Uniform Flow: Basic concepts of free surface flows,
velocity and pressure distribution,
Mass, energy and momentum principle for prismatic and non-prismatic channels,
Review of Uniform flow: Standard equations,
hydraulically efficient channel sections,
compound sections,
Energy-depth relations:
Concept of specific energy, specific force,
critical flow, critical depth,
hydraulic exponents, and
Channel transitions.
Uniform Flow: Basic concepts of free surface flows,
velocity and pressure distribution,
Mass, energy and momentum principle for prismatic and non-prismatic channels,
Review of Uniform flow: Standard equations,
hydraulically efficient channel sections,
compound sections,
Energy-depth relations:
Concept of specific energy, specific force,
critical flow, critical depth,
hydraulic exponents, and
Channel transitions.
OPEN CHANNEL FLOW AND HYDRAULIC MACHINERY
Open channel flow: Types of flows – Type of channels – Velocity distribution – Energy and momentum correction factors – Chezy’s, Manning’s; and Bazin formula for uniform flow – Most Economical sections. Critical flow: Specific energy-critical depth – computation of critical depth – critical sub-critical – super critical flows
Non-uniform flows –Dynamic equation for G.V.F., Mild, Critical, Steep, horizontal and adverse slopes-surface profiles-direct step method- Rapidly varied flow, hydraulic jump, energy dissipation
WEIRS VERSUS BERRAGE
TYPES OF WEIRS
COMPONENT PARTS OF A WEIR
CAUSES OF FAILURE OF WEIRS & THEIR REMEDIES
DESIGN CONSIDERATIONS
DESIGN FOR SURFACE FLOW
DESIGN OF BARRAGE OR WEIR
OPEN CHANNEL FLOW AND HYDRAULIC MACHINERY
Open channel flow: Types of flows – Type of channels – Velocity distribution – Energy and momentum correction factors – Chezy’s, Manning’s; and Bazin formula for uniform flow – Most Economical sections. Critical flow: Specific energy-critical depth – computation of critical depth – critical sub-critical – super critical flows
Non-uniform flows –Dynamic equation for G.V.F., Mild, Critical, Steep, horizontal and adverse slopes-surface profiles-direct step method- Rapidly varied flow, hydraulic jump, energy dissipation
WEIRS VERSUS BERRAGE
TYPES OF WEIRS
COMPONENT PARTS OF A WEIR
CAUSES OF FAILURE OF WEIRS & THEIR REMEDIES
DESIGN CONSIDERATIONS
DESIGN FOR SURFACE FLOW
DESIGN OF BARRAGE OR WEIR
VRA 2014- MDID Users Group PresentationGrace Barth
MDID Users Group session, Visual Resources Association 32nd annual conference, Milwaukee, WI. Thursday, March 13, 2014.
Organizer/Moderator: Grace Barth, James Madison University
Presenters:
Grace Barth, James Madison University
Kevin Hegg, James Madison University
Andreas Knab, vrcHost
Several institutions have switched to MDID3 in the past year, and we look forward to sharing some of those experiences as well as showcasing new features. In this session we will share updates to MDID3 such as the new ability to share collections between institutions, packaged slideshows, and cataloging improvements. The MDID team will be prepared to discuss software and hardware requirements, installation issues, best practices, system integration, custom application development, and other topics. Andreas Knab from vrcHost will discuss MDID hosting experiences and any upcoming features. This informative session is open to anyone using or interested in MDID. Adequate time for a question and answer period will follow the presentation.
Continuing the tradition of a freely shared educational resource, MDID is distributed free of charge under an open source license and is used at many institutions across the United States and around the world.
Sponsored by: vrcHost
vrcHost specializes in installation, integration, customization, and feature development for the Madison Digital Image Database (MDID) project - an open source digital content management system used at hundreds of institutions worldwide for teaching and scholarship in the visual arts.
Fluid Mech. Presentation 2nd year B.Tech.shivam gautam
This Presentation covers the following topics-
Series,parallel branching pipes,
equivalent pipe length,
moody's chart
for ppt format contact me on gautam.shivam98@yahoo.com
Fluid Mechanics
Internal and External Flows
Part A
Friction factor, Pipe losses, Boundary Layer, Over external bodies, Flow Separation and control methods, Lift generation, Flow simulation methodology
Part B
Siphon, Transmission of power, Drag and lift, Characteristics of bodies
This is basic course in mechanical engineering both graduate and post graduate level.
Hope you find it helping.
Do like, Share and Comment.
Aditya Deshpande
deshadi805@gmail.com
We have compiled the most important slides from each speaker's presentation. This year’s compilation, available for free, captures the key insights and contributions shared during the DfMAy 2024 conference.
Understanding Inductive Bias in Machine LearningSUTEJAS
This presentation explores the concept of inductive bias in machine learning. It explains how algorithms come with built-in assumptions and preferences that guide the learning process. You'll learn about the different types of inductive bias and how they can impact the performance and generalizability of machine learning models.
The presentation also covers the positive and negative aspects of inductive bias, along with strategies for mitigating potential drawbacks. We'll explore examples of how bias manifests in algorithms like neural networks and decision trees.
By understanding inductive bias, you can gain valuable insights into how machine learning models work and make informed decisions when building and deploying them.
HEAP SORT ILLUSTRATED WITH HEAPIFY, BUILD HEAP FOR DYNAMIC ARRAYS.
Heap sort is a comparison-based sorting technique based on Binary Heap data structure. It is similar to the selection sort where we first find the minimum element and place the minimum element at the beginning. Repeat the same process for the remaining elements.
Low power architecture of logic gates using adiabatic techniquesnooriasukmaningtyas
The growing significance of portable systems to limit power consumption in ultra-large-scale-integration chips of very high density, has recently led to rapid and inventive progresses in low-power design. The most effective technique is adiabatic logic circuit design in energy-efficient hardware. This paper presents two adiabatic approaches for the design of low power circuits, modified positive feedback adiabatic logic (modified PFAL) and the other is direct current diode based positive feedback adiabatic logic (DC-DB PFAL). Logic gates are the preliminary components in any digital circuit design. By improving the performance of basic gates, one can improvise the whole system performance. In this paper proposed circuit design of the low power architecture of OR/NOR, AND/NAND, and XOR/XNOR gates are presented using the said approaches and their results are analyzed for powerdissipation, delay, power-delay-product and rise time and compared with the other adiabatic techniques along with the conventional complementary metal oxide semiconductor (CMOS) designs reported in the literature. It has been found that the designs with DC-DB PFAL technique outperform with the percentage improvement of 65% for NOR gate and 7% for NAND gate and 34% for XNOR gate over the modified PFAL techniques at 10 MHz respectively.
Harnessing WebAssembly for Real-time Stateless Streaming PipelinesChristina Lin
Traditionally, dealing with real-time data pipelines has involved significant overhead, even for straightforward tasks like data transformation or masking. However, in this talk, we’ll venture into the dynamic realm of WebAssembly (WASM) and discover how it can revolutionize the creation of stateless streaming pipelines within a Kafka (Redpanda) broker. These pipelines are adept at managing low-latency, high-data-volume scenarios.
Hierarchical Digital Twin of a Naval Power SystemKerry Sado
A hierarchical digital twin of a Naval DC power system has been developed and experimentally verified. Similar to other state-of-the-art digital twins, this technology creates a digital replica of the physical system executed in real-time or faster, which can modify hardware controls. However, its advantage stems from distributing computational efforts by utilizing a hierarchical structure composed of lower-level digital twin blocks and a higher-level system digital twin. Each digital twin block is associated with a physical subsystem of the hardware and communicates with a singular system digital twin, which creates a system-level response. By extracting information from each level of the hierarchy, power system controls of the hardware were reconfigured autonomously. This hierarchical digital twin development offers several advantages over other digital twins, particularly in the field of naval power systems. The hierarchical structure allows for greater computational efficiency and scalability while the ability to autonomously reconfigure hardware controls offers increased flexibility and responsiveness. The hierarchical decomposition and models utilized were well aligned with the physical twin, as indicated by the maximum deviations between the developed digital twin hierarchy and the hardware.
Literature Review Basics and Understanding Reference Management.pptxDr Ramhari Poudyal
Three-day training on academic research focuses on analytical tools at United Technical College, supported by the University Grant Commission, Nepal. 24-26 May 2024
2. GROUP MEMBERS
2
No Name Id Programe
01 Lipon islam 14207082 BSME
02 Jilani al mamun 14207099 BSME
03 Rashedujjaman 14207069 BSME
04 Nazmul Hossain 14207088 BSME
05 ALamin 13107061 BSME
4. CONTENTS:
4
Flow through simple pipes
Loss of head in pipes
Darcy’s formula for loss of head in pipes
Chezy’s formula for loss of head in pipes
Transmission of power through pipe
Time of emptying a Tank through a long pipe
Flow through compound pipes
Discharge from one reservoir to another through a pipe line
Discharge through a compound pipe
Discharge through pipes in parallel
5. LOSS OF HEAD IN PIPES
5
Whenever the water is flowing in apipe ,it experiences some resistance to its
motion,whos efect is to reduse the velocity and ultimately the head of water
available .though there are many types of losses ,yet the major loss is due to
frictional resistance of the pipe only.the frictional resistance of the pipe depends
upon the roughness of the inside surface of the pipe,grseater will be the
resistance .this friction is known as fluid friction and the resistance is known as
frictional resistance . the earlier experiment on the fluid friction were conducted
by froude we concluded on that
1.The frictional resistance varies approximately with the square of thee velocity
of the liquid.
2.The frictional resistance varies with the name of the surface lare on ,some
empirical formula were derived for the loss of head due to the friction out of
which following two are important from the subject point of view.
3.dercy’s formula for loss of head in pipes and
4.chezy’s formula for loss of head in pipes
6. DARCY’S FORMULA FOR LOSS OF HEAD IN PIPE
Fig: uniform long pipe
Consider a uniform long pipe through which is
flowing at a uniform rate.
6
1
1
2
2
7. Let,
l = length of pipe
d = diameter of a pipe
v = velocity of water in the pipe
f' =frictional resistance per unit area per unit velocity
ℎ 𝑓=𝑙𝑜𝑠𝑠 𝑜𝑓 ℎ𝑒𝑎𝑑 𝑑𝑢𝑒 𝑡𝑜 𝑓𝑟𝑖𝑐𝑡𝑖𝑜𝑛
let us consider sections (1-1) and (2-2) of the pipe .
Now let
𝑃1= 𝑖𝑛𝑡𝑒𝑛𝑠𝑖𝑡𝑦 𝑜𝑓 𝑝𝑟𝑒𝑠𝑠𝑢𝑟𝑒 𝑎𝑡 𝑠𝑒𝑐𝑡𝑖𝑜𝑛 1 − 1,
𝑃2 = 𝑖𝑛𝑡𝑒𝑛𝑠𝑖𝑡𝑦 𝑜𝑓 𝑝𝑟𝑒𝑠𝑠𝑢𝑟𝑒 𝑎𝑡 𝑠𝑒𝑐𝑡𝑖𝑜𝑛 2 − 2 ,
Now considering horizontal forces on water between sections (1-1)
and (2-2)and equating the same ,
𝑝1 𝐴 = 𝑝2 𝐴 + 𝑓𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑎𝑙 𝑟𝑒𝑠𝑖𝑠𝑡𝑎𝑛𝑐
or frictional resistance
=𝑝1 𝐴 − 𝑝2 𝐴
∴
𝐹𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑎𝑙 𝑟𝑒𝑠𝑖𝑠𝑡𝑎𝑛𝑐𝑒
𝑤
=
𝑝1𝐴−𝑝2 𝐴
𝑤
7
7
8. 𝐹𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑎𝑙 𝑟𝑒𝑠𝑖𝑠𝑡𝑎𝑛𝑐𝑒
𝐴𝑤
=
𝑝1
𝑤
−
𝑝2
𝑤
But ,
𝑝1
𝑤
−
𝑃2
𝑤
= hf = loss of pressure head due to friction
ℎ
𝑓=
𝑓𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑎𝑙 𝑟𝑒𝑠𝑖𝑠𝑡𝑎𝑛𝑐𝑒
𝐴𝑤
=
𝐹𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑎𝑙 𝑟𝑒𝑠𝑖𝑠𝑡𝑎𝑛𝑐𝑒
𝜋
4
×𝑑2×𝑤
We know that as per froudes experiment frictional resistance
ℎ 𝑓
= 𝐹𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑎𝑙 𝑟𝑒𝑠𝑖𝑠𝑡𝑎𝑛𝑐𝑒 𝑝𝑒𝑟 𝑢𝑛𝑖𝑡 𝑎𝑟𝑒𝑎 𝑎𝑡 𝑢𝑛𝑖𝑡 𝑣𝑒𝑙𝑜𝑐𝑖𝑡𝑦
× 𝑤𝑒𝑡𝑡𝑒𝑑 𝑎𝑟𝑒𝑎 × (𝑣𝑒𝑙𝑜𝑐𝑖𝑡𝑦)2
f × 𝜋𝑑𝑙 × 𝑣2
substituting the value of friction resistance in the above
equation
ℎ 𝑓 =
𝑓𝜋𝑑𝑙×𝑣2
𝜋
4
×𝑑2 𝑤
=
4𝑓𝑙𝑣2
𝑤𝑑
8
9. let us introduce another coefficient (𝑓′
)𝑠𝑢𝑐ℎ 𝑡ℎ𝑎𝑡
𝑓′
=
𝑓𝑤
2𝑔
ℎ 𝑓 =
4
𝑤𝑑
×
𝑓𝑤
2𝑔
× 𝑙𝑣2
=
4𝑓𝑙𝑣2
2𝑔𝑑
We know that the discharge
Q=
𝜋
4
× 𝑑2
× 𝑣 𝑜𝑟 𝑣 =
4𝑄
𝜋𝑑2
𝑉2
=
16𝑄2
𝜋2 𝑑4
Substituting the value of 𝑉2 𝑖𝑛 𝑒𝑞𝑢𝑎𝑡𝑖𝑜𝑛 1
ℎ 𝑓 =
4, 𝑓𝑙
2𝑔𝑑
×
16𝑄2
𝜋2 𝑑4=
𝑓𝑙𝑄2
3𝑑5
9
10. CHEZY'S FORMULA FOR LOSS OF HEAD IN
PIPES:
Consider a uniform long pipe through which water is following at
a uniform rates shown in fig:
Let
I = Length of the pipe and
D = Diameter of the pipe
Area of pipe 𝐴 =
𝜋
4
×𝑑2
And perimeter of pipe P = 𝐴 = 𝜋d
V = velocity of water in pipe
f = Frictional resistance, per unit area of v'etted surface per unit
velocity and
ℎ1, Loss of head due to frication
Now let us consider section (1-1) and (2-2) of the pipe Let,
𝑝1= intensity of pressure at section 1 –land P2= Intensity of
pressure at section 2,2
11. A LITTLE CONSIDERATION WILL SHOW THAT P1 AND P2 WOULD HAVE BEEN
EQUAL , IF THERE WOULD HAVE BEEN NO FRICTIONAL RESISTANCE . NOW
CONSIDERING HORIZONTAL FORCES ON WATER BETWEEN SECTIONS 1-1 AND 2-
2 AND EQUATING THE SAME ,
𝑝1𝐴=𝑝2𝐴+𝑓𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑎𝑙 𝑟𝑒𝑠𝑖𝑠𝑡𝑎𝑛𝑐𝑐𝑒
OR, FRICTIONAL RESISTANCE=𝑝1 𝐴 − 𝑝2A
OR,
𝑓𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑎𝑙 𝑟𝑒𝑠𝑖𝑠𝑡𝑎𝑛𝑐𝑒
𝑤
=
𝑝1𝐴−𝑝2𝐴
𝑤
OR,
𝑓𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑎𝑙 𝑟𝑒𝑠𝑖𝑠𝑎𝑡𝑎𝑛𝑐𝑒
𝐴𝑤
=
𝑝1
𝑤
-
𝑝2
𝑤
11
12. But ,
𝑝1
𝑤
−
𝑝2
𝑤
= ℎ 𝑓= loss of pressure head due to friction
ℎ𝑓=
(𝑓𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑎𝑙 𝑟𝑒𝑠𝑖𝑠𝑡𝑎𝑛𝑐𝑒)
𝐴𝑤
We know that’s experiment , frictional resistance
=frictional resistance per unit area at velocity × wetted
area×(𝑣𝑒𝑙𝑜𝑐𝑖𝑡𝑦)2
=f´×𝜋𝑑𝑙 × 𝑣2
Substituting the value of frictional resistance in the above
equation
ℎ 𝑓=
f´× 𝜋𝑑𝑙×𝑣2
𝐴𝑤
=
f𝑙𝑣2´
𝐴𝑤
(∴ 𝜋𝑑 = 𝑝 𝑖. 𝑒 𝑝𝑟𝑒𝑚𝑖𝑡𝑒𝑟)
=
f𝑙𝑣2´
𝐴𝑤
×
𝑝
𝐴
12
13. Now substituting another term of hydraulic mean depth in the above
equation ,such that hydraulic mean depth
m=
𝑎𝑟𝑒𝑎 𝑜𝑓 𝑓𝑙𝑜𝑤
𝑤𝑒𝑦𝑦𝑒𝑑 𝑝𝑒𝑟𝑖𝑚𝑒𝑡𝑒𝑟
=
𝐴
𝑝
∴ ℎ 𝑓=
f´𝑙𝑣2
𝐴𝑤
×
1
𝑚
𝑣
2=
ℎ𝑓.𝑤.𝑚
𝑓´𝑙 =
𝑤
𝑓´
×m×
ℎ𝑓
𝑙
V=
𝑤
𝑓´
×m×
ℎ𝑓
𝑙
……(1)
Now substituting two more terms in the above equation such that
C=
𝑤
𝑓´
=c
ℎ 𝑓=𝑖
Now substituting the above two values in equation (1)
V=c 𝑚𝑖 13
15. Whenever water is allowed to fall from higher level to lower level ,
we can always generate some power as a matter of fact ,whenever
we come across a waterfall, we do not allow the water simply to
fall. But it is made to follow through a pipe , so that the direction of
the water may be set in some convenient way from which we may
produce some power .
A little consideration will show that some hade of water will be
lost due to friction in the pipe through which the water is flowing
Fig: transmission of pipes
15
16. Consider a high level strong tank .let a pipe AB lead
water from this tank from A to a power house at B
as shown in figure:
𝐻 =Hade of water at a power house AB in meters
𝑙 = length of the pipe AB in metre
𝑣 = velocity of water in the pipe in m/s
ℎ1=loss of heat in the pipe AB due to friction in
meters
𝑓 = coefficient of friction, and
d=diameter of the pipe AB in meters
16
17. Cross-sectional area of the pipe,
a =
𝜋
4
× d2
𝑚2
We know the weight of water flowing per second `
η = 𝑤𝑄 = 𝑤𝑣𝑎 𝐾𝑁
(AS
𝑣
𝑠
= 𝑄 𝑎𝑛𝑑 𝑤 =
𝑊
𝑣
)
And net head of water available at 𝐵 (neglecting minor losses)
Efficiency of transmission,
η =
ℎ
𝐻
=
𝐻−ℎ 𝑓 𝐴
𝐻
we also know that power available,
𝑝 = Weight of water flowing per second × Head of water
= 𝑤𝑄. ℎ = 𝑤𝑎𝑣 𝐻 − ℎ 𝑓 = 𝑤𝑎𝑣 (𝐻 −
4𝑓𝑙𝑣2
2𝑔𝑑
)
. = 𝑤𝑎(𝐻𝑣 −
4𝑓𝑙𝑣2
2𝑔𝑑
)
17
18. A little consideration will shown that, in that above equation, the
power transmitted depends upon the velocity of water (v),as the
other things are constant. Therefore the power transmitted will
be maximum when
𝑑𝑝
𝑑𝑣
= 0
Or when the differential coefficient of the amount inside the
bucket of equation (𝑖𝑖𝑖) is zero . i e
𝑑 ( 𝐻𝑣 −
4𝑓𝑙𝑣2
2𝑔𝑑
)
𝑑𝑣
= 0
Or 𝐻 – 3
4𝑓𝑙𝑣2
2𝑔𝑑
= 0
Or 𝐻 – 3ℎ 𝑓 = 0 as (
4𝑓𝑙𝑣2
2𝑔𝑑
= ℎ 𝑓)
Or ℎ 𝑓 =
𝐻
3
It means that the power transmission through a pipe is
maximum, when the head lost due to friction in the pipe is equal
to 1/3 of the total supply head.
18
20. Consider a tank, which is to be emptied through a long pipe as shown in fig.
Let,
𝐻1 = Initial head of water, in the tank, before opening the pipe,
𝐻2= Final head of water, in the tank, after opening the pipe in T seconds,
(𝐻1-𝐻2) =Fall of water level in the tank,
A (𝐻1-𝐻2) = Volume of water discharged through the pipe,
l = Length of the pipe,
d= diameter of the pipe
T=time taken in seconds , to fall the water level in the tank from 𝐻1 to 𝐻2
20
21. Consider an instant, when the head of water in the tank
is h. After a small interval of time dt, at the water level
in the tank fall down by an amount equal to dh.
Volume of water that has passed through the pipe in
the time dt
= -Adh ……. (1)
(Minus value of dh is taken, as the value of h
decreases as the as the discharge increases).
Since the water is being discharged in the
atmosphere, therefore (ignoring all other losses except
friction) there will be some loss of head of water at
outlet also.
21
23. dt=
−4𝐴 1+
4𝑓𝑙
𝑑
𝑑ℎ
𝜋𝑑2 2𝑔ℎ
=
−4𝐴 1+
4𝑓𝑙
𝑑
( ℎ−1
2)𝑑ℎ
𝜋𝑑2 2𝑔
Now the total time T, required to bring the water level
from 𝐻1 𝑡𝑜 𝐻2 may be found by integrating the equation
between the limits 𝐻1 𝑎𝑛𝑑 𝐻2 i,e…
T= 𝐻1
𝐻2
−4𝐴 1+
4𝑓𝑙
𝑑
( ℎ−1
2)𝑑ℎ
𝜋𝑑2 2𝑔
We have seen that the velocity of water
v =
2𝑔ℎ
(1+4𝑓𝑙
𝑑
)
∴ 𝑣𝑒𝑙𝑜𝑐𝑖𝑡𝑦 𝑜𝑓 𝑤𝑎𝑡𝑒𝑟 𝑤ℎ𝑒𝑛 𝑡ℎ𝑒 ℎ𝑒𝑎𝑑 𝑜𝑓 𝑤𝑎𝑡𝑒𝑟 𝑖𝑠 𝐻1
𝑣1=
2𝑔𝐻1
(1+4𝑓𝑙
𝑑
) 23
25. Taking minus out of the bracket,
T=
8𝐴 1+
4𝑓𝑙
𝑑
𝜋𝑑2 2𝑔
×( 𝐻1 + 𝐻2)
If the tank is to be completely emptied ,then
substituting 𝐻2=0,in the above equation
T=
8𝐴 1+
4𝑓𝑙
𝑑
𝜋𝑑2 2𝑔
× 𝐻1
25
26. DISCHARGE FROM ONE RESERVOIR TO
ANOTHER THROUGH A PIPE LINE
sometimes ,discharge from one reservoir to another takes place
through a pipe line.in such a case ,It is assumed that the
difference between the water levels of the two reservoir is lost
due to friction in the pipe in the line . we can discuss the
discharge from one reservoir to another through-
1.Compound pipes
2.Pipes in parallel
3.Branched pipes and
4. Siphon pipes
25
27. DISCHARGE THROUGH A COMPOUND PIPE(I.E
PIPES IN SERIES)
Sometimes while laying a pipeline ,we have to connect pipes of
different lengths and different diameters with one another to from
a pipe line . such a pipe line is called a compound pipe or pipes
in series .a little consideration will show that as the pipes are in
series ,therefore the discharge will be continuous.
Now consider a compound pipe discharge water from one tank
with a higher water level to another with a lower water level as
shown fig.
26
28. Let,
Q=discharge through the pie
H=total loss of head
𝑑1=diameter of pipe 1
𝑙1=length of pipe 1
𝑓1=coefficient of friction of pipe 1
𝑑2 𝑙2 𝑓2=corresponding value of pipe 2
𝑑3 𝑙3 𝑓3 =corresponding value of pipe 3 and so on
Neglecting minor losses except friction , we know that the total
loss of head,
H=loss of head in pipe 1+loss of head in pipe 2+loss of head in
pipe 3
=
4𝑙1 𝑓1 𝑣1
2
2𝑔𝑑1
+
4𝑙2 𝑓2 𝑣2
2
2𝑔𝑑2
+
4𝑙3 𝑓3 𝑣3
2
2𝑔𝑑3
+….
=
4
2𝑔
(
𝑙1 𝑓1 𝑣1
2
𝑑1
+
𝑙2 𝑓2 𝑣2
2
𝑑2
+
𝑙3 𝑓3 𝑣3
2
𝑑3
+…..)
27
29. If the coefficient of friction is the sum for all the
pipes,then
H=
4𝑓
2𝑔
(
4𝑙1 𝑣1
2
𝑑1
+
4𝑙2 𝑣2
2
𝑑2
+
4𝑙3 𝑣3
2
𝑑3
+……)
If the discharge through the pipe line is given then the
total loss of head
H=
𝑓1 𝑙1 𝑄2
3𝑑1
5 +
𝑓2 𝑙2 𝑄2
𝑑2
5 +
𝑓3 𝑙3 𝑄2
𝑑3
5 +………
=
𝑄2
3
(
𝑓1 𝑙1
𝑑1
5+
𝑓2 𝑙2
𝑑2
5+
𝑓3 𝑙3
𝑑3
5+………)
If the coefficient of friction is the same for all pipes,then
H==
𝑓𝑄2
3
(
𝑙1
𝑑1
5+
𝑙2
𝑑2
5+
𝑙3
𝑑3
5+………) 28
30. DISCHARGE THROUGH PIPES IN PARALLEL
Sometimes in order to increase the discharge from one tank into another , anew pipe
has to be laid along with the existing one . such an arrangement is known as pipes in
parallel as shown in fig.
fig: pipes in parallel
A little consideration will show that as the pipes are parallel, therefore the loss
of head for all the pipes will be the same and all the pipes will discharge water
idependently .the total discharge through all the pipes will be the same of
discharge in the various pipes.
29