Unit 6 discusses losses in pipes, including major and minor losses. Major losses are due to friction and calculated using Darcy-Weisbach or Chezy's formulas. Minor losses are due to changes in pipe direction, size, or obstructions and are also calculated using specific formulas. The document also discusses equivalent pipes, pipes in series, pipes in parallel, and two and three reservoir pipe flow analysis problems. Head losses are calculated using friction and minor loss formulas, and continuity and energy equations are used to analyze pipe flows.
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.
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.
Flow Through Orifices, Orifice, Types of Orifice according to Shape Size Edge Discharge, Jet, Venacontracta, Hydraulic Coefficients, Coefficient of Contraction,Coefficient of Velocity, Coefficient of Discharge, Coefficient of Resistance, Hydraulic Coefficients by Experimental Method, Discharge Through a Small rectangular orifice, Discharge Through a Large rectangular orifice, Discharge Through a Fully Drowned orifice, Discharge Through Partially Drowned orifice, Mouthpiece and its types. By Engr. M. Jalal Sarwar
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.
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
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
Flow Through Orifices, Orifice, Types of Orifice according to Shape Size Edge Discharge, Jet, Venacontracta, Hydraulic Coefficients, Coefficient of Contraction,Coefficient of Velocity, Coefficient of Discharge, Coefficient of Resistance, Hydraulic Coefficients by Experimental Method, Discharge Through a Small rectangular orifice, Discharge Through a Large rectangular orifice, Discharge Through a Fully Drowned orifice, Discharge Through Partially Drowned orifice, Mouthpiece and its types. By Engr. M. Jalal Sarwar
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.
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
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
Head losses
Major Losses
Minor Losses
Definition • Dimensional Analysis • Types • Darcy Weisbech Equation • Major Losses • Minor Losses • Causes Head Losses
3. • Head loss is loss of energy per unit weight. • Head = Energy of Fluid / Weight • Head losses can be – Kinetic Head – Potential Head – Pressure Head 6/10/2015 4Danial Gondal Head Loss
4. • Kinetic Head – K.H. = kinetic energy / Weight = v² /2g • Potential Head – P.H = Potential Energy / Weight = mgz /mg = z • Pressure Head – P.H = P/ ρ g 6/10/2015 5
5. • (P/ ρ g) + (v² /2g ) + (z) = constant • (FL-2F-1L3LT-2L-1T2) + (L2T-2L1T2)+(L) = constant • (L) + (L) + (L) = constant • As L represent height so it is dimensionally L. 6/10/2015 6 Dimensional Analysis
6. • However the equation (P/ ρ g) + (v² /2g ) + (z) = constant Is valid for Bernoulli's Inviscid flow case. As we are studying viscous flow so (P1/ ρ g) + (v1² /2g ) + (z1) = EGL1(Energy Grade Line At point 1) (P2/ ρ g) + (v2² /2g ) + (z2) = EGL2(Energy Grade Line At point 2) 6/10/2015 7 Head Loss
7. • For Inviscid Flow EGL1 - EGL2= 0 • For Viscous Flow EGL1 - EGL2= Hf 6/10/2015 8 Head Loss
8. MAJOR LOSSES IN PIPES
9. •Friction loss is the loss of energy or “head” that occurs in pipe flow due to viscous effects generated by the surface of the pipe. • Friction Loss is considered as a "major loss" •In mechanical systems such as internal combustion engines, it refers to the power lost overcoming the friction between two moving surfaces. •This energy drop is dependent on the wall shear stress (τ) between the fluid and pipe surface. 6/10/2015 10 Friction Loss
10. •The shear stress of a flow is also dependent on whether the flow is turbulent or laminar. •For turbulent flow, the pressure drop is dependent on the roughness of the surface. •In laminar flow, the roughness effects of the wall are negligible because, in turbulent flow, a thin viscous layer is formed near the pipe surface that causes a loss in energy, while in laminar flow, this viscous layer is non-existent. 6/10/2015 11 Friction Loss
11. Frictional head losses are losses due to shear stress on the pipe walls. The general equation for head loss due to friction is the Darcy-Weisbach equation, which is where f = Darcy-Weisbach friction factor, L = length of pipe, D = pipe diameter, and V = cross sectional average flow velocity.
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1. Unit-6:
Losses in Pipes
SYLLABUS:
A. Major and Minor Losses, Darcy-Wiesbach Equation, Concept of Equivalent Pipe,
Dupit’s Equation.
B. Pipes in Series, Parallel and Syphon, Two Reservoir Problems, Three Reservoir
Problems Concept of Water hammer. Surge Tanks (Function, Location and Uses).
2. FLOW THROUGH PIPE
• A pipe is a closed conduit (generally of circular section)
which is used for carrying fluids under pressure. The flow
in a pipe is termed pipe flow only when the fluid
completely fills the cross-section and there is no free
surface of fluid. The pipe running partially full (in such a
case atmospheric pressure exists inside the pipe)
behaves like an open channel.
3. LOSS OF ENERGY (OR HEAD) IN PIPES
• When water flows in a pipe, it experiences some resistance to its motion, due
to which its velocity and ultimately the head of water available is reduced.
This loss of energy (or head) is classified as follows :
A. Major Energy Losses
• This loss is due to friction.
B. Minor Energy Losses
• These losses are due to :
1. Sudden enlargement of pipe,
2. Sudden contraction of pipe,
3. Bend of pipe,
4. An obstruction in pipe,
5. Pipe fittings, etc.
4. MAJOR ENERGY LOSSES
• These losses which are due to friction are calculated by :
1. Darcy-Weisbach formula
2. Chezy’s formula.
17. Equivalent Pipe
• Equivalent pipes refer to imaginary pipes which are used
to determine the head loss and flow of discharge
considering that the flow of discharge and head loss in the
actual piping system is same as that of the equivalent
pipe. It is a technique used to decrease the large number
of attached pipe systems into an individual pipe system
such that the piping system analysis can be made easier.
• In equivalent pipe structure, the major properties of pipe
such as length of pipe, diameter of pipe and roughness
factor of pipe are required to do the analysis.
18.
19.
20.
21.
22. 4.6 Pipe Flow Analysis
•Pipeline system used in water distribution, industrial
application and in many engineering systems may
range from simple arrangement to extremely
complex one.
•Problems regarding pipelines are usually tackled by
the use of continuity and energy equations.
•The head loss due to friction is usually calculated
using the D-W equation while the minor losses are
computed using equations depending on the
appropriate conditions.
23. 4.6.2 Pipes in Series
▪ When two or more pipes of different
diameters or roughness are connected in
such a way that the fluid follows a single
flow path throughout the system, the
system represents a series pipeline.
▪ In a series pipeline the total energy loss
is the sum of the individual minor losses
and all pipe friction losses.
Pipelines in
series
24. ▪ Referring to Figure the Bernoulli equation can be written between points 1 and 2 as follows;
where P/ρg = pressure head
z = elevation head
V2/2g = velocity head
HL1-2 = total energy lost between point 1 and 2
Realizing that P1=P2=Patm, and V1=V2, then equation reduces to
z1-z2 = HL1-2
Or we can say that the different of reservoir water level is equivalent to the total head losses in the system.
The total head losses are a combination of the all the friction losses and the sum of the individual minor
losses.
HL1-2 = hfa + hfb + hentrance + hvalve + hexpansion + hexit.
Since the same discharge passes through all the pipes, the continuity equation can be written as;
Q1 = Q2
25. 4.6.3 Pipes in Parallel
Pipelines in parallel
• A combination of two or more pipes
connected between two points so that
the discharge divides at the first
junction and rejoins at the next is
known as pipes in parallel. Here the
head loss between the two junctions is
the same for all pipes.
26. ▪ Applying the continuity equation to the system;
Q1 = Qa + Qb = Q2
▪ The energy equation between point 1 and 2 can be written as;
▪ The head losses throughout the system are given by;
HL1-2=hLa = hL
▪ Equations are the governing relationships for parallel pipe line systems. The system
automatically adjusts the flow in each branch until the total system flow satisfies
these equations.