Uploaded by 2021ge5uet

Flow measurement (1)

advertisement
Flow Measurement
Flow Measurement Devices
Devices for Pipe flow (flow under
pressure)
Devices for Open Channels
i.
ii.
iii.
iv.
v.
i. Notches
ii. Weirs
iii. Pitot Tube
Orifices
Mouthpieces
Nozzles
Venturimeter
Pitot Static Tube
Orifice
An orifice is an opening, usually circular, in the side or base of a tank or reservoir,
through which fluid is discharged in the form of a jet, usually into the atmosphere.
• Discharge depends on the Head ‘H’, size, shape and form of orifice.
• Usually sharped edge is provided to reduce friction
Whenever there’s discharge
through the orifice, the
streamlines converge at a
particular section which is
termed as vena contracta.
This contraction depends
on head, shape and size of
orifice.
Classification of Orifice
According to size
According to shape
i.
Small orifice (Do < H/5)
i.
Circular orifice
ii. Large orifice (Do > H/5)
ii.
Rectangular orifice
 An orifice is termed as small when its
size is small compared to head causing
flow. The velocity does not vary
appreciably from top to bottom edge of
the orifice and is assumed to be
uniform.
iii. Square orifice
 The orifice is large if the dimensions are
comparable with the head causing flow.
The variation in the velocity from top to
bottom edge is considerable.
iv. Triangular orifice
Classification of Orifice
According to shape of upstream edge
According to discharge condition
i.
Sharp-edged orifice
i.
Free discharge orifice
ii.
Bell-mouthed orifice
ii.
Submerged orifice
Sharp edged
orifice
Bell mouth
orifice
Square (flat)
orifice
Fully Submerged Orifice
Partially Submerged Orifice
Its inner
Its upstream edge Its upstream edge
(upstream edge of is rounded. Due to is square.
orifice is sharp)
rounded shape
friction is
reduced.
Orifice
Vena Contracta
The Vena Contracta is formed due to convergence of streamlines. The section of the jet
in which the streamlines become parallel and the dia of jet is minimum (even less than
the dia of orifice).
The location is usually at a distance of (N x D) from the wall of tank.
( N is distance coefficient ≈ 0.5)
Hydraulic Coefficients of Orifice
i.
Co-efficient of Contraction (Cc)
ii.
Co-efficient of velocity (Cv)
iii.
Co-efficient of discharge (Cd)
Orifice
Coefficient of Contraction
The ratio between area of jet at Vena Contracta and area of orifice.
Cc =
For circular orifice ⇒ Cc =
πœ‹
4
πœ‹
4
𝐴𝑐
π΄π‘œ
𝐷𝐢2
π·π‘œ
<1
2/D 2)
=
(D
c
o
2
Where,
Dc = Dia. of contracted jet
Do = Dia. of orifice
Generally Cc ≈ 0.64 for sharped edge orifices
but it varies between 0.61-0.69 depending on shape, size and head H over the orifice
Torricelli’s Equation / Theorem
Consider two sections: 1) A at the free surface & 2) B at the
opening on the side near the right bottom of tank as shown.
Let H= Head over the opening causing the flow
v= Velocity of the fluid jet
Applying Bernoulli's eq. at A & B
𝑃
zA + 𝐴
𝛾
+
2
𝑣𝐴
2𝑔
𝑃
= zB + 𝐡
𝛾
zA + 0 + 0 = zB + 0 +
⇒ H=
𝑣 𝐡2
2𝑔
2
𝑣𝐡
+
2𝑔
2
𝑣𝐡
2𝑔
(∡ zA – zB = H)
⇒ vth = 2𝑔𝐻
Torricelli’s equation states that the theoretical velocity is proportional to square root of H
Orifice
Co-efficient of Velocity
The ratio between the actual velocity of jet of fluid at Vena Contracta and the
theoretical velocity of jet.
Cv =
π‘‰π‘Žπ‘π‘‘
π‘‰π‘‘β„Ž
=
π‘‰π‘Žπ‘π‘‘
2π‘”β„Ž
Generally Cv ≈ 0.98 for shaped edge orifices
but it varies between 0.95-0.99 depending on shape, size and head H over the orifice
Orifice
Co-efficient of Discharge
The ratio between the actual discharge from an orifice to the theoretical discharge of
the orifice.
x
Generally Cd for sharp edge orifice
is taken as 0.62, but it varies from
0.61 to 0.65
Experimental Determination of Hydraulic
Coefficients
Co-efficient of Discharge (Cd)
• The water is allowed to flow through an orifice fitted
to a tank under a constant head at H.
• The water is collected in a measuring tank for the
time t.
• The height of water in the measuring tank is
observed and noted.
Qact =
π΄π‘Ÿπ‘’π‘Ž π‘œπ‘“ π‘‘π‘Žπ‘›π‘˜ ∗ π»π‘’π‘–π‘”β„Žπ‘‘ π‘œπ‘“ π‘€π‘Žπ‘‘π‘’π‘Ÿ 𝑖𝑛 π‘‘β„Žπ‘’ π‘‘π‘Žπ‘›π‘˜
π‘‘π‘–π‘šπ‘’ π‘œπ‘“ π‘π‘œπ‘™π‘™π‘’π‘π‘‘π‘–π‘œπ‘›
Cd =
π‘„π‘Žπ‘π‘‘
π‘„π‘‘β„Ž
=
π‘„π‘Žπ‘π‘‘
π΄π‘Ÿπ‘’π‘Ž π‘œπ‘“ π‘œπ‘Ÿπ‘–π‘“π‘–π‘π‘’ ∗ 2𝑔𝐻
Experimental Determination of Hydraulic
Coefficients
Co-efficient of Velocity (Cv)
• Suppose C-C represents the vena contracta of the
jet of water coming out of the orifice under
constant head H.
• Consider a liquid particle is at C-C when time t=0
and it takes the position P along the jet.
Vertical distance = y = ½ gt2
y= ½ g
(x2/V2)
⇒ V=
Vth = 2𝑔𝐻
(t=x/V)
𝑔π‘₯2
2𝑦
Experimental Determination of Hydraulic
Coefficients
Co-efficient of Contraction (Cc)
As we know that:
Cd = Cv x Cc
⇒
Cc =
𝐢𝑑
𝐢𝑣
Mouthpieces/Tubes
• A tube/mouth piece is a short pipe whose length is not more than two or three
times the diameter.
• There is no sharp distinction between a tube and a thick walled orifice.
• A tube may be of uniform diameter or it may diverge
Nozzle
A nozzle is a tube of changing diameter, usually converging as shown in figure if
used for liquids.
Pressure at 1 is P1 & Dia is D1
Pressure at 2 is P2 & Dia is D2
Nozzle
Jet is a stream coming out of a nozzle, orifice or a tube.
Nozzle (Head loss)
z1 +
P1
γ
+
v12
2g
P
= z2 + γ2
+
v22
2g
+ hL = H (head causing flow)
Since z1= z2 & P2 = 0 (atm), v1 =
P1
v12
v22
+ =
γ
2g
2g
2𝑔𝐻
v22
2g
2
+ hL = H
v2 = Cv 2𝑔𝐻
v22
2g
1
⇒
v22=
Cv (2gH)
⇒H=
V 22 x 1
2g Cv2
+ hL = H
+ hL =
V22 x 1
2g Cv2
hL =
V22 x 1
V22
2g Cv2 2g
hL =
V22 x
2g
1
(C 2 - 1)
v
Head loss hL is a function of velocity head &
Co-efficient of velocity of the nozzle.
Venturimeter , Orifice Meter & Pitot Tube
• Already discussed in previous topic
οƒ˜ Pitot tube:
It measures sum of velocity head and pressure head
οƒ˜ Piezometer:
It measures pressure head
οƒ˜ Pitot-Static tube:
It is combination of piezometer and pitot tube.
It can measure velocity head. In the pitot static tube, one
tube is inserted inside the other bent tube. Inner tube acts as
a pitot tube and outer as piezometric tube(s). The outer tube
also has holes transverse to the direction of flow. Sometimes
these tubes are also connected to differential manometer.
Flow measurement in Open Channels
Notches
• Metallic
• Doesn’t Raise W/L on d/s side
• Smaller in size
• Used in labs mostly
Weirs
• Concrete/Masonry structures
• Raises W/L on d/s side
• Bigger in size
• Used in field
Flow measurement in Open Channels
Notch
A notch may be defined as an opening in the side of a tank or vessel such that the liquid
surface in the tank is below the top edge of the opening. A notch may be regarded as an
orifice with the water surface below its upper edge. It is generally made of metallic plate. It
is used for measuring the rate of flow of a liquid through a small channel of tank.
Weir
It may be defined as any regular obstruction in an open stream over which the flow takes
place. It is made of masonry or concrete. The condition of flow, in the case of a weir are
practically same as those of a rectangular notch.
Nappe
The sheet of water flowing through a notch or over a weir
Sill or crest
The top of the weir over which the water flows is known as sill or crest.
Classification of Notches/Weirs
Classification of Notches
According to shape
1.
Rectangular notch
2.
Triangular notch
3.
Trapezoidal Notch
4.
Stepped notch
Classification of Weirs
According to shape
Rectangular weir
Trapezoidal weir (Cippoletti weir)
According to nature of discharge
Ordinary weir
Submerged weir
According to width of weir
Narrow crested weir
Broad crested weir
According to nature of crest
Sharp crested weir
Ogee weir
Discharge over Rectangular Notch/Weir
H= Head of water over the crest
L= Length of Notch or weir
For finding Q, an elementary strip of
thickness dh at depth h from free surface is
selected.
Area of strip= dh x L
&
Vth = 2π‘”β„Ž
The discharge through strip = dQ
The total discharge can be found by
integration between 0 and H.
Discharge over Triangular Notch (V-Notch)
The same procedure is applied for triangular notch as adopted for rectangular one with
different geometry.
Discharge over Trapezoidal Notch
Trapezoidal notch is a combination of a rectangular & triangular notch. Discharge through
trapezoidal notch is a summation of rectangular & triangular notch.
Let,
Cd1 = Co-efficient of discharge for rectangular portion
Cd2 = Co-efficient of discharge for triangular portion
Q = Q1 + Q 2
Discharge over Stepped Notch
Stepped notch is a combination of a rectangular notches.
Problem 1
The head of water over an orifice of diameter 40 mm is 10 cm. Find the actual
discharge and actual velocity of the jet. Take Cd = 0.6 and Cv = 0.98
Problem 2
The head of water over an orifice of diameter 100 mm is 10 m. The water coming out of
the orifice is collected in a circular tank of 1.5 m diameter. The rise of water in this tank is
1 m in 25 seconds. Also the coordinates of the point on the jet, measured from vena
contracta are 4.3 m horizontal and 0.5 m vertical. Find Cd, Cv and Cc
Problem 3
A pipe, 100 mm in diameter has a nozzle attached to it at the discharge end, the
diameter of the nozzle is 50 mm. The rate of discharge of water through the nozzle is 20
litres/s and the pressure at the base of nozzle is 5.886 N/cm2. Calculate Cd. (Assume that
the base of nozzle and outlet of nozzle are at the same elevation)
Problem 4
The head of water over a rectangular notch is 900 mm. The discharge is 300 litres/s.
Find the length of the notch, when Cd = 0.62
Problem 5
Water flows over a rectangular weir 1 m wide at a depth of 150 mm and afterwards
passes through a triangular right angled weir. Taking Cd of rectangular and triangular
weir as 0.62 and 0.59 respectively, find the depth over the triangular weir.
Problem 6
Find the discharge through a trapezoidal notch which is 1m wide at the top and 0.4 m
at bottom & is 30 cm in height. The head of water on the notch is 20 cm. Assume Cd for
rectangular portion = 0.62 while for triangular portion = 0.60
Download