Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Chapter 2
Fluid Statics CLO2: Describe the concept of fluid statics in pressure measurement and buoyancy force determination
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Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Outline • Definition of fluid statics • Hydrostatic Equilibrium • Barometric equation • Pressure measurement: Principle and devices • Buoyancy
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Learning Outcome • At the end of this chapter, you should be able to: – Define the term “fluid statics” statics” – Calculate – Calculate pressure using manometers – Determine – Determine buoyancy force – Apply – Apply the fluid statics principle to the chemical engineering unit operations.
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
What Is Fluid Statics? Fluid statics (also called hydrostatics) hydrostatics) is the science of fluids dealing with forces applied by fluids at rest or in rigidbody motion*
No shear stresses involved The only forces develop on the surfaces of the particles will be due to pressure.
Application of fluids statics 1. Manometers 2. Cont Contin inuo uous us grav gravit ity y deca decant nter er 3. Centrifu ifugal dec decanter ter 4. De Dete term rmin inat atio ion n bu buoy oyan ancy cy fo forc rcee 5. others (*Rigid (*Rigid body motion - fluid that that is moving moving in such a manner manner that there there is no
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Fluid Statics
• Example: – Water – Water in a tank. – Water – Water in a lake (Water actually move very slowly in the lake. However the movement of water relative to each other is nearly zero that water is seen as “static”) “st atic”)
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Pressure It can be defined as a normal force exerted by a fluid per unit area. It has the unit of Newtons Newtons per square meter (N/m2) which which is called called a pasca pascall (Pa) Types of pressure defined in fluid mechanics: • Absolute pressure (P (Pabs): actual pressure at given position • Gage pressure (P (Pgage): Pabs - Patm ( Pvac): Patm-Pabs • Vacuum pressure (P
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Absolute, Gage and Vacuum pressures
Pgage Pabs
Pvac Patm
Patm Pabs
Absolute vacuum, P abs = 0
Pabs = Patm + Pgage
Absolute vacuum, Pabs = 0
Pabs = Patm – P – Pvac
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Atmospheric Pressure
• Highest recorded Patm 108.6 kPa (Tosontsengel, Mongolia, 19 December 2001)
• Lowest Lowest reco recorde rded d non-tor non-tornad nadic ic Patm 87.0 kPa (Western Pacific during Typhoon Tip, 12 October 1979)
In Fluid Mechanics: • Patm = 1 atm atm = 10 101. 1.32 325 5 kPa kPa = 14 14.7 .7 psi psi • Some devices devices uses uses 100 100 kPa (or 1 bar) as atmospheric pressure.
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Class Example 1
a) A vacu vacuum um gag gage e conn connect ected ed to to a cham chamber ber reads reads 24 24 kPa at location location where where the local local atmospher atmospheric ic pressure is 92 kPa. Determine Pabs. b) If the the abso absolut lute e press pressure ure in in a tank tank is 20 20 psi psi at at norma normall atmospheric pressure, determine Pgage. c) Gage Gage pres pressu sure re rea readin dings gs show showss a val value ue of – of – 60 60 kPa. What does it means? And, determine Pabs.
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Solution
Class Example 1: Solution
a) Pgauge = 24 kPa, Patm = 92 kPa Pabs = 24 + 92 = 116 kPa b) Pgauge
= Pabs - Patm = 20-14.7 = 5.3 psi c) Pgage = – 60 – 60 kPa It means vacuum since the value is negative. (The same if mention as Pvac = 60 kPa) Pabs = Pgauge+Patm = 101.3 – 101.3 – 60 60 = 41.3 kPa
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
• In a stationary fluid the pressure is exerted equally in all directions and is referred to as the static pressure.
P1
P3
P4
P2
An element of fluid
Fluid
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Pressure Variation in a Fluid at Rest • •
Fluid pressure at a point is the same in all directions (Pascal’s Law) In a fluid at rest the pressure intensities in a horizontal plane are equal
Since fluid is at rest, there is no accelerations, and hence, Newton’s Laws of motion sum of the forces f orces on any part of the fluid in any direction is zero Let us consider the z direction, direction, opposite the direction of gravity. gravity. The sum of forces (positive upward):
Pz= z z = z
F bottom – F top – F weight = 0 We can write,
z=0 x
(P z=0) x y - (P z=z ) x y – ρg x y z = 0 ………(1)
W
y
Pz=0 forces acting acting Fig. Surface and body forces
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Dividing equation 1 by x y z and rearranging, we find
P z=z ─ P z=0 z
Pz= z
ρg = ─ ρg
z = z
If we now let z approach zero, then
limit z
dP P = ─ ρg ρg = ─ = ─ γ = dz 0 z
z=0 x W
This is the basic equation of fluid statics, called the Barometric equation
y
Pz=0
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Pressure Pres sure-- depth relations relationships hips for incompres incompressible sible fluids fluids What is incompressible fluids??
In fluid mechanics, mechanics, an incompressible fluid is a fluid that does not change the volume (e.g., density) of the fluid due to external pressure.. Incompress pressure Incompressible ible fluids fluids are a hypothetical type of fluids, fluids , which are introduced for the convenience of calculations. The compressibility of an incompressible fluid is always zero
Example: water
What is the difference between Compressible Fluids and Incompressible Fluids ?
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
PressurePressur e- depth relationships relationships for incompressible incompressible fluids Assumption: Assumption: g is constant We can write barometric equation can be directly integrated
2
1
2
dz dz
dP
1
P1 = Patm 1
z1
z
2
to yield
h y
1
P2 P1 z 2 z1 or
P2 P1 ( z 1 z 2 )
or
P 2
P 1 h
z2
2
P2
x
v ariation in a Fig. Notation for pressure variation fluid at rest with a free surface
Pressure in a liquid at rest increases linearly with distance from the free surface
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Pressure Pres sure-- depth relations relationships hips for incompres incompressible sible fluids fluids Ps z=h
Ps
P
Ps
h
dP
dz 0
P h P P h s
z=0
• For free surface Ps = Patm • Normally take Ps = 0 (Pgage definition) • P = h = Pgage • P increase as one go downward. • P decrease as one go upward.
P
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Pressure at the same elevation
At same elevation, pressure is the same for the same fluid at rest.
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Class Example 2
Find the pressure at the bottom of a tank containing glycerin under pressure shown (glycerin = 12.34 N/m3)
Solu Solutti on: Assumption: Assumption: glycerin is an incompressible fluid
Pbottom = Ps + h = 50 + (12.34)(2) = 74.68 kPa
50 kPa
2m
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Class Example 3 Determine the pressure at the bottom of an open tank containing water at atmospheric pressure. Ps = Patm
Solution: Ass A ssum ump pti on: water is an incompressible fluid
P bottom = Ps + gh = Ps + (1000)(9.81)(10) If we measure the pressure relative to atmospheric pressure (gage pressure),It follows that Ps = 0, therefore, P bottom = 98. 98.1 1 kPa kPa (gag (gage) e)
10 m
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Compressible Fluid Density change with pressure
Example; Ideal/perfect gases
The equation of state for ideal gas is
P RT
PM R u T
P M Ru R T
= absulate absulate pressure pressure (kPa) (kPa) = molar mass (kg/kmol) = Universal Universal gas gas constant constant (J/mol (J/mol K) = Gas constant (kJ/kg K) = absolute temperature (K)
Substituting above equation for density in Barometric equation, we find
dP dz
PM R u T
g …………….(1)
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
If the temperature is constant, equation 1 can be separated and integrated as follows:
2
1
ln
dP P P 2 P 1
gM R u T gM w R u T
2
1
dz
( z 2 z 1 )
gM w z 2 z1 P2 P1 exp R u T
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Pressure Measurement • Objective: • Understand the principles of manometer u sing • Learn how to calculate pressure using manometer
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
In measuring pressure: • Pressure increases as one go downward • In calculation, has to “plus” the pressure
A
B
• Pressure decreases as one go upward • In calculation, has to “minus” the pressure
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Measurement of Pressure Barometer : (Mercury Barometer) A barometer is used to measure atmospheric pressure
• A simple barometer consists of: – a tube more than 30 inch (760 mm) long – inserted in an open container of mercury – a closed and evacuated end pointing upward – open end in the mercury pool – mercury extending from the container up into the tube. – It contains mercury vapor at its saturated vapor pressure
P2
P1
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
P vapor
Measurement of atmospheric pressure
A
In reference to barometric equation, we can write,
P atm= γHgh + P vapor P atm Since pressure exerted by mercury vapor is very small, therefore,
B Mercury
P atm= γHgh
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Manometer: They use vertical or inclined liquid
columns to measure pressure A standard technique for measuring pressure involves the use of liquid columns in vertical or inclined tubes.
Piezometer
tube U-tube manometer Inverted U-tube manometer Inclined tube manometer
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Piezometer Piezomet er Tube Tube Manometer Ma nometer The simplest manometer is a tube, open at the top, which is attached to the top of a vessel containing liquid at a pressure (higher than atmospheric) to be measured. Patm
As the tube is open open to the atmosphere atmosphere the pressure measured is relative to atmospheric so is gauge pressure h1
Pressure at A = pressure due to column of liquid above A
A
0
h2
P A = Patm + ρgh1 = ρgh1 Pressure at B = pressure due to column of liquid above B P B = Patm + ρgh2 = 0 + ρgh2
B Liquid
This method can only be used for liquids (i.e., not for gases) and only when the liquid height is convenient to measure. It must not be too small or too large and pressure changes must be detectable
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
The “U”-Tube “U”-Tube Manometer Using a “U”-Tube “U”-Tube enables the pressure of both of both liquids and gases to be measured with the same instrument. instrument. The “U” is connected as in the figure below and filled with a fluid called called the manometric fluid. The The fluid whose pressure is being measured should have a mass mass density density less than that of the manometric fluid and the two fluids should not be able to mix readily - that is, they must must be immiscible. immiscible. Fluid density, ρ D h2
A h1
B
Manometric Manometric fluid density, density, ρman
C
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Pressure in a continuous static fluid is the same at any horizontal level so, PB= PC ……….(1) For the left hand arm, Pressure at B = pressure at A + pressure due to height hei ght h 1 of measured fluid PB= P A + ρgh1
For the right hand arm Pressure Pressure at C = pressure pressure at D + pressure due to height h of manometric manometric fluid
PC= Patm + ρmangh2 = ρmangh2 ( Since we we are measuring measuring gage gage pressure, pressure, Patm = 0 )
Putting the values of PB and PC in equation 1, we find, PA =ρmangh2 - ρgh1
If the fluid being measured is a gas, the density will probably be very low in comparison to the density of the manometric manometric fluid i.e., i.e., ρ man>> ρ. In this case the term ρgh1can be neglected, and the gauge pressure give by PA =ρmangh2
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Measurement of Pressure Difference Using a “U”-Tube “U” -Tube Manometer If the “U”-tube “U”-tube manometer is connected to a pressurized vessel at two points the pressure difference between these two points can be measured. B
If the manometer is arranged as in the figure, then we say Pressure at C = Pressure at D Fluid density, ρ
PC = PD ………(1)
hb
E
PC= PA +ρgha ……. (2)
h
PD= PB +ρg(h b – h) h) + ρmangh ……(3)
A ha
Combining equation 1, 2 & 3, PA +ρgha = PB +ρg(h b – h) h) + ρmangh or, PA-PB = ρg(hb – ha) + (ρman – ρ) gh
C
Manometric Manometric fluid density, density, ρman
if the fluid whose pressure difference is being measured is a gas and ρ man>> ρ, then the terms involving ρ can be neglected, so
P -P
=ρ
gh
D
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
At the lower part of the pipe, require another manometer manometer liquid to measure P
Flow
2
1
h
Manometer liquid, ( ρman )
ρ
Prove that pressure difference P1-P2= P = g h ( ρman - ρ)
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
h
Flow
At the upper part part of the pipe,it does not require another manometer liquid to measure P
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Inclined-tube manometer
Fluid C
Liquid B
1
h3 b
a
h1 h2
c
d L
Fluid A
Prove that P1-P2= γBLsin Lsinθ θ
2 e
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Selection of Manometer Care must be taken when attaching the manometer to vessel, no burrs must be present around this joint. Burrs would alter the flow causing local pressure variations to affect the measurement.
Advantages Advan tages and and disadvanges disadvanges of Manometer Manometer Advantages •
small pressure differences can be measured
•
They are very simple
•
No calibration is required; the pressure difference can be calculated from first principles.
Disadvantages • Not for measuring larger pressure differences • Some liquids are unsuitable for use. Surface tension can also cause errors due to capillary rise; this can be avoided if the diameters of the tubes are sufficiently large - preferably not not less than 15 mm diameter • Slow response; unsuitable for measuring fluctuating pressures.
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Class example 1 A simple U-tube manometer is installed across an orifice meter. The manometer is filled with mercury (specific gravity 13.6), and the liquid above the mercury is carbon tetrachloride (specific gravity 1.6). The manometer reads 200 mm. What is the pressure difference over the manometer?
Solution: Pressure at X = pressure at X' Pressure at X, P X= P1 + ρCCl4g (a+h)
Pressure at X‘, PX'= P2 + ρmer g h +ρCCl4g a We can write, P1 + ρCCl4g (a+h) = P2 + ρmer g h +ρ +ρCCl4g a or, P1-P2 = ρmer g h - ρCCl4g h =ghρ =ghρwater (SG mercury- SG CCl4) = 9.81x 0.2 x1000 (13.6-1.6) = 23544 Pa The pressure difference is 23544 Pa Pa
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Class example 2 The fluid shown shaded in the manometer is ethyl iodide with a specific gravity of 1.93. The heights are h 1 = 100 cm and h 2 = 20 cm. a)
What What is the the gag gage e pre press ssur ure e in in the the tan tank? k?
b)
What What is the the abs absol olut ute e pre press ssur ure e in in the the tank tank? ?
Tank full of air
h1
h2
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Ptank + air gh2 – EIg(h1 + h2)= Patm Since we’re taking gage pressure, Patm = 0 Ptank = air gh2 + EIg(h1 + h2) = – (1.2)(9.81)(0.2) – (1.2)(9.81)(0.2) + (1.93)(1000)(9.81)(1.00 + 0.200) = 22717.6 Pa = 22.72 kPag Assuming the density of air is i s too small Ptank = air gh2 + EIg(h1 + h2) = (1.93)(1000)(9.81)(1.00 + 0.200) = 22719.96 Pa = 22.72 kPag
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Example
Self assessment Assignment Assignment
• The mercury manometer below indicates a differential reading of 0.30 m when the pressure in pipe A is 30-mm Hg vacuum. Determine the pressure in pipe B if the specific gravity of the oil and mercury is 0.91 and 13.6, respectively.
Ans: 33.47 kPa
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Mechanical and Electronic Pressure Measuring Device
Measure of high pressures
Pressure gage Used where only a visual indication is needed at the site where the pressure is being measured.
Pressure transducer Pressure is measured at a point, and the value is displayed at another point.
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Bourdon Pressure Gage •
When pressure acts on an elastic structure, the structure will deform.
•
This deformation relates to the magnitude of pressure
• As the pressure within tube increases tube straighten translated into pointer motion on dial. •
The pressure indicated
the difference between that communicated by the system to the external (ambient) pressure
Pgage
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Pressure transducer •
The sensed pressure is converted to electrical signal – generated, and transmitted at another location such as central control station – Continuously monitor pressure changes with time (for rapidly changing pressure)
•
Types of pressure transducers: – Strain gage pressure transducer – Linear-variable differential transformer (LVDT) pressure transducer – Piezoelectric pressure transducers – Quartz resonator pressure transducers
Chemical Engineering Fluid Mechanics (CDB 1033)
Objectives:
May 2015
Buoyancy
To derive the equation of buoyant force
To analyze the case of bodies floating on a fluid
Use the principle of static equilibrium to solve forces involved in buoyancy problems.
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
What is Buoyancy When an object is submerged or floating in a static fluid the resultant force exerted on it by the fluid is called buoyancy for ce. ce. In a column of fluid, fluid , pressure increases with depth as a result of the weight of the overlying fluid. Thus a column of fluid, or an object submerged in the fluid, experiences greater pressure at the bottom of the column than at the top. This difference in pressure results in a net force that tends to accelerate an object upwards.
The magnitude of buoyancy force is proportional to the difference in the pressure between the top and the bottom of the column, c olumn, and (as explained by Archimedes' principle) is also equivalent equivalent to the weight of the fluid that would otherwise occupy the column, column, i.e. the displaced fluid.
Archimedes’ Principle: Any Principle: Any Object, wholly or partially immersed immersed in a fluid is buoyed up by a force equal to the weight of the fluid displaced by the object
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Buoyant force – force – Principle Principle
P1
a b
P2
• The buoyant force is caused by the increase of pressure in a fluid with depth. • Consider a body with a thickness, b is submerged in a liquid of density, f. • The hydrostatic forces: F1 = P1A acting downward F2 = P2A acting upward
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Buoyant force – force – Principle (Cont’d) (Cont’d)
P1
a
• Buoyant force = the difference between the two forces i.e the net upward force
b
FB P2
= P2A – P – P1A = f g(a+b)A – g(a+b)A – f gaA = f gbA = f gVb
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
The buoyant force on the solid object is equal to the weight of the fluid displaced (Archimedes' principle) principle)
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
For full fully y subme submerge rged d or imme immersed rsed body body in a fluid fluid , Archimedes’ principle is restated as: The buoyant force on a completely submerged submerged body is equal to the weight of fluid displaced
FB = W = f gVb = f Vb
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Buoyant force = Weight of fluid displaced With respect to the fluid dispersed:
FB = W = bgVf = bVf FB
ρf gVbody mbody ρf g ρbody ρf mbody g ρbody
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Example • A piece of irregularly shaped metal weighs 300.0 N in air. When the metal is completely submerged in water, it weighs 232.5 N. find the volume of the metal. Solution: FB = W = 300 – 300 – 232.5 232.5 = 67.5 N FB = fgV = (1000 (1000)( )(9. 9.81) 81) V = 67. 67.5 5 V = 0.00688 m3
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
For floating bodies, Archimedes’ principle is restated as: A floating body displaces a volume volume of fluid whose weight is exactly equal to its own The weight of the entire body must be equal to the buoyant force (Weight of the fluid whose volume is equal to the volume of the submerged portion of the floating body).
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
• For floating bodies,
W ρ f gVbody,sub ρavg, bodygVtotal FB
Vbody,sub Vtotal
ρ avg, body ρ f
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Example • Determine the submerged depth of a cube of steel 0.30 m on each side floating in mercury. Given SGsteel = 7.8 SGHg = 13.6
steel D mercury
Chemical Engineering Fluid Mechanics (CDB 1033)
Solution • FB = W Vbody,total = 0.3 0.3 0.3 = 0.027 m3 f gVbody,sub = body gVbody,total
(13.6)(1000)(9.81)(0.3 0.3 D) = (7.8)(1000)(9.81)(0.027) D = 0.172 m
May 2015
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Example • A solid block (SG = 0.9) floats such that 75% of its volume is in water and 25% of its volume is in liquid X, which is layered above the water. Determine the density of liquid X.
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Solution • FB = W bgVf = fgVb bg(Vw + VX) = wgVb,sub in w + XgVb,sub in X bVb = wVb,sub in w + XVb,sub in X
0.9Vb = (1.0)(0.75Vb) + (SGX)(0.25Vb) SGX = 0.60 X = 600 kg/m3
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Sink or Float
An object with an average specific weight less than that of the fluid tend to float because W < FB
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Sink or Float
An object with an average specific weight greater than that of the fluid tend to sink because W > FB.
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
Sink or Float
An object whose average specific weight is equal to that of the fluid is neutrally buoyant.
Chemical Engineering Fluid Mechanics (CDB 1033)
May 2015
What we leant in this chapter (Outcomes)
What is fluid statics and hydrostatic equilibrium?
Pascal Law
How to derive Barometric equation
Definition of incompressible and compressible fluids?
Pressure depth relationships for fluids
Application Application
of fluids statics statics
(a) pressure measurement using manometer (b) Buoyancy force determination determination End of Chapter 2