Last Updated 08 Apr 2020

Performance And Specifications Of Power Pumps Engineering Essay

Category Performance
Essay type Research
Words 1848 (7 pages)
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The agencies of pumping is the most of import manner of fluid transportation for 1000s of old ages. Ancient Egyptians used water wheels with hoppers for the motion of vehicle marked with H2O for irrigation intent. In the 3rd century BC ; the Grecian scientist Stisebeos Alexandria invents the reciprocating pump to pump H2O. The about the same clip discovered the Grecian mathematician Archimedes the prison guard pump, called the composit of mandolins with a coiling traveling on inside the cylinder. Till that clip the there was no much development occurs until the late 17th century, where the Gallic adventurer Denis invent a pump with consecutive blades. Then the British adventurer John Oblad invents the centrifugal pump with curving blades in 1851. Thereafter, the first usage of compressors with axial-flow turbo jet engines where found in the mid-fortiess of the 20th century AD.

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Reciprocating Pump

Positive supplanting pumps are that type of machines which is common for applications that require a really high Pressures and comparatively low flow. In this machine, the liquid flows into a contained infinite, such as a cylinder, speculator, or rotor. Then a traveling Piston forces the liquid out of the cylinder, increasing the force per unit area. The usage of positive supplanting pumps is common in applications that require high discharge force per unit area and comparatively low flow. The discharge force per unit area generated by a positive supplanting pump is - in theory - space. If the pump is dead headed, the force per unit area generated will increase until either a pump portion fails or the driver stalls from deficiency of power.

The Reciprocating Pump - besides known as Power Pump- is one type from the Positive Displacement Pump. In his book, Pollak illustrates that the Reciprocating pump has a random-access memory, speculator, Piston or other cylindrical component working backwards and forwards within a cylinder or pump barrel ; this gesture is normally delivered from a grouch go arounding unvarying velocity, and linking rod. Automatic valve control the flow of liquid into the cylinder, and out once more. A Piston or a speculator moves back and Forth in an enclosed cylinder. A reciprocating pump besides has a power terminal and a liquid terminal. Most piston pumps are individual playing ; plunger pumps are dual moving. The diameter of the Piston, the length of the Piston shot and the speed of the

Walter pistons determine the pump capacity.

See fig

Power Pumps:

As mentioned by Igor Karassik in his book that the power pump does non develop force per unit area ; it merely produces a flow of fluid. The downstream procedure or shrieking system produces a opposition to this flow, thereby bring forthing force per unit area in the piping system and dispatch part of the pump. The flow fluctuates at a rate proportional to the pump velocity and figure of cylinders. The amplitude of the fluctuations is a map of the figure of cylinders. Karassik added that greater the figure of cylinders, the lower the amplitude of the flow fluctuations at a specific revolutions per minute.

It is ever possible for the power pump to bring forth different capacity as they are capable of operating over a broad scope of velocities. Each pump has maximum suction and discharge force per unit area limits that ; when combined with its maximal velocity, find the pump 's power evaluation. The pump can be applied to power conditions that are less than its maximal evaluation but at a little lessening in mechanical efficiency

Operating Principles:

In his paper, Samuel explains the pump operation as follows ; the reciprocating pump uses a crankshaft-connecting rod mechanism. The crankshaft-connecting rod mechanism converts the rotary motion of the crankshaft to a reciprocating additive motion of Pistons. The Piston motion creates volume alterations. As a pit opens when a Piston retracts, the fluid is admitted through an recess cheque valve. When the Piston reverses, the recess look into valve stopping points, and the pit reduces when the Piston extends. The mercantile establishment look into valve clears and the fluid is forced out by the Piston.

Despite that of the fluid being pumped, the discharge volume is fixed for each crankshaft revolution. Pressure is determined by the system flow opposition and pump building. The Speed decrease is so needed for diminishing high velocity from the driver to low pump shaft velocity.

Applications for Power pumps are:

• Oil well clay pumps

• Reverse osmosis charge pumps

• Auxiliary boiler provender pumps

• Pipeline pumps

• Oil field H2O injection pumps

• Slurry pumps

• Process pumps

Performance and specifications:

In his paper, David Parker negotiations about the specification illustrating that the quality and measure of information on suction conditions will find the ultimate success or failure of any pump installing. The bulk of pump jobs, start at the suction. There must be a minimal sum of absolute force per unit area available to provide fluid to the pump suction. PD pumps by and large require less absolute force per unit area. Net Positive Inlet Pressure Required ( NPIPR ) , at the pump suction rim, is the evaluation of entire recess losingss within that pump at rated conditions. Unit of measurements are force per unit area footings ; PSI, Kg/cm2, Bar, KPa. These losingss include the unstable clash loss along the internal suction way, the alteration in lift from the suction rim to the enclosed volume, the unstable clash loss of come ining the enclosed volume, and the acceleration to the speed of the enclosed volume. For any given size, NPIPR will increase with increased viscousness or flow ( increased flow = increased velocity ) . Volumes of gas are normally specified comparative to standard temperature and force per unit area ( STP ) of 680F and atmospheric force per unit area ; 14.7 psia ; 200C, 1.034 Kg/cm2 absolute. By stipulating the standard volume of gas and stipulating the suction force per unit area and temperature, the volume of gas nowadays at the pump suction can be calculated. This capacity must be added to the liquid capacity in order to size the pump for the needed liquid flow rate. If suction force per unit area is below atmospheric force per unit area, even little sums of entrained gas will spread out in volume necessitating a larger pump. Capacity should be defined for the rated status. If there is an acceptable scope of capacities, the lower limit and maximal acceptable should be stated. This allows pump providers to offer standard merchandises without holding to modify for specific capacity demands.


In the reciprocating pump, merely two efficiency losingss need to be considered ; volumetric and Mechanical.

Volumetric efficiency loss is provoked by slippage through valves, ratio of liquid chamber volume at terminal of shot to plunger/piston supplanting volume, and liquid squeezability.

Mechanical efficiency loss occurs while get the better ofing mechanical clash in bearing and velocity decrease.

The overall efficiency of a reciprocating pump unit is by and large above 85 % throughout its full operating scope. However, in the reciprocating pump can run over 90 % because many pumps and decrease units operate at a mechanical efficiency of 98 per centum, and the volumetric efficiency can frequently be above 95 per centum.


Viscosity of a fluid is the ratio of shear emphasis to the rate of shear strain. It is a step of its opposition to flux. High viscousness fluids, like gum elastic, adhesives, or molasses, are really immune to forces applied to travel them. Low viscousness fluids, like kerosine or H2O, have really small opposition to coerce. Viscosity is reduced as temperature is increased ; hot fluids flow more readily than cold fluids. Viscosity should ever be given at a specified temperature. Typical units for viscousness are centipoises, centistokes, and SSU. Positive Displacement pumps maintain high efficiencies throughout the viscousness scope. Entrained gasses can be handled in big measures by most Positive Displacement pump designs ; nevertheless care must be taken in stipulating measure of gas entrained and flow required.

Positive Displacement pumps are used to keep the changeless flow rate as nozzle force per unit areas change due to choke offing and gnawing. Precise control of fuel add-on rates increases the operators control over burning conditions. This in bend leads to cut down air emanations, a really critical concern in a extremely regulated industry.

The reciprocating pump provides a about changeless flow rate over a wider scope of force per unit area ; the centrifugal pump gives unvarying force per unit area over a scope of flow, so it drops dramatically as the flow rate additions. On a reciprocating pump, fluid viscousness has small consequence on the flow rate as the force per unit area increases. However, unstable viscousness has a large impact on the centrifugal pump 's force per unit area and flow rate. The efficiency besides drops well.


Efficiency is rather high even though there are alterations in the needed caput. It can be up to 85 % to 95 % or even more. Merely with high velocity it tends to diminish somewhat.

Reciprocating pumps run at much lower operating velocities than centrifugal pumps and therefore is better suited for managing viscose fluid.

For a given velocity the flow rate is changeless regardless of caput, the pump is limited merely by the power of the premier mover and the strength of the pump parts.

The fluid flow from the reciprocating pump is well high.

It is start automatically. No demand to make full the cylinders before get downing.


There are poorer in managing liquids incorporating solids that tend to eat valves and seats.

Because of the pulsating flow and force per unit area bead throw the valves they require larger suction force per unit area at the subdivision rim to avoid cavitations.

Due to mechanical quivers, the pulsating flow require a particular attending to subdivision and discharge piping design

Hovering gesture of the nozzle creates perturbations that travel at velocity of sound from the pump cylinder shrieking system. These perturbations cause the force per unit area degree of the system to fluctuate with regard to clip.

It is hard to pump syrupy liquid in the reciprocating pump

The cost of bring forthing Piston pumps is high. This is due to the really accurate sizes of the cylinders and Pistons. Besides, the geartrain needed to change over the rotary motion of the thrust motor into a reciprocating action involves excess equipment and cost.

Discharge flow problems:

Care cost a batch considered with its handiness, because throbing flow and big figure of traveling parts, as the atoms can acquire into the little clearances and cause terrible wear. The Piston pump therefore, should non be used for slurries.

The throbing features of the fluid fluxing into and out of power pumps are significantly affected by the figure of Pistons. Discharge flow pulsings are the most critical because of the high energy potency generated when the system opposition reacts with the flow to make force per unit area. Since the magnitude of the discharge pulsing is largely affected by the figure of cylinders, so we can get the better of the pulsing flow by increasing the figure of cylinders.

Besides, we can cut down the discontinuity by utilizing an collector at the terminal of the nose which will provides a continues flow.

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