpm])
s.g. = specific gravity of the fluid
3,960 is a units conversion to state fluid
power in terms of horsepower
Initial Pump Selection
The operating point of centrifugal
pumps at which their efficiency is
highest is known as the best efficiency
point (BEP). Efficiencies range
widely, from 35% to more than 90%,
and they are a function of many
design characteristics](https://image.slidesharecdn.com/pumpinstallationmaintenance-240510030138-2495ceb5/75/Presentacion-Pump-Installation-_-Maintenance-pdf-41-2048.jpg)
Presentación Pump Installation _ Maintenance.pdf
- 1.
- 2. Course Objective identify pumpclassifications describe the purpose of pump parts. define various pump terms. explain pump operation. describe the components of a pump curve. Describe a simple pumping system. describe typical pump failures and their causes
- 3.
- 4. Purpose of apump: A pump is designed to: transfer fluid from one point to another. -from low pressure areas to higher pressure Areas. -from lower elevations to higher Elevations. -From local locations to distant locations. Pump Definition Pump is defined as a mechanical device that rotates or reciprocates to move fluid from one place to another Introduction
- 5. 41% 30% 24% 5% 20 Year LifeCycle Cost Chemical Process Pump Maintenance Operation Installation Purchase Life Cycle Cost Energy and maintenance costs during the life of a pump system are usually more than10 times its purchase price
- 6. Pumping System Basics Typicalpumping systems contain five basic components: Pumps. prime movers. Piping. Valves. end-use equipment.
- 7. Pumps are availablein a wide range of types, sizes, and materials, two categories described—positive displacement and centrifugal. positive displacement pumps have a fixed displacement volume. Consequently, the flow rates they generate are directly proportional to their speed. Centrifugal pumps have a variable flow/pressure relationship. Pumps Types
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- 9. Positive Displacement Pumps Positivedisplacement pumps work on the principle that – No two objects can occupy the same space at the same time A solid will displace a volume of fluid equal to its own volume Reciprocating element (piston – plunger) Rotating element (Vans , Screws or Gears)
- 10. Discharge flow /rate can be controlled by: - Change the speed of the prime mover. - Use of bypass lin. - Change of the piston stroke length. Types of Positive Displacement Pumps Reciprocating Pumps Rotary Pumps Positive Displacement Pumps
- 11. Three main types: -Piston Type. - Plunger Type. - Diaphragm Type. Reciprocating Pumps
- 12. Piston Type ReciprocatingPump Each complete movement of the piston along the length of the cylinder is called A STROKE Used as portable backup pumps for the removal of surplus process fluids
- 13. Very similar topiston type pumps and either vertical or horizontal acting Plunger Type Reciprocating Pump What is the difference between piston and plunger pumps?
- 14. Diaphragm Pump Get theirname from the flexible diaphragm
- 15.
- 16. A perfect seal,it makes Diaphragm Pump ideal for: 1- pumping chemicals. 2- Controlled metering. Diaphragm Pump A diaphragm is usually made of a flexible rubber materials often covered with a thin metal disc where the connecting rod is attached.
- 17. Rotary Pumps Types ofRotary Pumps -Gear Pump. -Sliding Vane Pump. -Rotary Lobe Pump. -Rotary Screw Pump.
- 18. Gear Pump /External consists of two intermeshing gears, one driven and one idling, in a close-fitting casing
- 19. Gear Pump /External
- 20. Gear Pump /Internal Internal gear pump has a small (driven) gear mounted eccentrically inside a larger idler gear that rotates inside a circular casing.
- 21. Vane Pump The commonvane type pump consists of a rotor with a radial slots machined into it. The rotor is mounted off-center and rotates inside a circular casing.
- 22. Vane Pump Liquid isdrawn in through the suction side and squeezed out under pressure through the discharge side.
- 23. Rotary Lobe Pump Therotary lobe pump works on a similar principle to the gear pump
- 24. Rotary Screw Pump Rotaryscrew pumps are special types of rotary positive displacement pumps in which the flow through the pumping elements is truly axial. Screw pumps are also called axial flow pumps
- 25. TYPES OF SCREWPUMPS Screw pumps can have one , two or three screws The types of screw pumps are the: Single Screw Pump Multiple Screw Pump
- 26. Single Screw Pumps Itconsists of a spiral-shaped rotor that turns in an internal- helix liner. The rotor is usually metal. The liner is rubber.
- 27. Multiple Screw Pumps Multiplescrew pump increases the pumping capacity of a single screw type by providing additional rotors to move fluid. Multiple screw pumps are driven by a single rotor called the power rotor. Two screw pumps are often called timed screw pumps
- 28.
- 29. Multiple Screw Pumps Three-screwpumps have two idler screws. The idlers are threaded to mesh with the power rotor. (untimed screw pumps)
- 30.
- 31. Centrifugal and axialpumps impart kinetic energy to a fluid and rely on the conversion of this kinetic energy to potential energy to increase fluid pressure Initial Pump Selection Centrifugal and axial pumps centrifugal pumps are used typically in high-flow, low-head applications in which fluid viscosity is not prohibitively high
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- 34. 1. Casing half,lower 2. Casing half, upper 3. Casing wear ring 4. Neck bush 5. Lantern ring 6. Stuffing gland 7. Bearing housing 8. Bearing cower I. 9. Bearing cover II. 10. Cooling cover 11. Shaft 12. Impeller 13. Impeller ring 14. Shaft protecting sleeve 15. Shaft nut 16. Lock nut 17. Labyrinth ring 18. Shoulder ring 19. Distance sleeve 20. Lubrication ring 21. Bearing pumps, typical sectional drawing
- 35. Pumps, typical sectionaldrawing
- 36. Axial-flow pumps with pull-outrotor and with blading adjustable during operation Initial Pump Selection Axial pumps
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- 38. 1. Suction cone 2.Suction bell 3. Wearing ring 4. Guide bearing casing 5. Guide vanes casing 6. Tube 7. Delivery elbow 8. Neck bush 9. Stuffing box 10. Thrust bearing casing 11. Thrust bearing cover 12. Motor stool 13. Cover 14. Shaft nut 15. Blade 16. Fixing plate 17. Impeller hub 18. Shaft sleeve 19. Shaft 20. Packing 21. Shaft sleeve 22. Oil retaining tube 23. Bearing bell 24. Coupling Vertical shaft
- 39. ADVANTAGES OF CENTRIGUGALPUMPS Advantages • Simple in construction and cheap • Handle liquid with large amounts of solids • No metal to metal fits • No valves involved in pump operation • Maintenance costs are lower Disadvantages Cannot handle highly viscous fluids efficiently Cannot be operated at high heads Maximum efficiency holds over a narrow range of conditions
- 40.
- 41. The amount offluid power that a system consumes is a product of head and flow, according to this equation: Fluid power = HQ (s.g.) 3,960 where H = head (ft) Q = flow rate (gallons per minute [gpm]) s.g. = specific gravity of the fluid 3,960 is a units conversion to state fluid power in terms of horsepower Initial Pump Selection The operating point of centrifugal pumps at which their efficiency is highest is known as the best efficiency point (BEP). Efficiencies range widely, from 35% to more than 90%, and they are a function of many design characteristics
- 42. Vapor pressure vs.temperature
- 43. Boiling water withlow pressure
- 44.
- 45. Specific gravity isthe density ratio of a liquid as compared to water at a given temperature. Water is used as the standard at 14.69 psia (1.013 bar abs) and at 60°F (15.5°C). Specific Gravity Its specific gravity is 1.0 at this standard temperature and pressure.
- 46. Static Head Initial PumpSelection
- 47.
- 48. is defined asthe minimum hydraulic head condition in which a pump can meet its head and capacity requirements without the liquid vaporizing inside the pump. Net Positive Suction Head (NPSH) Vaporization of the liquid causes cavitations. This cavitations reduces a pump’s performance and may damage the pump.
- 49.
- 50.
- 51. The standard testsfor NPSHR tell us that even if NPSHA equals NPSHR there still is still a mild incipient cavitation occurring. Therefore, we need a little safety margin. A good margin to use is: NPSHA > NPSHR +3 ft. (1m) This margin can vary with pump type, impeller type, and fluid being pumped. However for most Overhung Impeller Centrifugal Pumps the 3 ft (1m) safety margin is usually satisfactory. NPSH Available and NPSH Required
- 52.
- 54. Most pumps aredriven by electric motors. Although some pumps are driven by direct current (dc) motors, the low cost and high reliability of alternating current (ac) motors make them the most common type of pump prime mover. Prime Movers
- 55.
- 57. Piping Piping is usedto contain the fluid and carry it from the pump to the point of use. aspects of piping are its dimensions, material type, and cost. The flow resistance at a specified flow rate of a pipe decreases as the pipe diameter gets larger; however, larger pipes are heavier, take up more floor space, and cost more than smaller pipe.
- 58. In systems thatoperate at high pressures small-diameter pipes can have thinner walls than large- diameter pipes and are easier to route and install. Piping Small-diameter pipes restrict flow, can be especially problematic in systems with surging flow characteristics. Smaller pipes also operate at higher liquid velocity, increasing erosion effects, wear, and friction head. Increased friction head affects the energy required for pumping
- 59. Valves The flow ina pumping system may be controlled by valves. Some valves have: distinct positions. shut or open. throttle flow. selecting the correct valve for an application depends on: ease of maintenance. Reliability. leakage tendencies. Cost. frequency with which the valve will be open and shut.
- 60.
- 61. End-Use Equipment The essentialpurpose of a pumping system may be to provide cooling, to supply or drain a tank or reservoir, or to provide hydraulic power to a machine.
- 62.
- 63. Design Practices Fluid systemdesigns are usually developed to support the needs of other systems. In cooling system applications, the requirements flow is determine. Pump capabilities are then calculated based on the system layout and equipment characteristics The most challenging aspect of the design process is cost- effectively matching the pump and motor characteristics to the needs of the system
- 64. Analyzing System Requirements fullyunderstand system requirements (peak demand, average demand, and the variability of demand) with respect to time of day and time of year Problems with oversized pumps often develop because the system is designed for peak loads, while normal operating loads are much smaller. Excess flow energy is then forced into the system. In addition to increasing operating costs, this excess flow energy creates unnecessary wear on components such as valves, piping, and piping supports.
- 65. Initial Pump Selection Pumpselection starts with a basic knowledge of: System operating conditions. Fluid properties. Pressures. Temperatures. System layout. System Operating Costs. These conditions determine the type of pump that is required to meet certain service needs. positive displacement centrifugal. Axial flow pumps flow rate and head! efficiency suction inlet conditions operating life maintenance. Costs
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- 67.
- 68. 1. Serial number 2.Pump Model 3. Frequency 4. Rated Power 5. Speed 6. Maximum Head 7. Capacity 8. Head Range 9. Maximum Operating Pressure 10. Rotating Direction Pump nameplate information
- 69. 1-Check the pump/pumpunit immediately upon delivery/receipt of dispatch for damage or missing parts. 2-The pump/pump unit must be transported carefully and by competent personnel. Avoid serious impacts. 3-Keep the pump/pump unit in the same position in which it was supplied from the factory. 4-Take note of the instructions on the packaging. 5-The intake and discharge side of the pump must be closed with plugs during transport and storage Transport, Handling
- 70. Transport, Handling Dispose ofall packing materials in accordance with local regulations. 6-Lifting devices (e.g. fork-lift truck, crane, crane device, pulleys, sling ropes, etc.) must be sufficiently strong and must only be used by authorized persons. 7-The weight of the pump/pump unit is given in the Data Sheet. · 8-The pump/pump unit may only be lifted by solid points such as the casing, flanges or frame. 9-The following illustration shows the correct method of carrying by crane.
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- 72.
- 73. Transport, Handling Do notstand underneath suspended loads.
- 74. Pumps or pumpunits that are stored for a long time (6 months max) before use must be protected against moisture, vibrations and dirt (e.g. by wrapping in oil paper or plastic sheeting). Pumps must basically be stored in a place where they are protected from the weather, e.g. under cover. During this time, all suction and discharge branches and all other intakes and outlets must be closed with dummy flanges or plugs. Please contact factory for storage instructions for storage periods longer than 6 months Pumps Storage Cover the equipment with industrial strength plastic, preferably transparent to allow its visual inspection, including its nameplate, without uncovering the unit.
- 75. Drain the casingcompletely and dry it including : bearing housing . stuffing box. seal chamber. Apply a coat of soluble rust preventive solution both internally and externally Pumps Storage Remove the shaft coupling; it may cause the shaft to develop a permanent sag during prolonged storage. Store the unit in its normal position in a dry place. Protect the bearing housing from moisture by placing bags of vapor phase inhibitor crystals around the housing
- 76. Inspect the unitperiodically and turn the shaft a few times plus 1/4 turn. Turning the shaft prevents pitting of finished surfaces. The extra 1/4 turn is to displace the sag and prevent the shaft from developing a permanent bow. Pumps Storage
- 77. Mounting of pumponto a base frame Pumps Installation Installation and Alignment of Coupling Connecting the pipes to the pump Electrical connection Starting up Operation and Monitoring Shutting down
- 78. Pumps Installation Mounting ofpump onto a base frame The pump unit must be provided with a shared base frame made of steel or cast iron or a welded steel profile frame. This base frame must be placed on a foundation which can withstand all loads that arise during operation. following is to be noticed The base must withstand all loads occurring during operation. The mounting surfaces of the pump feet and motor on the base frame must be flat safe fastening Space between pump and motor depending on the used coupling
- 79. Pumps Installation Installation andAlignment of Coupling Make sure that nobody can start the motor during work on the coupling. Before starting installation coupling carefully clean shaft ends do not hit the coupling coupling may be heated before hand in an oil bath approx. 100°C Secure coupling hubs against axial sliding
- 80. Pumps Installation Installation andAlignment of Coupling The installation and alignment of the coupling must be carried out with the utmost care and attention. Badly aligned couplings cause noise. vibration . increased wear on bearings, couplings and shaft seals Mount coupling guard after alignment and before starting the unit.
- 81. Pumps Installation Connecting thepipes to the pump The pipes must be of a size and design that liquid can flow freely it is recommended that a check valve is installed in the discharge pipe shortly after the pump. Particular attention is to be paid to ensuring that suction pipes are air tight and that the NPSH values are observed. Do not install fittings or bends right before the suction nozzle. When laying the pipes, make sure that the pump is accessible for maintenance, installation and disassembly.
- 82. If the pipesystem is tested with the pump installed, do not exceed the maximum permitted casing pressure of the pump and/or shaft sealing. In the case of pumps with stuffing boxes, replace packing after pressure test Any sealing, flushing or cooling pipe connections must be installed Pumps Installation Connecting the pipes to the pump
- 83. This vent willprevent air binding problem during operation and facilitate proper filling and vent of the pump during startup. An additional flushed piping -– discharge branch-vent line – makes it easier to de- aerate the pump before start-up. Pumps Installation Connecting the pipes to the pump
- 84. Pumps Installation Connecting thepipes to the pump
- 85. Pumps Installation Electrical connection Electricalconnection work may only be carried out by an authorized professional Before starting work, check that the information on the motor rating. The power supply cable accordance with the wiring diagram. A protective motor switch is to be provided. The direction of rotation should only be checked when the pump is full. Dry running will cause damage to the pump.
- 86. Fixed Discharge System VariableDischarge System Tank TransferUnloading
- 87. Pumps Installation Starting up Theplant may only be started up by people who are familiar with the local safety regulations and with these Operating Instructions Starting up for the first time If pump is oil lubricated, first open oil drain and drain off any liquid that may have collected. Fill until the fluid level is at the mid of the oil level sight glass. For pumps with grease lubrication, no further lubrication is needed before initial start-up.
- 88. ·Pump and suctionpipe must be filled completely with liquid when starting up. ·Turn pump unit once again by hand and check that it moves smoothly and evenly. ·Check that coupling guard is installed and that all safety devices are operational. ·Switch on any sealing, flushing or cooling devices that are provided. ·Open isolation valve in suction /intake pipe. ·Set discharge side isolation valve to approx. 25% of rated flow quantity. With pumps with a discharge branch rated width less than 200, the isolation valve can remain closed when starting up ·Check direction of rotation by switching on and off briefly. It must be the same as the directional arrow on the bearing frame. ·Start drive device. ·As soon as it reaches normal operating speed, open discharge valve immediately and adjust the required operating point. Pumps Installation Starting up
- 89. During the firstfew hours of operation, slowly reduce the leakage rate as the pump is running by gradually tightening the packing gland. The guideline value is around 30 - 100 drops/minute Pumps Installation Starting up /Packing Packing that run dry will harden and then destroy the shaft sleeve and/or the shaft. If pump does not reach attended head or if atypical sounds or vibrations do occur: Switch off pump and seek for causes
- 90. Pumps Installation Starting up/Packing
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- 92.
- 93. • RUN-DRY • DEADHEADING • TEMPERATURE • ALIGNMENT • VIBRATION • PARTICULATE / ABRASIVES • CHEMICAL INCOMPATIBILITY MECHANICAL SEAL COMMON FAILURES
- 95.
- 96. Pumps Installation Operation andMonitoring suction pressure: Suction pressure is the actual pressure, positive or negative, at the pump suction connection as measured on a gauge. Pumps do not “suck” fluid as the pump suction
- 97. 25 % 50 % 75% 5,8kW 7,6 kW 9,2 kW 1,8 kW 3,2 kW 5,7 kW 4,0 kW 4,4 kW 3,5 kW 11.680 kWh 12.848 kWh 10.220 kWh 34.748 kWh year (2920 hours) saving per 1/3 saving in kW variable speed pumpat power consumption as per curve constant speed pumpat in % capacity Energy saving within 1 year (8.760 hours) Reduces Operating Cost
- 98. Constant Pressure • SprayNozzles • Decoking • Boiler Feed • Fire Suppression Constant Flow • Distillation Tower • Reactor Feed • Filter Supply • Pipe line System Curve • Pilot Plant • Heat Exchanger Feed Actuator Mode • Process Metering • TankSump Level Control • Tank Unloading Process Application
- 99. pump discharge? The pumpdischarge is the outlet or flange area where the fluid leaves the olute (casing). The discharge flange is usually oriented up (or vertically), but can also be mounted sideways (or horizontally) if the application requires it. Pumps Installation
- 100. Troubleshooting a SystemProblem Some pumping system problems are sufficiently expensive to justify a system assessment. Examples of these problems include inefficient operation, cavitations, poor flow control, and high maintenance Inefficient system operation can be caused by a number of problems as: improper pump selection. poor system design. excessive wear-ring clearances. wasteful flow control practices. Indications of inefficient system operation include: high energy costs. excessive noise in the pipes and across valves. high maintenance requirements Inefficient Operation.
- 101. Bearing Failures andTheir Causes
- 102. Bearing Failures andTheir Causes
- 103. Troubleshooting a SystemProblem
- 104. 6 month periodin a typical process plant C AUS E NUM B E R % o f T O T AL B earin g 25 10.50 B earin g h o u sin g 1 0.42 C ase w earin g rin g 2 0.84 Im p eller 8 3.36 Ro tatin g face 1 0.42 S crew s /set screw s 1 0.42 S eals - m ech an ical 179 75.21 S h aft 12 5.04 S leeve 9 3.78 T O T AL 238 100.00% PUMP FAILURE ANALYSIS
- 105. High Temp. Rise Head Head Flow Flow BEP BEP LowFlowCavitation DischargeRecirculation Reduced Impeller Life SuctionRecirculation Low Brg. & Seal Life Cavitation Low Brg. & Seal Life Results of Operating Off BEP
- 106. Shaft deflection isthe result of unbalanced radial loads. The amount of shaft deflection or bending depends on the amount of unbalance radial forces and a pump’s slenderness ratio. The higher the forces or the larger the slenderness ratio, the more shaft deflection will occur. Shaft deflection results in sealing device, bearing, and other pump mechanical failures. Shaft Deflection The Shaft Slenderness Ratio is a ratio of shaft length to shaft diameter. Shaft Slenderness Ratio
- 107.
- 108. SIMULTANEOUS DYNAMIC LOADSON PUMP SHAFT Impeller Axial Thrust Impeller Radial Thrust Hydraulically Induced Forces due to Recirculation & Cavitation Hydraulic Imbalance Seal Radial Thrust due to Impeller and Misalignment Axial Load from Misalignment and Impeller Radial Thrust due to Impeller and Misalignment Coupling Motor Shaft Deflection
- 109. TEMPERATURE RISE Overheating ofthe liquid in the casing can cause: • Rubbing or seizure from thermal expansion • Vaporization of the liquid and excessive vibration • Accelerated corrosive attack by certain chemicals Temperature rise per minute at shutoff is: T oF (oC) / min.= HP (KW)so x K Gal (m3) x S.G. x S.H. HPso = HP (KW) @ shutoff from curve Gal. (m3) = Liquid in casing S.G. = Specific gravity of fluid S.H. = Specific heat of fluid Ex.: Pump w/ 100HP (75KW) @s.o. , 6.8 gal casing (.03m3) w/ 60oF (16oC) water would reach boiling in 2 min. A recirculation line is a possible solution to the low flow or shut off operation problems....
- 110. CASING GROWTH DUETO HIGH TEMPERATURE T° F T° C INCHES MILLIMETERS EXPANSION 100 F 55 C 0.0097 IN 0.245 MM 200 F 110 C 0.0190 IN 0.490 MM 300 F 165 C 0.0291 IN 0.735 MM 400 F 220 C 0.0388 IN 0.900 MM 500 F 275 C 0.0485 IN 1.230 MM 600 F 330 C 0.0582 IN 1.470 MM 10 inches 250 mm ROTATION COEFFICIENT OF THERMAL EXPANSION FOR 316 S/S IS 9.7X10-6 IN/IN/°F OR 17.5 X10-6 MM/MM/°C CALCULATION IS T x 9.7 X10-6 X LENGTH IN INCHES T x 17.5X10-6 X LENGTH IN MILLIMETERS High temperature requires more clearance
- 111. PUMP GROWTH DUETO HIGH TEMPERATURE
- 112. IMPELLER BALANCE MECHANICAL -Weight offset from center of impeller - Balance by metal removal from vane HYDRAULIC - Vane in eye offset from impeller C/L - Variation in vane thickness - Results in uneven flow paths thru impeller - Investment cast impeller eliminates problem - Careful machining setup can help
- 116.