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2 Fluid Statics

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Technological Institute of the Philippines
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
CE 023
Fluid Mechanics
Technological Institute of the Philippines
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Pressure
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
Pressure- or unit pressure, is defined as the normal force per unit area exerted by a solid, liquid or gas over a
𝑑𝐹
surface. 𝑝 =
𝑑𝐴
𝑑𝐹
𝑝=
𝑑𝐴
Unit pressure
𝑑𝐹 𝐹
𝑝=
=
𝑑𝐴 𝐴
Uniform or average pressure
Technological Institute of the Philippines
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Pascal’s Law
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
Pascal’s Law- states that the intensity of the pressure acting at a point in a fluid at rest (or moving in constant
velocity) is the same in all directions, stated by a French Mathematician Blaise Pascal in 17th century.
𝐹𝑦 − π‘Š − 𝐹𝑁 cos πœƒ = 0
+↑
𝐹𝑉 = 0 𝑝 𝑑π‘₯(𝑑𝑧) − 0 − 𝑝 𝑑𝑠(𝑑𝑧) cos πœƒ = 0
𝑦
𝑁
𝑑𝐹
𝑝=
𝑑𝐴
𝐹𝑁
𝐹π‘₯
π‘Š
𝑑𝑦 𝑑𝑠
𝑑π‘₯
𝑑π‘₯ = 𝑑𝑠 cos πœƒ
𝑑𝑦 = 𝑑𝑠 sin πœƒ
𝐹𝑦
+→
𝑝𝑦 (𝑑𝑠 cos πœƒ)(𝑑𝑧) − 0 − 𝑝𝑁 𝑑𝑠(𝑑𝑧) cos πœƒ = 0
𝑝𝑦 − 0 − 𝑝𝑁 = 0
𝑝𝑦 = 𝑝𝑁
𝐹π‘₯ − 𝐹𝑁 sin πœƒ = 0
𝐹𝐻 = 0 𝑝 𝑑𝑦(𝑑𝑧) − 𝑝 𝑑𝑠(𝑑𝑧) sin πœƒ = 0
π‘₯
𝑁
𝑝π‘₯ (𝑑𝑠 sin πœƒ)(𝑑𝑧) − 𝑝𝑁 𝑑𝑠(𝑑𝑧) sin πœƒ = 0
𝑝π‘₯ − 𝑝𝑁 = 0
πœƒ
𝑝π‘₯ = 𝑝𝑦 = 𝑝𝑁
𝑝π‘₯ = 𝑝𝑁
Technological Institute of the Philippines
Absolute and Gage Pressure
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
π‘Žπ‘π‘ π‘œπ‘™π‘’π‘‘π‘’ π‘π‘Ÿπ‘’π‘ π‘ π‘’π‘Ÿπ‘’ (π‘π‘Žπ‘π‘  )
π‘”π‘Žπ‘”π‘’
π‘”π‘Žπ‘”π‘’
π‘π‘Ÿπ‘’π‘ π‘ π‘’π‘Ÿπ‘’ π‘π‘Ÿπ‘’π‘ π‘ π‘’π‘Ÿπ‘’
(π‘π‘”π‘Žπ‘”π‘’ )
(π‘π‘”π‘Žπ‘”π‘’ )
π‘£π‘Žπ‘π‘’π‘’π‘š
π‘œπ‘Ÿ π‘ π‘’π‘π‘‘π‘–π‘œπ‘›
Absolute pressure- is the intensity of pressure that is measured above the absolute zero pressure (lowest
possible pressure) and can never be negative in value.
Atmospheric pressure- is the prevailing pressure in the air surrounding which decreases with increasing
altitude.
Standard atmospheric pressure- is the absolute pressure that is measured at sea level and at a temperature of
15°C (59°F) equivalent to 101.325 kPa or 14.7 psi or 760 mm Hg or 29.9 in. Hg or 2116 lb/ft2 or 1 atmosphere
(atm)
Gage pressure- or relative pressure, is the pressure that is measured above or below the atmospheric pressure.
π‘π‘”π‘Žπ‘”π‘’ = π‘π‘Žπ‘π‘  − π‘π‘Žπ‘‘π‘š
π‘Žπ‘‘π‘šπ‘œπ‘ π‘β„Žπ‘’π‘Ÿπ‘–π‘ π‘π‘Ÿπ‘’π‘ π‘ π‘’π‘Ÿπ‘’
π‘π‘”π‘Žπ‘”π‘’ = π‘π‘Žπ‘π‘  − π‘π‘Žπ‘‘π‘š
π‘Žπ‘π‘ π‘œπ‘™π‘’π‘‘π‘’ π‘§π‘’π‘Ÿπ‘œ π‘π‘Ÿπ‘’π‘ π‘ π‘’π‘Ÿπ‘’
(π‘π‘’π‘Ÿπ‘“π‘’π‘π‘‘ π‘£π‘Žπ‘π‘’π‘’π‘š)
Technological Institute of the Philippines
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
Static Pressure Variation in Incompressible Fluids
𝐹1 1
𝑦
π‘₯
πœƒ
π‘Š
β„Ž
β„Ž
cos πœƒ =
𝐿
+β†˜
𝐹π‘₯ = 0
2
𝑑𝐹
𝑝=
𝑑𝐴
𝐹2
π‘Š
𝛾=
𝑉
𝐹1 + π‘Š cos πœƒ − 𝐹2 = 0
𝑝1 𝑑𝐴 + 𝛾𝐿 𝑑𝐴 cos πœƒ − 𝑝2 𝑑𝐴 = 0
𝑝1 + π›Ύβ„Ž − 𝑝2 = 0
𝑝2 − 𝑝1 = π›Ύβ„Ž
π’‘πŸ − π’‘πŸ = πœΈπ’‰
The difference in pressure between any two points in a homogeneous
fluid at rest is equal to the product of the unit weight of the fluid and their
difference in elevation(vertical distance between the points)
′
′
𝑝
− 𝑝1 − 𝑑𝑝 = π›Ύβ„Ž
2
𝑝1 = 𝑝1 + 𝑑𝑝
′
𝑝
2 = 𝑝1 + π›Ύβ„Ž + 𝑑𝑝
[𝑝2 − 𝑝1 = π›Ύβ„Ž]
′
𝑝
= 𝑝2 + 𝑑𝑝
2
𝑝2 ′ − (𝑝1 + 𝑑𝑝) = π›Ύβ„Ž
π’‘πŸ = π’‘πŸ + πœΈπ’‰
Any change in pressure applied at any point in a liquid at rest is
transmitted equally and undiminished to every other point in the liquid.
𝐹1 1
𝑝2 = π‘π‘Žπ‘‘π‘š + π›Ύβ„Ž
𝑝2 = 𝑝1 + π›Ύβ„Ž
πœƒ
𝑝2 = π›Ύβ„Ž
[π‘π‘”π‘Žπ‘”π‘’ = π‘π‘Žπ‘π‘  − π‘π‘Žπ‘‘π‘š ]
π‘Š
𝒑 = πœΈπ’‰
β„Ž
The pressure at any point below a
free liquid surface is equal to the
product of the unit weight of the fluid
β„Ž
and its vertical distance from the free
2
cos πœƒ =
𝐹2
𝐿
liquid surface.
Technological Institute of the Philippines
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
Static Pressure Variation in Incompressible Fluids
𝐹1 1
𝑦
π‘₯
πœƒ
𝑦
+β†˜
𝐹π‘₯ = 0
π‘₯
π‘Š
π‘Š
β„Ž
β„Ž
cos πœƒ =
𝐿
+→
2
𝑑𝐹
𝑝=
𝑑𝐴
𝐹1
2
1
𝐿
𝐹2
π‘Š
𝛾=
𝑉
𝐹1 + π‘Š cos πœƒ − 𝐹2 = 0
𝑝1 𝑑𝐴 + 𝛾𝐿 𝑑𝐴 cos πœƒ − 𝑝2 𝑑𝐴 = 0
𝑝1 + π›Ύβ„Ž − 𝑝2 = 0
𝑝2 − 𝑝1 = π›Ύβ„Ž
𝐹2
𝐹1 1
πœƒ
π‘Š
β„Ž
β„Ž
cos πœƒ =
𝐿
2
𝐹2
𝐹π‘₯ = 0 𝑝 =
𝑑𝐹
𝑑𝐴
𝐹1 − 𝐹2 = 0
𝑝1 𝑑𝐴 − 𝑝2 𝑑𝐴 = 0
[𝑝2 = 𝑝1 + π›Ύβ„Ž]
𝑝1 − 𝑝2 = 0
𝑝2 = 𝑝1 + 𝛾(0)
𝑝1 = 𝑝2
𝑝1 = 𝑝2
The pressures along the same
horizontal plane in a homogeneous
fluid at rest are equal
𝑝2 = π‘π‘Žπ‘‘π‘š + π›Ύβ„Ž
𝑝2 = 𝑝1 + π›Ύβ„Ž
𝑝2 = π›Ύβ„Ž
[π‘π‘”π‘Žπ‘”π‘’ = π‘π‘Žπ‘π‘  − π‘π‘Žπ‘‘π‘š ]
𝒑 = πœΈπ’‰
The pressure at any point below a
free liquid surface is equal to the
product of the unit weight of the fluid
and its vertical distance from the free
liquid surface.
Technological Institute of the Philippines
Pressure Head
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
Pressure Head- is the height of a column of homogeneous fluid that will produce a given intensity of pressure
(gage).
𝑝
𝑝 = π›Ύβ„Ž
β„Ž=
𝛾
Given a pressure of magnitude of 50 kPa, find the pressure head of water
with a unit weight of 9.81 kN/m3 and the pressure head of mercury with a
unit weight of 133 kN/m3.
𝑝
β„Ž=
𝛾
𝑝
50 π‘₯ 103 𝑁/π‘š2
= 5.10 π‘š
β„Žπ‘€ =
=
3
3
𝛾𝑀
9.81 π‘₯10 𝑁/π‘š
β„Žπ»π‘”
𝑝
50 π‘₯103 𝑁/π‘š2
= 0.376 π‘š
=
=
3
3
𝛾𝐻𝑔 133 π‘₯10 𝑁/π‘š
Technological Institute of the Philippines
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Sample Problems:
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
1. The underground storage tank used in a service station contains gasoline filled to the level A. Determine the
gage pressure at each of the five identified points. Note that point B is located in the stem, and point C is just
π‘˜π‘”
below it in the tank. Take πœŒπ‘” = 730 3.
π‘š
Solution:
𝑝𝐷 = 𝑝𝐴 + 𝛾𝑔 β„Ž
𝑝 = 0 π‘˜π‘ƒπ‘Ž
𝐴
[𝑝2 = 𝑝1 + π›Ύβ„Ž]
π‘˜π‘”
𝑝𝐷 = 0 + 730 3
π‘š
𝑝𝐡 = 𝑝𝐴 + 𝛾𝑔 β„Ž
π‘˜π‘”
π‘š
𝑝𝐡 = 0 + 730 3 9.81 2 1 π‘š
π‘š
𝑠
𝑁
𝑝𝐡 = 7161.3 2 = 7.1613 π‘˜π‘ƒπ‘Ž
π‘š
π‘š
9.81 2
𝑠
1π‘š+2π‘š
𝑁
𝑝𝐷 = 21,483.9 2 = 21.4839π‘˜π‘ƒπ‘Ž
π‘š
𝑝𝐸 = 𝑝𝐷 = 21.4839π‘˜π‘ƒπ‘Ž
𝑝𝐢 = 𝑝𝐡 = 7.1613 π‘˜π‘ƒπ‘Ž
Recall:
Any change in pressure applied at any point in a liquid at rest is transmitted equally and undiminished to every
other point in the liquid.
The pressures along the same horizontal plane in a homogeneous fluid at rest are equal
Technological Institute of the Philippines
Measurement of Static Pressure
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
Barometer- is a device for measuring intensities of pressure exerted by the atmosphere. It was invented in the
mid-17th century (1643) by Evangelista Torricelli, using mercury as a preferred fluid, since it has a high
density and a very small vapor pressure.
[𝑝2 = 𝑝1 + π›Ύβ„Ž]
𝑝𝐡 = 𝑝𝐴 + 𝛾𝐻𝑔 β„Ž
π‘˜π‘
101.325 π‘˜π‘ƒπ‘Ž = 0 + 133.29 3 β„Ž
π‘š
β„Ž = 0.760 π‘š = 760 π‘šπ‘š = 29.9 𝑖𝑛
Technological Institute of the Philippines
Measurement of Static Pressure
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
Manometer- is a device consists of a transparent tube that is used to determine the gage pressure in a liquid.
Types of Manometer
Open Type- a manometer with an atmospheric surface in one end and capable of
measuring gage pressures.
Piezometer- is the simplest type of manometer which consist of a tube which is
open at one end to the atmosphere, while the other end is inserted into a vessel,
where the pressure of a liquid is to be measured.
U-tube Manometer- consist of a tube, usually bent in the form of a U, containing a
liquid of known specific gravity, the surface of which moves proportionally to changes
of pressure.
Differential Type- a manometer without an atmospheric surface and
capable of measuring only differences of pressure.
Differential Manometer- is used to determine the difference in pressure
between two points in a closed fluid system.
Technological Institute of the Philippines
Measurement of Static Pressure
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
Bourdon Gage- this gage consists of a coiled metal tube that
is connected at one end to the vessel where the pressure is
to be measured. The other end of the tube is closed so that
when the pressure in the vessel is increased, the tube
begins to uncoil and respond elastically. Using the
mechanical linkage attached to the end of the tube, the dial
on the face of the gage gives a direct reading of the pressure,
which can be calibrated in various units, such as kPa or psi.
Pressure Transducers- an electromechanical device that can
be used to measure pressure as a digital readout. When end
A is connected to a pressure vessel, the fluid pressure will
deform the thin diaphragm. The resulting strain in the
diaphragm is then measured using the attached electrical
strain gage.
Technological Institute of the Philippines
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Sample Problems:
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
2. The funnel is filled with oil and water to the levels shown. Determine the depth of oil β„Ž′ that must be in the
π‘˜π‘”
funnel so that the water remains at a depth C, and the mercury level made h = 0.8 m. Take πœŒπ‘œ = 900 3, πœŒπ‘€ =
π‘˜π‘”
1000 3,
π‘š
Solution:
πœŒπ»π‘” =
π‘š
π‘˜π‘”
13,550 3 .
π‘š
[𝑝2 = 𝑝1 + π›Ύβ„Ž]
𝑝𝐡 = 𝑝𝐴 + π›Ύπ‘œ β„Ž′
𝑝𝐢 = 𝑝𝐡 + 𝛾𝑀 (0.4)
𝑝𝐢 = (𝑝𝐴 + π›Ύπ‘œ β„Ž′) + 𝛾𝑀 (0.4)
𝑝𝐷 = 𝑝𝐢 − 𝛾𝐻𝑔 [ 0.2 + β„Ž′ + 0.4 − 0.8]
𝑝𝐷 =
0=
𝑝𝐴 + π›Ύπ‘œ β„Ž′ + 𝛾𝑀 0.4 − 𝛾𝐻𝑔 [ 0.2 + β„Ž′ + 0.4 − 0.8]
π‘˜π‘” ′
π‘˜π‘”
0 + 900 3 β„Ž + 1000 3
π‘š
π‘š
β„Ž′ = 0.2458 π‘š = 246 π‘šπ‘š
0.4
π‘˜π‘”
− (13,550 3 )[ 0.2 + β„Ž′ + 0.4 − 0.8]
π‘š
Technological Institute of the Philippines
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Static Pressure Variation in Compressible Fluids
[π‘π‘Žπ‘π‘  = πœŒπ‘…π‘‡π‘Žπ‘π‘  ] [𝛾 = πœŒπ‘”]
𝑝
𝑔 π‘‘β„Ž
𝑅𝑇
𝑑𝑝
𝑔
=−
π‘‘β„Ž
𝑝
𝑅𝑇
𝑑𝑝 = −
𝑝1
1
𝑝1 − 𝑝2 = 𝑑𝑝 = −𝛾 π‘‘β„Ž π‘‘β„Ž
𝑝2 2
π‘šπ‘’π‘Žπ‘› π‘ π‘’π‘Ž 𝑙𝑒𝑣𝑒𝑙
𝑝1
𝑝2
𝑑𝑝
=
𝑝
β„Ž1
−
β„Ž2
𝑔
π‘‘β„Ž
𝑅𝑇
π‘Žπ‘ π‘ π‘’π‘šπ‘’ 𝑇 = π‘π‘œπ‘›π‘ π‘‘π‘Žπ‘›π‘‘(π‘–π‘ π‘œπ‘‘β„Žπ‘’π‘Ÿπ‘šπ‘Žπ‘™)
𝑔
ln 𝑝1 − ln 𝑝2 = −
(β„Ž1 − β„Ž2 )
𝑅𝑇
𝑝1
𝑔
ln
=−
β„Ž1 − β„Ž2
𝑝2
𝑅𝑇
𝑝1
−
=𝑒
𝑝2
−
𝑝1 = 𝑝2 𝑒
𝑔
𝑅𝑇 β„Ž1 −β„Ž2
𝑔
𝑅𝑇 β„Ž1 −β„Ž2
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
Technological Institute of the Philippines
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Sample Problems:
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
3. The natural gas in the storage tank is contained within a flexible membrane and held under constant
pressure using a weighted top that is allowed to move up or down as the gas enters or leaves the tank as shown
in the figure. Determine the required weight of the top if the (gage) pressure at the outlet A is to be 600 kPa.
π‘˜π‘”
𝐽
The gas has a temperature of 20°C, πœŒπ‘” = 0.665 3 and 𝑅 = 518.3
.
π‘š
π‘˜π‘”−𝐾
Solution:
π‘Žπ‘ π‘ π‘’π‘šπ‘’ π‘π‘œπ‘šπ‘π‘Ÿπ‘’π‘ π‘ π‘–π‘π‘™π‘’ π‘”π‘Žπ‘ :
+↑
𝐹𝑉 = 0
𝑑𝐹
𝑝=
𝑑𝐴
π‘“π‘œπ‘Ÿ 𝑇 = π‘π‘œπ‘›π‘ π‘‘π‘Žπ‘›π‘‘(π‘–π‘ π‘œπ‘‘β„Žπ‘’π‘Ÿπ‘šπ‘Žπ‘™)
𝑝𝐡 =
𝑔
− 𝑅𝑇 β„Ž1 −β„Ž2
𝑝𝐴 𝑒
9.81
−
30−0
3
101.325)10 )𝑒 (518.3)(20+273.15)
πœ‹
𝑝𝐡 = ((600 +
π‘Š = (202 )𝑝𝐡
4
𝑝𝐡 = 598,642.881 π‘ƒπ‘Ž
π‘Žπ‘ π‘ π‘’π‘šπ‘’ π‘–π‘›π‘π‘œπ‘šπ‘π‘Ÿπ‘’π‘ π‘ π‘–π‘π‘™π‘’ π‘”π‘Žπ‘ :
πœ‹
𝑝𝐴 = 𝑝𝐡 + 𝛾𝑔 β„Ž
π‘Š = 202 𝑝𝐡 = 188,069.2077 π‘˜π‘
4
π‘˜π‘”
600π‘₯103 π‘ƒπ‘Ž = 𝑝𝐡 + (0.665 3 )(9.81)(30 π‘š)
π‘š
π‘Žπ‘ π‘ π‘’π‘šπ‘’ π‘π‘œπ‘›π‘ π‘‘π‘Žπ‘›π‘‘ π‘”π‘Žπ‘  π‘π‘Ÿπ‘’π‘ π‘ π‘’π‘Ÿπ‘’:
𝑝𝐡 = 599,804.2905 π‘ƒπ‘Ž
𝑝𝐴 = 𝑝𝐡
πœ‹
πœ‹
π‘Š = 202 𝑝𝐡 = 188,434.0753 π‘˜π‘
π‘Š = 202 (600) = 188,495.5592 π‘˜π‘
4
4
Technological Institute of the Philippines
Sample Problems:
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
4. Determine the difference in pressure 𝑝𝐡 − 𝑝𝐴 between the centers A and B of the pipes, which are filled
with water. The mercury in the inclined-tube manometer has the level shown 𝑆𝐻𝑔 = 13.55
Solution:
[𝑝2 = 𝑝1 + π›Ύβ„Ž]
𝑝𝐴 + 9810 0.1 + 13.55 9810 0.25 − 0.1 − 9810(0.25) = 𝑝𝐡
𝑝𝐡 − 𝑝𝐴 = 18,467.325 π‘ƒπ‘Ž
Technological Institute of the Philippines
938 Aurora Blvd., Cubao, Quezon City
College of Engineering and Architecture
Department of Civil Engineering
Sample Problems:
Prepared by: Engr. Adams Royce A. Dionisio, RCE
Structural Engineer
5. A 0.5-in.-diameter bubble of methane gas is released from the bottom of a lake. Determine the bubble’s
𝑙𝑏
diameter when it reaches the surface. The water temperature is 68°F and the atmospheric pressure is 14.7 2
𝑖𝑛
Solution:
π‘Žπ‘‘ π‘‘β„Žπ‘’ π‘ π‘’π‘Ÿπ‘“π‘Žπ‘π‘’:
π‘Žπ‘‘ π‘‘β„Žπ‘’ π‘π‘œπ‘‘π‘‘π‘œπ‘š:
π‘š
[π‘π‘Žπ‘π‘  = πœŒπ‘…π‘‡π‘Žπ‘π‘  ] [𝑝2 = 𝑝1 + π›Ύβ„Ž] 𝜌 =
𝑉
𝑙𝑏
𝑙𝑏
14.7 2 + 62.4 3 20 𝑓𝑑
𝑖𝑛
𝑓𝑑
1 𝑓𝑑
12 𝑖𝑛.
𝑙𝑏
𝑙𝑏
14.7 2 + 62.4 3 20 𝑓𝑑
𝑖𝑛
𝑓𝑑
1 𝑓𝑑
12 𝑖𝑛.
2
π‘š
=
π‘…π‘‡π‘Žπ‘π‘ 
𝑉𝑏
2
𝑉𝑏 = π‘šπ‘…π‘‡π‘Žπ‘π‘ 
𝑙𝑏
π‘š
14.7 2 =
π‘…π‘‡π‘Žπ‘π‘ 
𝑖𝑛
𝑉𝑠
𝑙𝑏
14.7 2 (𝑉𝑠 ) = π‘šπ‘…π‘‡π‘Žπ‘π‘ 
𝑖𝑛
𝑙𝑏
𝑙𝑏
14.7 2 + 62.4 3 20 𝑓𝑑
𝑖𝑛
𝑓𝑑
14.7 + 62.4 20
𝑑𝑠 = 0.5835 𝑖𝑛
1
12
2
2
1 𝑓𝑑
12 𝑖𝑛.
4
0.5
πœ‹
3
2
3
𝑙𝑏
𝑉𝑏 = 14.7 2 (𝑉𝑠 )
𝑖𝑛
4
𝑑𝑠
= 14.7 πœ‹
3
2
3
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