This document contains lecture notes and examples on fluid mechanics and reciprocating pumps. It discusses concepts like pressure head on pistons at different points in the suction and delivery strokes, manometric efficiency, specific speed of centrifugal pumps, and examples calculating pressure and power requirements for various pump configurations. It also contains problems asking the reader to calculate values like pump discharge, head, power requirements, impeller diameters, number of stages, and pressure heads on pistons.
PLEASE NOTE THIS IS PART-1
By Referring or said Learning This Presentation You Can Clear Your Basics Fundamental Doubts about Fluid Mechanics. In this Presentation You Will Learn about Fluid Pressure, Pressure at Point, Pascal's Law, Types Of Pressure and Pressure Measurements.
PLEASE NOTE THIS IS PART-1
By Referring or said Learning This Presentation You Can Clear Your Basics Fundamental Doubts about Fluid Mechanics. In this Presentation You Will Learn about Fluid Pressure, Pressure at Point, Pascal's Law, Types Of Pressure and Pressure Measurements.
Governing of the Turbine | Fluid MechanicsSatish Taji
Watch Video of this presentation on Link: https://youtu.be/LmJtNo-zgjo
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For Video, Visit our YouTube Channel (link is given below).
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Minor losses are a major part in calculating the flow, pressure, or energy reduction in piping systems. Liquid moving through pipes carries momentum and energy due to the forces acting upon it such as pressure and gravity. Just as certain aspects of the system can increase the fluids energy, there are components of the system that act against the fluid and reduce its energy, velocity, or momentum. Friction and minor losses in pipes are major contributing factors.
Governing of the Turbine | Fluid MechanicsSatish Taji
Watch Video of this presentation on Link: https://youtu.be/LmJtNo-zgjo
For notes/articles, Visit my blog (link is given below).
For Video, Visit our YouTube Channel (link is given below).
Any Suggestions/doubts/reactions, please leave in the comment box.
Follow Us on
YouTube: https://www.youtube.com/channel/UCVPftVoKZoIxVH_gh09bMkw/
Blog: https://e-gyaankosh.blogspot.com/
Facebook: https://www.facebook.com/egyaankosh/
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.
Hydraulic Intensifier ( Pressure raising device ) Umar Saeed
Through this presentation you will know about the how Hydraulic Intensifier works, its working principle and its components. This presentation also covers its animation through which you easily understand its function.
Minor losses are a major part in calculating the flow, pressure, or energy reduction in piping systems. Liquid moving through pipes carries momentum and energy due to the forces acting upon it such as pressure and gravity. Just as certain aspects of the system can increase the fluids energy, there are components of the system that act against the fluid and reduce its energy, velocity, or momentum. Friction and minor losses in pipes are major contributing factors.
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2. Example 4
• A single acting reciprocating pump has a stroke of length
150 mm. The suction pipe is 7.5 meters long and the
ratio of plunger diameter to the suction diameter is 4/3.
The water level in the pump is 2.5 meters below the axis
of the pump cylinder, and the pipe connecting the sump
and pump cylinder is 75 mm diameter. If the crank is
running at 75 r.p.m. Find the pressure head on the piston
• In the begining of the suction stroke.
• In the middle of the suction stroke.
• In the end of the suction stroke.
• Take coefficient of friction as 0.01.
3. Example 5
• A double acting reciprocating pump has a
cylinder of 200 mm diameter and stroke of 400
mm. The pump delivers water toa height of 10
meters through a pipe 36 meters long and 150
mm diameter at 40 r.p.m. Find the pressure in
the cylinder at the begining of the delivery
stroke, if a large air vessel is fitted in the delivery
pipe at the same level of the pump, but 3 meters
from the cylinder. Take coefficient of friction to
be 0.008.
4. Separation In Reciprocating Pump
When the vacuum pressure head reaches
-7.8 meters of water or 2.5 meters absolute
the continuity of flow will stop and
separation takes place.
This phenomenon occurs in suction and
delivery pipes of reciprocating pumps.
The speed at which separation may takes
place can be increase by fitting an air
vessel.
5. Example 6
• A single acting reciprocating pump is to raise a liquid of
11.8 kN/m3 through a verticle height of 11.5 meters
from 2.5 meters below the pump axis and 9 meters
above it. The plunger which moves with S.H.M has
diameter 125 mm and stroke 225 mm. The suction and
delivery pipes are 75 mm diameter and 3.5 meters and
13.5 meters long respectively. There is a large air
vessel placed on the delivery pipe near the pump axis.
But there is no air vessel on the suction pipe. If
separation takes place at 90 kPa below atmospheric
pressure. Find
a Maximum speed with which the pump can run without
separation taking place and
b Power required to drive the pump if f=0.02.
6. Manometeric Efficiency
• It is the ratio of manometric head to the
energy supplied by the impeller/kN of
water.
7. Specific Speed of a centrifugal
Pump
• The speed of the imaginary pump,
identical with the given pump which will
discharge one litre per second of water
while it is being raised through a head of
one meter.
8. Example 7
• A single stage centrifugal pump with
impeller diameter of 300 mm rorates at
2000 r.p.m and lifts 3 m3 of water per
minute to a height of 30 meters. Find the
number of stages and the diameter of
each impeller of a similar multistage pump
to lift 4.5 m3 of water per minute to a
height of 130 m when rotating at 1500
r.p.m.
9. Problem 1
• A centrifugal pump delivers 30 litres of
water per second against a head of 12
meters and runninng at 1200 r.p.m.
requires 6 kW power. Determine the
discharge, head of teh pump and power
required, if the pump runs at 1500 r.p.m.
10. Problem 2
• A centrifugal pump was built to supply
water against a head of 22.5 mters. But
later on it was required to supply the
required quantity of water against a head
of 20 meters. Find teh necessary
reduction in the impeller diamter, if it
planned to reduce the original diameter of
300 mm without reducing the speed of
impeller.
11. Problem 3
• Find the specific speed of a centrifula
pump, delivering 750 litres of water per
second against a head of 15 meters at
725 r.p.m.
12. Problem 4
• A multistage centrifugal pump is required
to lift 9000 litres of water per minute from
a mine, the total head including friction
being 75 meters. If the speed of the pump
is 1200 r.p.m. Find the least number of
stages, if teh specific speed per stage is
not to be less than 60 r.p.m.
13. Problem 5
• A single acting reciprocating pump has
plunger of diameter 150 mm and stroke of
length 400 mm. It draws water fram a
depth of 4.5 m through a pipe 8 m long
and 80 mm diameter at 25 r.p.m. If the
atmospheric pressure head is 10.3 find the
pressure head on the piston at the
begining and end of the suciton stroke.
14. Problem 6
• A single acting reciprocating pump has plunger
of diameter 150 mm and stroke of 300 mm. The
lengths of suction and delivery pipes are 6.5 m
and 39 m respectively and both the pipes are of
teh same diameter of 75 mm. The axis of the
pump is 5 m above the level of the water in the
sump and 33 m below the delivery water level. If
the atmospheric pressure head is 10.3 m of
water and coefficient of friction of both pipes is
0.01. Find the pressure head of the piston at the
beginning, middle and end of the suction
strokes. Take speed of crank as 30 r.p.m.