the presentation includes basic ideas about water pumps, various terminology generally used for the pumps, classification of pumps and ideas about the types its construction and working
the presentation includes basic ideas about water pumps, various terminology generally used for the pumps, classification of pumps and ideas about the types its construction and working
Watch Video of this presentation on Link: https://youtu.be/xIGlZ3UvLdw
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.
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Hydraulics is a branch of science which deals with hydraulic fluid. It is used in places where cleanliness is not a priority but requires huge power to perform tasks.
application:
1. Industrial: Plastic processing machineries, steel making and primary metal extraction applications, automated production lines, machine tool industries, paper industries, loaders, crushes, textile machineries, R & D equipment and robotic systems etc.
2 Mobile hydraulics: Tractors, irrigation system, earthmoving equipment, material handling equipment, commercial vehicles, tunnel boring equipment, rail equipment, building and construction machineries and drilling rigs etc.
3 Automobiles: It is used in the systems like breaks, shock absorbers, steering system, wind shield, lift and cleaning etc.
4 Marine applications: It mostly covers ocean going vessels, fishing boats and navel equipment.
5 Aerospace equipment: There are equipment and systems used for rudder control, landing gear, breaks, flight control and transmission etc. which are used in airplanes, rockets and spaceships.
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.
Pumps come in a variety of sizes for a wide range of applications. They can be classified
according to their basic operating principle as dynamic or displacement pumps. Dynamic
pumps can be sub-classified as centrifugal and special effect pumps. Displacement pumps can
be sub-classified as rotary or reciprocating pumps.
Watch Video of this presentation on Link: https://youtu.be/xIGlZ3UvLdw
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/
Hydraulics is a branch of science which deals with hydraulic fluid. It is used in places where cleanliness is not a priority but requires huge power to perform tasks.
application:
1. Industrial: Plastic processing machineries, steel making and primary metal extraction applications, automated production lines, machine tool industries, paper industries, loaders, crushes, textile machineries, R & D equipment and robotic systems etc.
2 Mobile hydraulics: Tractors, irrigation system, earthmoving equipment, material handling equipment, commercial vehicles, tunnel boring equipment, rail equipment, building and construction machineries and drilling rigs etc.
3 Automobiles: It is used in the systems like breaks, shock absorbers, steering system, wind shield, lift and cleaning etc.
4 Marine applications: It mostly covers ocean going vessels, fishing boats and navel equipment.
5 Aerospace equipment: There are equipment and systems used for rudder control, landing gear, breaks, flight control and transmission etc. which are used in airplanes, rockets and spaceships.
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.
Pumps come in a variety of sizes for a wide range of applications. They can be classified
according to their basic operating principle as dynamic or displacement pumps. Dynamic
pumps can be sub-classified as centrifugal and special effect pumps. Displacement pumps can
be sub-classified as rotary or reciprocating pumps.
A regenerative turbine pump varies from the more familiar centrifugal pump mostly in the design of its impeller. This design difference makes the regenerative turbine pump uniquely suited for low NPSH (Net Positive Suction Head) applications, among others. Regenerative turbine pumps can safely pump liquids close to the boiling point without the detriment of cavitation, and the pump design is suitable for handling highly unstable liquids.
Southern Methodist UniversityBobby B. Lyle School of Engineeri.docxwhitneyleman54422
Southern Methodist University
Bobby B. Lyle School of Engineering
CEE 2342/ME 2342 Fluid Mechanics
Roger O. Dickey, Ph.D., P.E.
V. STEADY PIPE FLOW
D. Pump Selection
Reading Assignment:
Chapter 12 Turbomachines
Section 12.4 – The Centrifugal Pump, pp. 687-700
E. Pump Selection
Pump Applications –
Pumps are used in a wide array of engineering applications including:
Low-lift pumps high-volume, low-head pumps used to elevate fluids, e.g., elevating water from a supply source to a water treatment plant or wastewater from a gravity sewer to a wastewater treatment plant.
High-service pumps used to deliver fluids under “adequate” pressure throughout a distribution piping network, or through long transmission pipelines.
Booster pumps used to increase fluid pressure at intermediate points along transmission pipelines, or within distribution piping networks.
Recirculation and transfer pumps used to convey fluids for one unit operation or process to another within an engineered system or facility.
Well pumps used to lift water from ground water aquifers for water supply purposes.
Chemical metering pumps used to deliver reagent chemicals at precisely controlled rates to chemical processes.
Fire pumps used for delivering high flow rates at high pressures for firefighting.
Sludge pumps used to convey thick slurries from one unit operation or process to another within an engineered system or facility.
Sampling pumps used in both portable and fixed equipment designed to collect precise sample volumes over precise time intervals within engineered systems or facilities.
Pump Types -
Pumps can be broadly classified as either,
Dynamic
Positive displacement
Dynamic pumps deliver flow rates that vary as a function of the discharge head on the pump.
Conversely, positive displacement pumps deliver flow rates that remain relatively constant, regardless of changes in the discharge head.
Dynamic pumps can be further subdivided into classes,
Centrifugal – axial flow, radial flow, mixed flow, and peripheral flow pumps
Special effect – including eductor (or jet), ejector, and air lift pumps
10
Positive displacement pumps can be further subdivided into classes,
Reciprocating – piston (or plunger) and diaphragm pumps
Rotary – including gear, lobe, screw, progressing cavity, vane, and peristaltic (or tubing) pumps
11
Centrifugal pumps are the most widely used type in engineering applications including:
Low-lift – Vertical Turbine
Axial Flow
Archimedes Screw
High-service – Split-case, double suction centrifugal
Vertical-turbine Pump
Axial Flow (Vertical Propeller) Pump
Archimedes Screw Pumps
Split-case, Double-suction Centrifugal Pump
Booster
Recirculation and transfer
Well – down-hole pumps
Firefighting
Figure 12.6 – Schematic of Basic Elements of Centrifugal Pumps
Centrifugal Pumps
Submersible
Vertical Sump Pump
Horizontal
Fire Pump System, Internal Combustion Driver
Ce.
Immunizing Image Classifiers Against Localized Adversary Attacksgerogepatton
This paper addresses the vulnerability of deep learning models, particularly convolutional neural networks
(CNN)s, to adversarial attacks and presents a proactive training technique designed to counter them. We
introduce a novel volumization algorithm, which transforms 2D images into 3D volumetric representations.
When combined with 3D convolution and deep curriculum learning optimization (CLO), itsignificantly improves
the immunity of models against localized universal attacks by up to 40%. We evaluate our proposed approach
using contemporary CNN architectures and the modified Canadian Institute for Advanced Research (CIFAR-10
and CIFAR-100) and ImageNet Large Scale Visual Recognition Challenge (ILSVRC12) datasets, showcasing
accuracy improvements over previous techniques. The results indicate that the combination of the volumetric
input and curriculum learning holds significant promise for mitigating adversarial attacks without necessitating
adversary training.
Industrial Training at Shahjalal Fertilizer Company Limited (SFCL)MdTanvirMahtab2
This presentation is about the working procedure of Shahjalal Fertilizer Company Limited (SFCL). A Govt. owned Company of Bangladesh Chemical Industries Corporation under Ministry of Industries.
About
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
Technical Specifications
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
Key Features
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface
• Compatible with MAFI CCR system
• Copatiable with IDM8000 CCR
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
Application
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
Overview of the fundamental roles in Hydropower generation and the components involved in wider Electrical Engineering.
This paper presents the design and construction of hydroelectric dams from the hydrologist’s survey of the valley before construction, all aspects and involved disciplines, fluid dynamics, structural engineering, generation and mains frequency regulation to the very transmission of power through the network in the United Kingdom.
Author: Robbie Edward Sayers
Collaborators and co editors: Charlie Sims and Connor Healey.
(C) 2024 Robbie E. Sayers
CFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptxR&R Consult
CFD analysis is incredibly effective at solving mysteries and improving the performance of complex systems!
Here's a great example: At a large natural gas-fired power plant, where they use waste heat to generate steam and energy, they were puzzled that their boiler wasn't producing as much steam as expected.
R&R and Tetra Engineering Group Inc. were asked to solve the issue with reduced steam production.
An inspection had shown that a significant amount of hot flue gas was bypassing the boiler tubes, where the heat was supposed to be transferred.
R&R Consult conducted a CFD analysis, which revealed that 6.3% of the flue gas was bypassing the boiler tubes without transferring heat. The analysis also showed that the flue gas was instead being directed along the sides of the boiler and between the modules that were supposed to capture the heat. This was the cause of the reduced performance.
Based on our results, Tetra Engineering installed covering plates to reduce the bypass flow. This improved the boiler's performance and increased electricity production.
It is always satisfying when we can help solve complex challenges like this. Do your systems also need a check-up or optimization? Give us a call!
Work done in cooperation with James Malloy and David Moelling from Tetra Engineering.
More examples of our work https://www.r-r-consult.dk/en/cases-en/
Water scarcity is the lack of fresh water resources to meet the standard water demand. There are two type of water scarcity. One is physical. The other is economic water scarcity.
Saudi Arabia stands as a titan in the global energy landscape, renowned for its abundant oil and gas resources. It's the largest exporter of petroleum and holds some of the world's most significant reserves. Let's delve into the top 10 oil and gas projects shaping Saudi Arabia's energy future in 2024.
3. When faced with the need to increase volume flow rate or pressure
rise by a small amount, we might consider adding an additional small
pump in parallel or in series with the original pump.
However, to avoid pump damage and loss of combined capacity, any
individual pump should be shutoff at net heads larger than that that
pump’s shutoff heads as indicated by the horizontal dashed lines.
That pump’s branch should also be blocked with a valve to avoid
reverse flow.
Pumps in Parallel and in Series
If the three pumps are identical, it would not be necessary to turn
off any off of the pumps, since the shutoff head of each pump would
occur at the same net head.
4. A pump head-characteristic curve is a graphical representation of the
total head versus the discharge that a pump can supply. These curves, which
are determined from pump tests, are supplied by the pump manufacturer.
Two points of interest on the pump curve are the shutoff head and the
normal discharge or rated capacity.
The shutoff head is the head output by the pump at zero discharge,
while the normal discharge (or head) or rated capacity is the discharge
(or head) where the pump is operating at its most efficient
Variable speed motors can drive pumps at a series of rotative speeds,
which would result in a set of pump curves for the single pump, as
illustrated in the following curve.
Definitions
5. Flow Rates
₪ Volume flow rate: is the volume of fluid flowing past a
section per unit time.
₪ Mass flow rate: is the mass of fluid flowing past a
section per unit time.
₪ Weight flow rate: is the weight of fluid flowing past a
section per unit time.
7. Friction, Fitting,
and Valve Losses
Pump
hS
Total Static Head
Flow rate
Head
System-head-capacity Curve with Positive Lift
The figure illustrates a system-head-
curve in which the head is the sum of
friction, fitting, and valve losses.
The figure illustrates a system-head-
curve in which the head is the sum of
friction, fitting, and valve losses.
8. For Max. Lift
For Min. Lift
Flow rate
Head
System-head-capacity Curve with Varying Static Lift
Z (max)
Z (min)
Pump
hS (min)
hS (max)
hS (max)
hS (min)
The figure illustrates a system-head-
curve with a varying static lift. One for
the minimum lift and the second for
the maximum
9. System Throttled by Valve Operation
Valve
Flow rate
Head
The figure illustrates a system-head-curve
for a throttled system in which various
valve opening are used to vary the head-
discharge curve.
10. When “n” pumps operated in series, the combined net head is
simply the sum of the net head of each pump (at a given
volume flow rate),
Pumps in Series / Parallel
n
1
i
i
combined H
H
When “n” pumps operated in parallel, their individual volume
flow rates (rather than heads) are assumed,
n
1
i
i
combined V
V
11. Pumps Operating in Parallel or in Series
Pump manufacturers also provide curves relating to the break
horsepower (required by pump) to the pump discharge. The break
horsepower is calculating using
550
H
Q
g
bhp
e
Where:
Q is the pump discharge in cfs,
H is the total head in ft,
.g is the specific weight of water
in Ib / ft3, and
e is the pump efficiency.
Where:
Q is the pump discharge in m3/s,
H is the total head in m,
.g is the specific weight of water in
kilonewtons/m3, and
e is the pump efficiency.
e
H
Q
g
bhp
The break horse power (bhp) The (bhp) in SI unites is given in
kilowatts
12. Pumps in Parallel
Volume Flow- rate V
.
Performance Curve “one pump”
Performance Curve “two pump”
System Curve
A
B
Head
H
For two identical pumps in parallel, the combined performance curve is
obtained by adding flow-rates at the same head. As shown in the figure above,
the flow-rate for the system will not be doubled with the addition of two pumps
in parallel (if the same system curve applies). However, for a relatively flat
system curve (see the shown figure), a significant increase in flow-rate can be
obtained as the operating point moves from point “A” to point “B”.
For two pumps in parallel,
added flow-rates
13. Pumps in Series
Volume Flow- rate V
.
Performance Curve “one pump”
Performance Curve “two pump”
System Curve
A
B
Head
H
When two pumps are placed in series, the resulting pump performance curve is
obtained by adding heads at the same flow-rate. As shown in the figure, for two
identical pumps in series, both the actual head gained by the fluid and the flow-
rate increased, but neither will be doubled if the system curve remains the
same. The operating point is at “A” for one pump and moves to “B” for two
pumps in series.
For two pumps in series,
added heads
14.
V
Head
H
Fig. ( ) – Pumps Operating in Parallel
Q1 Q2
V
Head
H
H1
H2
Fig. ( ) – Pumps Operating in Series
For pumps operating in parallel, the head-
characteristic curves are added horizontally
with respective heads remaining the same.
For pumps operating in parallel, the
head-characteristic curves are added
horizontally with respective heads
remaining the same.
Pumps Operating in Parallel or in Series
15.
V
Head
H
500 rev/min
800 rev/min
1000 rev/min
1200 rev/min
Fig. ( ) - Pump Performance Curves for Variable-speed Pumps.
Pump Performance Curves for Variable-speed Pumps.
16. Pumps Operating in Parallel or in Series
A better course of action is to
Increase the original pumps speed and/or input power
(large electric motor),
Replace the impeller with a larger one, or
Replace the enter pump with a larger one.
17. hS
System Head Curve
Pump Characteristic Curve
Volume Flow Rate
Efficiency
Head
Efficiency
Determination of Operating Points for a Single Speed Pump
For a Fixed Static Lift (head) hS
18. Determination of Operating Points for a Single Speed Pump
In order to determine the operating point for a pump or
pumps in a piping system, the characteristic curve is
superimposed on the system curve as illustrated in the figure.
The point of intersection of the two curves is the pump
operating point.
The pump operating point should be at or near the maximum
efficiency of the
19. hS Max.
Characteristic Curve for
two Pumps
Volume Flow Rate
Head
Determination of Operating Points for Two Single Speed Pumps
Pumps in Parallel and a Variable Static Lift (head) hS
Characteristic Curve for
one Pump
hS Min.
Maximum System Curve
Minimum System Curve
Operating Points
Possible range of
operation for one pump
Possible range of
operation for two pumps
20. Determination of Operating Points for Two Single Speed Pumps
The figure illustrates the operating points for two single-
speed pumps operating in parallel for piping system that has
a range of static lift
The system curves are shown for the maximum lift and the
minimum lift.
Also shown is the range of operating points (between
minimum and maximum static lift) for a single pump.
21.
V
Head
H
100% speed
System with a Single Pump Operating at Variable-speed
95% speed
90% speed
85% speed
Operating Points
hS
System Curve
The Figure illustrates the operating points for a variable-speed pump
with a system curve. The affinity laws can be used to determine the
rotational at any desired operating points.
22. Pump “1”
Pump “2”
Pump “3”
Combined
Capacity
Shutoff head of combined pumps
Free delivery of combined pumps
Pump Performance Curve for Three Dissimilar Pumps in Parallel
Pump “3” is the strongest & Pump “1” is the weakest
Pump “3”
Pump “1”
V
2
3 V
V
1
2
3 V
V
V
H
23. At low values of net head, the combined capacity is equal to
the sum of the capacity of each pump by itself,
However, to avoid pump damage and loss of combined
capacity, any individual pump should be shut off at net heads
larger than that pump’s shutoff heads as indicated by the
horizontal dashed lines. That pumps branch should also be
blocked with a valve to avoid reverse
If the three pumps are identical, it would not be necessary to
turn off any off any of the pumps, since the shutoff head of
each pump would occur at the same net head.
Pump Performance Curve for Three Dissimilar Pumps in Parallel
24. Pump “1”
Pump “2”
Pump “3”
Shutoff head of combined pumps
Free delivery of
combined pumps
Pump Performance Curve for Three Dissimilar Pumps in Series
Pump “3” is the strongest & Pump “1” is the weakest
Pump 3
Pump 1
H
1
2
3 H
H
H
2
3 H
H
only
H3
V
25. At low values of volume flow rate, the combined net head is
equal to the sum of the net head of each pump by itself.
However, to avoid pump damage and loss of combined net
head, any individual pump should be shut off and bypassed at
flow rates larger than that pump’s free delivery, as indicated by
the vertical dashed lines.
If the three pumps were identical, it would not be necessary to
turn off any of the pumps, since the free delivery of each pump
would occur at the same volume flow rate.
Pump Performance Curve for Three Dissimilar Pumps in Series
26. Pumps Operating in Parallel or in Series
Arranging dissimilar pumps in series may create problems
because the volume flow rate through each pump must be
the same, but the overall pressure rise is equal to the present
rise of one pump plus that of the other. If the pumps have
widely different performance curves, the smaller pump may
be forced to operate beyond its free delivery flow rate,
whereupon it acts like a head loss, reducing the total volume
flow rate.
Arranging dissimilar pumps in parallel may create problems
because the overall pressure rise must be the same, but the
net volume flow rate is the sum of that through each branch.
27. Operating Characteristics
Operating characteristics of pumps are dependent upon their:
Size Speed and design
In centrifugal pumps, similar flow patterns occur in geometrically
similar pumps. Through dimensional analysis the following three
independent coefficients can be derived to describe the operation
of pumps.
3
Q
D
N
Q
C
:
t
coefficien
Discharge
-
2
2
H
D
N
H
C
:
t
coefficien
Head
-
ess)
correction
l
dimensiona
(for
D
N
H
g
C
or 2
2
H
5
3
H
D
N
P
C
:
t
coefficien
Power
-
Affinity laws
Even though it is not dimensionally
correct, it is commonly used
29. Operating Characteristics
These equations are the same either in SI of BG units, but with
different values.
ft3/s
m3/s
is pump capacity
Q
r.p.m
radians /
second
is the speed
N
ft
m
is the impeller diameter
D
32.2ft3/s
9.81m3/s
is the acceleration due to gravity
g
horsepower
kilowatts
is the power
P
Slugs/ft3
Kg/m3
is the density
30. Operating Characteristics
The coefficients mentioned before can be used to define the
affinity laws for a pump operating at two different speeds and the
same diameter. Consider the ratios (CQ)1 = (CQ)2 for the same
diameter and different speeds N1 and N2. (where 1 and 2 represent
corresponding points)
2
1
2
1
N
N
Q
Q
Similarly for (CH)1= (CH)2:
2
2
1
2
1
N
N
H
H
and similarly for (CP)1= (CP)2:
3
2
1
2
1
N
N
P
P
Affinity laws for
discharge and for head
equation are accurate
The affinity laws for power
may not be accurate
31. Operating Characteristics
These relationships assume that the efficiency remains the same
for one point on a pump curve to a homologous point on another
pump curve.
32. Specific Speed “NS”
The specific speed NS is not really representative of any meaningful
or measurable speed in a machine, so some practitioners refer to it
as “type number”, since it is used in selection of pump type.
The value of NS for a particular machine is calculated for the
conditions obtained at its point of optimum efficiency, since ideally
this should coincide with the installed operating point of pump.
The wide variety of units are used in calculating values of NS. The
engineer needs to check this point carefully with the pump
manufacturer.
33. Specific Speed “NS”
3
Q
D
N
Q
C 2
2
H
D
N
H
C
can be eliminated by dividing CQ
1/2 by CH
1/2 as so the specific
speed becomes
H
Q
N
)
D
N
H
(
)
ND
Q
(
C
C
N 4
3
4
3
2
2
2
1
3
4
3
H
2
1
Q
S
The discharge and head coefficients
Historically the “g”
term was disregarded
4
3
2
1
4
3 /
/
S
ft
min)
/
gal
(
)
m
.
p
.
r
(
H
Q
N
N
Note:
NS is applied
only to BEP
Best Efficient
Point
34. Specific Speed “NS”
a very rough guide to the range of duties covered by the different
machine is as follows:
Taking
N: revolution/ min Q: in m3/s and H: in m
10 ˂ NS ˂ 70 : centrifugal pump (high head, low to moderate discharge)
70 ˂ NS ˂ 165 : mixed flow pump (moderate head, moderate discharge)
NS ˂ 165 : axial flow pump (low head, high discharge)
35. Worked Example
A 6.85-in pump, running at 3500 r.p.m, has the following measured
performance for water:
450
400
350
300
250
200
150
100
50
Q,
(gal/min)
139
156
169
181
189
194
198
200
201
H ( ft)
74
79
81
80
77
72
64
50
29
%
A. Estimate the horsepower at BEP.
B. If this pump is rescaled in water to provide 20hp at
3000 r.p.m, determine the appropriate:
C. Impeller diameter,
D. Flow rate, and
E. Efficiency for this new condition.
36. hp
.
.
.
)
.
.
(
/
H
Q
g
power 47
18
550
81
0
169
10
228
2
350
2
32
94
1 3
Worked Example
From the table given: at best efficient point = 81% and the
corresponding flow rate = 350 gal/min and the head = 169 ft. The
corresponding horsepower
N = 3000 r.p.m
N = 3500 r.p.m
D2 = ??-in
D1 = 6.85-in
Q2 = ??? gal/min
Q1 = 350 gal/min
(Power) 2 = 20 hp
(Power) 1 = 18.47 hp
The given data can be tabulated in the following table:
37. 3
1
2
1
2
1
2
D
D
N
N
Q
Q
Worked Example
Applying the similarity laws:
gives
min
/
gal
.
.
D
D
N
N
Q
Q 415
85
6
63
7
3000
3500
350
3
3
1
2
1
2
1
2
5
1
2
3
1
2
1
2
1
2
D
D
N
N
P
P
gives
5
2
3
85
6
3500
3000
47
18
20
.
D
.
which gives in
.
D
63
7
2
The efficiency for this new condition have to be = 81%:
38. Worked Example
Tests on a 14.62-in-diameter centrifugal water pump at 2134 r.p.m
yields the following data:
10
8
6
4
2
0
Q, (ft3/sec)
220
300
330
340
340
340
H ( ft)
330
330
255
205
160
135
bhp
A. What is the BEP?
B. What is the specific speed?
C. Estimate the maximum discharge possible.
Table (1)
39.
/
H
Q
g
power
horse
break
Worked Example
550
2
32
94
1
H
Q
.
.
bhp
/
H
Q
g
or
Substituting the given values (Table 1) into Eq. (1) for 2134 r.p.m
gives :
10
8
6
4
2
0
Q, (ft3/sec)
220
300
330
340
340
340
H ( ft)
330
330
255
205
160
135
bhp
76
83
88
75
48
0
%
1.0 gallon/min=
2.22810-3 ft3 / sec
……………….….. (1)
46. 3 to 4ycr
ycr
ycr
Example Locations of Critical Flow
Critical Depth near Overfall
Flow over a Broad-crested Weir
47. Example Locations of Critical Flow
ycr
Hydraulic Jump
Flow Through a Hydraulic Jump
ycr
Chang in the Bottom Slope of the Channel
48. 3 to 4ycr
ycr
ycr
Example Locations of Critic
Critical Depth near Overfall
Flow over a Broad-crested Weir
3 to 4ycr
ycr
ycr
Example Locations of Critical Flo
Critical Depth near Overfall
Flow over a Broad-crested Weir
Example Locations of Critical Flow
ycr
Hydraulic Jump
Flow Through a Hydraulic Jump
ycr
Chang in the Bottom Slope of the Channel
Example Locations of Critical Flow
ycr
Hydraulic Jump
Flow Through a Hydraulic Jump
ycr
Chang in the Bottom Slope of the Channel
Example Locations of Critical Flow
49. hp
EGL
Z1- Zo
Zo=0
P0 = 14.7 psi
P0/g = 34ft
EGL
Pv = 0.506 psi
Pv/g = 1.17ft
For water at T=27oC
65. Control Surface
A Fitting between Two Pipes of Different Size (TRANSITION)
The continuity equation gives:
The general momentum equation
for steady one-dimensional flow
is:
x
y
P1
V1 V2
P2
)
V
V
(
Q
F
p
p
1
2
bold
2
1