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FLUID MECHANICS FOR CHEMICAL ENGINEERING Chapter 1: Fluid Mechanics and Fluid Properties

(Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

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Page 1: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

FLUID MECHANICS FOR CHEMICAL ENGINEERINGChapter 1: Fluid Mechanics and

Fluid Properties

Page 2: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

SEQUENCE OF CHAPTER 1Introduction

Objectives

1.1 Definition of A FluidShear stress in moving fluidDifferences between liquid and gasesNewtonian and Non-Newtonian Fluid

1.2 Engineering Units1.3 Fluid Properties

Vapor PressureEngineering significance of vapor pressureSurface TensionCapillarity Example 1.2Example 1.3

Summary

Page 3: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Introduction• Fluid mechanics is a study of the behavior of

fluids, either at rest (fluid statics) or in motion (fluid dynamics).

• The analysis is based on the fundamental laws of mechanics, which relate continuity of mass and energy with force and momentum.

• An understanding of the properties and behavior of fluids at rest and in motion is of great importance in engineering.

Page 4: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

1. Identify the units for the basic quantities of time, length, force and mass.

2. Properly set up equations to ensure consistency of units.

3. Define the basic fluid properties.4. Identify the relationships between specific

weight, specific gravity and density, and solve problems using their relationships.

Objectives

Page 5: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

1.1 Definition of Fluid

• Fluid mechanics is a division in applied mechanics related to the behaviour of liquid or gas which is either in rest or in motion.

• The study related to a fluid in rest or stationary is referred to fluid static, otherwise it is referred to as fluid dynamic.

• Fluid can be defined as a substance which can deform continuously when being subjected to shear stress at any magnitude. In other words, it can flow continuously as a result of shearing action. This includes any liquid or gas.

Page 6: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

1.1 Definition of Fluid

A fluid is a substance, which deforms continuously, or flows, when subjected to shearing force

In fact if a shear stress is acting on a fluid it will flow and if a fluid is at rest there is no shear stress acting on it.

Fluid Flow Shear stress – YesFluid Rest Shear stress – No

Page 7: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

1.1 Definition of Fluid

• Thus, with exception to solids, any other matters can be categorised as fluid. In microscopic point of view, this concept corresponds to loose or very loose bonding between molecules of liquid or gas, respectively.

• Examples of typical fluid used in engineering applications are water, oil and air.

Page 8: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

1.1 Fluid Concept In fluid, the molecules can move freely but are

constrained through a traction force called cohesion. This force is interchangeable from one molecule to another.

For gases, it is very weak which enables the gas to disintegrate and move away from its container.

For liquids, it is stronger which is sufficient enough to hold the molecule together and can withstand high compression, which is suitable for application as hydraulic fluid such as oil. On the surface, the cohesion forms a resultant force directed into the liquid region and the combination of cohesion forces between adjacent molecules from a tensioned membrane known as free surface.

Page 9: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

1.1 Definition of Fluid

Figure 1.1 Comparison Between Solids, Liquids and Gases

• For solid, imagine that the molecules can be fictitiously linked to each other with springs.

(a) Solid (b) Liquid (c) Gas

k

k k

k

Free surface

Page 10: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Shear stress in moving fluid

• If fluid is in motion, shear stress are developed if the particles of the fluid move relative to each other. Adjacent particles have different velocities, causing the shape of the fluid to become distorted

• On the other hand, the velocity of the fluid is the same at every point, no shear stress will be produced, the fluid particles are at rest relative to each other.

Moving plate Shear force

Fluid particles New particle position

Fixed surface

Page 11: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Differences between liquid and gases

Liquid GasesDifficult to compress and often regarded as incompressible

Easily to compress – changes of volume is large, cannot normally be neglected and are related to temperature

Occupies a fixed volume and will take the shape of the container

No fixed volume, it changes volume to expand to fill the containing vessels

A free surface is formed if the volume of container is greater than the liquid.

Completely fill the vessel so that no free surface is formed.

Page 12: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Example:AirWaterOilGasolineAlcoholKeroseneBenzeneGlycerine

Fluid Newton’s lawof viscosity

Newtonian fluids obey refer

Newton’s’ law of viscosity is given by;

dydu

(1.1)

• The viscosity is a function only of the condition of the fluid, particularly its temperature.

• The magnitude of the velocity gradient (du/dy) has no effect on the magnitude of .

= shear stress = viscosity of fluiddu/dy = shear rate, rate of strain or velocity gradient

Newtonian and Non-Newtonian Fluid

Page 13: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Fluid Newton’s lawof viscosity

Non- Newtonianfluids

Do not obey

•The viscosity of the non-Newtonian fluid is dependent on the velocity gradient as well as the condition of the fluid.

Newtonian Fluids a linear relationship between shear stress and the velocity gradient

(rate of shear), the slope is constant the viscosity is constant

non-Newtonian fluids slope of the curves for non-Newtonian fluids varies

Newtonian and Non-Newtonian Fluid

Page 14: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Figure 1.1 Shear stress vs. velocity gradient

Bingham plastic : resist a small shear stress but flow easily under large shear stresses, e.g. sewage sludge, toothpaste, and jellies.Pseudo plastic : most non-Newtonian fluids fall under this group. Viscosity decreases with increasing velocity gradient, e.g. colloidal

substances like clay, milk, and cement.Dilatants : viscosity decreases with increasing velocity gradient, e.g.

quicksand.

Page 15: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

1.2 Units and Dimensions• The primary quantities which are also referred to as

basic dimensions, such as L for length, T for time, M for mass and Q for temperature.

• This dimension system is known as the MLT system where it can be used to provide qualitative description for secondary quantities, or derived dimensions, such as area (L), velocity (LT-1) and density (ML-3).

• In some countries, the FLT system is also used, where the quantity F stands for force.

Page 16: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

1.2 Units and Dimensions• An example is a kinematic equation for the velocity V

of a uniformly accelerated body,V = V0 + at

where V0 is the initial velocity, a the acceleration and t the time interval. In terms for dimensions of the equation, we can expand that

LT-1 = LT -1 + LT-2 • T

Page 17: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Example The free vibration of a particle can be simulated by the

following differential equation:

where m is mass, u is velocity, t is time and x is displacement. Determine the dimension for the stiffness variable k.

0 kxdtdum

Page 18: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Example By making the dimension of the first term equal to the

second term:

[m] • = [k]•[x]

Hence,

[k] = =

= MT-2

[ u ][ t ]

[ m ] • [ u ][ t ] • [ x ]

M • LT-1

LT

Page 19: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Primary Units

In fluid mechanics we are generally only interested in the top four units from this table.

1.2 Engineering Units

Quantity SI UnitLength Metre, m

Mass Kilogram, kg

Time Seconds, s

Temperature Kelvin, K

Current Ampere, A

Luminosity Candela

Page 20: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Derived UnitsQuantity SI Unit

velocity m/s -

acceleration m/s2 -

force Newton (N) N = kg.m/s2

energy (or work) Joule (J) J = N.m = kg.m2/s2

power Watt (W) W = N.m/s = kg.m2/s3

pressure (or stress) Pascal (P) P = N/m2 = kg/m/s2

density kg/m3 -

specific weight N/m3 = kg/m2/s2 N/m3 = kg/m2/s2

relative density a ratio (no units) dimensionless

viscosity N.s/m2 N.s/m2 = kg/m/s

surface tension N/m N/m = kg/s2

Page 21: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Unit Cancellation Procedure1. Solve the equation algebraically for the desired

terms.2. Decide on the proper units of the result.3. Substitute known values, including units.4. Cancel units that appear in both the numerator and

denominator of any term.5. Use correct conversion factors to eliminate

unwanted units and obtain the proper units as described in Step 2.

6. Perform the calculations.

Page 22: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

ExampleGiven m = 80 kg and a=10 m/s2. Find the force

Solution F = ma F = 80 kg x 10 m/s2 = 800 kg.m/s2

F= 800N

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1.3 Fluid PropertiesDensity Density of a fluid, , Definition: mass per unit volume, • slightly affected by changes in temperature and pressure.

= mass/volume = m/ (1.2) Units: kg/m3

Typical values:Water = 1000 kg/m3; Air = 1.23 kg/m3

Page 24: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Fluid Properties (Continue)

Specific weightSpecific weight of a fluid, • Definition: weight of the fluid per unit volume • Arising from the existence of a gravitational force • The relationship and g can be found using the

following:

Since = m/therefore = g (1.3)Units: N/m3

Typical values:Water = 9814 N/m3; Air = 12.07 N/m3

Page 25: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Specific gravityThe specific gravity (or relative density) can be defined in two ways:

Definition 1: A ratio of the density of a substance to the density of water at standard temperature (4C) and atmospheric pressure, orDefinition 2: A ratio of the specific weight of a substance to the specific weight of water at standard temperature (4C) and atmospheric pressure.

(1.4)

Unit: dimensionless.

Cw

s

Cw

sSG

44 @@

Fluid Properties (Continue)

Page 26: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Example A reservoir of oil has a mass of 825 kg. The reservoir has a volume of 0.917 m3. Compute the density, specific weight, and specific gravity of the oil.

Solution:3/900

917.0825 mkgm

volumemass

oil

3oil m/N882981.9x900gmg

volumeweight

9.0998900

@

STPw

oiloilSG

Page 27: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Viscosity• Viscosity, , is the property of a fluid, due to cohesion and

interaction between molecules, which offers resistance to shear deformation.

• Different fluids deform at different rates under the same shear stress. The ease with which a fluid pours is an indication of its viscosity. Fluid with a high viscosity such as syrup deforms more slowly than fluid with a low viscosity such as water. The viscosity is also known as dynamic viscosity.

Units: N.s/m2 or kg/m/s

Typical values:Water = 1.14x10-3 kg/m/s; Air = 1.78x10-5 kg/m/s

Fluid Properties (Continue)

Page 28: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Kinematic viscosity, Definition: is the ratio of the viscosity to the density;

• will be found to be important in cases in which significant viscous and gravitational forces exist. Units: m2/sTypical values: Water = 1.14x10-6 m2/s; Air = 1.46x10-5 m2/s;

In general, viscosity of liquids with temperature, whereas

viscosity of gases with in temperature.

/

Page 29: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Bulk Modulus All fluids are compressible under the application of an external

force and when the force is removed they expand back to their original volume.

The compressibility of a fluid is expressed by its bulk modulus of elasticity, K, which describes the variation of volume with change of pressure, i.e.

Thus, if the pressure intensity of a volume of fluid, , is increased by Δp and the volume is changed by Δ, then

Typical values:Water = 2.05x109 N/m2; Oil = 1.62x109 N/m2

strainvolumetricpressureinchangeK

/pK

pK

Page 30: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Vapor Pressure A liquid in a closed container is subjected to a

partial vapor pressure in the space above the liquid due to the escaping molecules from the surface;

It reaches a stage of equilibrium when this pressure reaches saturated vapor pressure.

Since this depends upon molecular activity, which is a function of temperature, the vapor pressure of a fluid also depends on its temperature and increases with it.

If the pressure above a liquid reaches the vapor pressure of the liquid, boiling occurs; for example if the pressure is reduced sufficiently boiling may occur at room temperature.

Page 31: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Engineering significance of vapor pressure In a closed hydraulic system, Ex. in pipelines or pumps, water

vaporizes rapidly in regions where the pressure drops below the vapor pressure.

There will be local boiling and a cloud of vapor bubbles will form. This phenomenon is known as cavitations, and can cause serious

problems, since the flow of fluid can sweep this cloud of bubbles on into an area of higher pressure where the bubbles will collapse suddenly.

If this should occur in contact with a solid surface, very serious damage can result due to the very large force with which the liquid hits the surface.

Cavitations can affect the performance of hydraulic machinery such as pumps, turbines and propellers, and the impact of collapsing bubbles can cause local erosion of metal surface.

Cavitations in a closed hydraulic system can be avoided by maintaining the pressure above the vapor pressure everywhere in the system.

Page 32: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Surface Tension

Liquids possess the properties of cohesion and adhesion due to molecular attraction.

Due to the property of cohesion, liquids can resist small tensile forces at the interface between the liquid and air, known as surface tension, .

Surface tension is defined as force per unit length, and its unit is N/m. The reason for the existence of this force arises from intermolecular

attraction. In the body of the liquid (Fig. 1.2a), a molecule is surrounded by other molecules and intermolecular forces are symmetrical and in equilibrium.

At the surface of the liquid (Fig. 1.2b), a molecule has this force acting only through 180.

This imbalance forces means that the molecules at the surface tend to be drawn together, and they act rather like a very thin membrane under tension.

This causes a slight deformation at the surface of the liquid (the meniscus effect).

Figure 1.2: Surface Tension

Page 33: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

A steel needle floating on water, the spherical shape of dewdrops, and the rise or fall of liquid in capillary tubes is the results of the surface tension.

Surface tension is usually very small compared with other forces in fluid flows (e.g. surface tension for water at 20C is 0.0728 N/m).

Surface tension,, increases the pressure within a droplet of liquid. The internal pressure, P, balancing the surface tensional force of a spherical droplet of radius r, is given by

r2P

(1.7)

2R = pR2

Page 34: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Capillarity• The surface tension leads to the phenomenon known as

capillarity • where a column of liquid in a tube is supported in the

absence of an externally applied pressure.• Rise or fall of a liquid in a capillary tube is caused by surface

tension and depends on the relative magnitude of cohesion of the liquid and the adhesion of the liquid to the walls of the containing vessels.

• Liquid rise in tubes if they wet a surface (adhesion > cohesion), such as water, and fall in tubes that do not wet (cohesion > adhesion), such as mercury.

• Capillarity is important when using tubes smaller than 10 mm (3/8 in.).

• For tube larger than 12 mm (1/2 in.) capillarity effects are negligible.

Page 35: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Figure 1.3 Capillary actions

rcos2h

(1.8)

where h = height of capillary rise (or depression) = surface tension = wetting (contact) angle = specific weight of liquidr = radius of tube

Page 36: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

A reservoir of oil has a mass of 825 kg. The reservoir has a volume of 0.917 m3. Compute the density, specific weight, and specific gravity of the oil.Solution:

3/900917.0

825 mkgmvolumemass

oil

3oil m/N882981.9x900gmg

volumeweight

9.01000900SG

C4@w

oiloil

Example

Page 37: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

Water has a surface tension of 0.4 N/m. In a 3-mm diameter vertical tube, if the liquid rises 6 mm above the liquid outside the tube, calculate the wetting angle.SolutionCapillary rise due to surface tension is given by;

rcos2h

= 83.7

4.0x2006.0x0015.0x9810

2rhcos

Example

Page 38: (Chapter 1) Fluid Mechanics for Chemical Engineering.ppt

This chapter has summarized on the aspect below: Understanding of a fluid The differences between the behaviours of liquid and

gases Newtonian and non-Newtonian fluid were identified Engineering unit of SI unit were discussed Fluid properties of density, specific weight, specific

gravity, viscosity and bulk modulus were outlined and taken up.

Discussion on the vapor pressure of the liquid Surface tension Capillarity phenomena

Summary