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1 FUNDAMENTALS OF FUNDAMENTALS OF FLUID FLUID MECHANICS MECHANICS Chapter 7 Dimensional Chapter 7 Dimensional Analysis Analysis Modeling, and Similitude Modeling, and Similitude

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FUNDAMENTALS OFFUNDAMENTALS OF FLUID MECHANICS FLUID MECHANICS

Chapter 7 Dimensional AnalysisChapter 7 Dimensional Analysis

Modeling, and SimilitudeModeling, and Similitude

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MAIN TOPICSMAIN TOPICS

Dimensional AnalysisDimensional Analysis Buckingham Pi TheoremBuckingham Pi Theorem Determination of Pi TermsDetermination of Pi Terms Comments about Dimensional AnalysisComments about Dimensional Analysis Common Dimensionless Groups in Fluid MechanicsCommon Dimensionless Groups in Fluid Mechanics Correlation of Experimental DataCorrelation of Experimental Data Modeling and SimilitudeModeling and Similitude Typical Model StudiesTypical Model Studies Similitude Based on Governing Differential EquationSimilitude Based on Governing Differential Equation

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Dimensional Analysis Dimensional Analysis 1/41/4

A typical fluid mechanics problem in which A typical fluid mechanics problem in which experimentation is required, consider the steady flow of an experimentation is required, consider the steady flow of an incompressible Newtonian fluid through a long, smooth-incompressible Newtonian fluid through a long, smooth-walled, horizontal, circular pipe. walled, horizontal, circular pipe.

An important characteristic of this system, which would An important characteristic of this system, which would be interest to an engineer designing a pipeline, is the be interest to an engineer designing a pipeline, is the pressure drop per unit length that develops along the pipe pressure drop per unit length that develops along the pipe as a result of friction.as a result of friction.

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Dimensional Analysis Dimensional Analysis 2/42/4

The first step in the planning of an experiment to study The first step in the planning of an experiment to study this problem would be to decide on the factors, or this problem would be to decide on the factors, or variables, that will have an effect on the pressure drop.variables, that will have an effect on the pressure drop.

Pressure drop per unit lengthPressure drop per unit length

)V,,,D(fp

Pressure drop per unit length depends on FOUR variables:Pressure drop per unit length depends on FOUR variables:sphere size (D); speed (V); fluid density (ρ); fluid viscosity sphere size (D); speed (V); fluid density (ρ); fluid viscosity (m)(m)

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Dimensional Analysis Dimensional Analysis 3/43/4

To perform the experiments in a meaningful and To perform the experiments in a meaningful and systematic manner, it would be necessary to change on of systematic manner, it would be necessary to change on of the variable, such as the velocity, which holding all other the variable, such as the velocity, which holding all other constant, and measure the corresponding pressure drop.constant, and measure the corresponding pressure drop.

Difficulty to determine the functional relationship between Difficulty to determine the functional relationship between the pressure drop and the various facts that influence it.the pressure drop and the various facts that influence it.

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Series of TestsSeries of Tests

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Dimensional Analysis Dimensional Analysis 4/44/4

Fortunately, there is a much simpler approach to the Fortunately, there is a much simpler approach to the problem that will eliminate the difficulties described problem that will eliminate the difficulties described above.above.

Collecting these variables into two nondimensional Collecting these variables into two nondimensional combinations of the variables (called dimensionless combinations of the variables (called dimensionless product or dimensionless groups)product or dimensionless groups)

Only one dependent and one Only one dependent and one independent variableindependent variable

Easy to set up experiments to Easy to set up experiments to determine dependencydetermine dependency

Easy to present results (one graph)Easy to present results (one graph)

VD

V

pD2

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Plot of Pressure Drop Data Using …Plot of Pressure Drop Data Using …

0002124

3

2TLF

)FT)(TFL(

)L/F(L

V

pD

0002

124

TLF)TFL(

)L)(LT)(TFL(VD

dimensionless product or dimensionless product or dimensionless groupsdimensionless groups

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Buckingham Pi Theorem Buckingham Pi Theorem 1/51/5

A fundamental question we must answer is how many A fundamental question we must answer is how many dimensionless products are required to replace the original list of dimensionless products are required to replace the original list of variables ?variables ?

The answer to this question is supplied by the basic theorem of The answer to this question is supplied by the basic theorem of dimensional analysis that statesdimensional analysis that states

If an equation involving k variables is dimensionally homogeneous, it can be reduced to a relationship among k-r independent dimensionless products, where r is the minimum number of reference dimensions required to describe the variables.

Buckingham Pi TheoremBuckingham Pi Theorem Pi termsPi terms

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Buckingham Pi Theorem Buckingham Pi Theorem 2/52/5

Given a physical problem in which the dependent variable Given a physical problem in which the dependent variable is a function of k-1 independent variables.is a function of k-1 independent variables.

Mathematically, we can express the functional relationship Mathematically, we can express the functional relationship in the equivalent formin the equivalent form

)u,.....,u,u(fu k321

0)u,.....,u,u,u(g k321

Where g is an unspecified function, different from f.Where g is an unspecified function, different from f.

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Buckingham Pi Theorem Buckingham Pi Theorem 3/53/5

The Buckingham Pi theorem states that: Given a relation The Buckingham Pi theorem states that: Given a relation among k variables of the formamong k variables of the form

The k variables may be grouped into k-r independent The k variables may be grouped into k-r independent dimensionless products, or Π terms, expressible in dimensionless products, or Π terms, expressible in functional form byfunctional form by

0)u,.....,u,u,u(g k321

0),,,,,,(or

),,,,,(

rk321

rk321

r ?? r ?? Π??Π??

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Buckingham Pi Theorem Buckingham Pi Theorem 4/54/5

The number r is usually, but not always, equal to the The number r is usually, but not always, equal to the minimum number of independent dimensions required to minimum number of independent dimensions required to specify the dimensions of all the parameters. Usually the specify the dimensions of all the parameters. Usually the reference dimensions required to describe the variables reference dimensions required to describe the variables will be the basic dimensions M, L, and T or F, L, and T.will be the basic dimensions M, L, and T or F, L, and T.

The theorem does not predict the functional form of The theorem does not predict the functional form of or or . The functional relation among the independent . The functional relation among the independent dimensionless products Π must be determined dimensionless products Π must be determined experimentally.experimentally.

The k-r dimensionless products Π terms obtained from The k-r dimensionless products Π terms obtained from the procedure are independent.the procedure are independent.

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Buckingham Pi Theorem Buckingham Pi Theorem 5/55/5

A Π term is not independent if it can be obtained from a A Π term is not independent if it can be obtained from a product or quotient of the other dimensionless products of product or quotient of the other dimensionless products of the problem. For example, ifthe problem. For example, if

then neither Πthen neither Π55 nor Π nor Π66 is independent of the other is independent of the other

dimensionless products or dimensionless products or dimensionless groupsdimensionless groups..

23

4/31

632

15 or

2

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Determination of Pi Terms Determination of Pi Terms 1/121/12

Several methods can be used to form the dimensionless Several methods can be used to form the dimensionless products, or pi term, that arise in a dimensional analysis.products, or pi term, that arise in a dimensional analysis.

The method we will describe in detail is called the The method we will describe in detail is called the METHOD of repeating variables.METHOD of repeating variables.

Regardless of the method to be used to determine the Regardless of the method to be used to determine the dimensionless products, dimensionless products, one begins by listingone begins by listing all all dimensional variablesdimensional variables that are known (or believed) to that are known (or believed) to affect the given flow phenomenon.affect the given flow phenomenon.

Eight steps listedEight steps listed below outline a recommended below outline a recommended procedure for determining the Π terms.procedure for determining the Π terms.

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Determination of Pi Terms Determination of Pi Terms 2/122/12

Step 1 List all the variables.Step 1 List all the variables. 1 1

List all the dimensional variables involved.List all the dimensional variables involved. Keep the number of variables to a minimum, so that we Keep the number of variables to a minimum, so that we

can minimize the amount of laboratory work.can minimize the amount of laboratory work. All variables must be independent. For example, if the All variables must be independent. For example, if the

cross-sectional area of a pipe is an important variable, cross-sectional area of a pipe is an important variable, either the area or the pipe diameter could be used, but either the area or the pipe diameter could be used, but not both, since they are obviously not independent.not both, since they are obviously not independent.

γγ==ρρ×g, that is, ×g, that is, γγ,,ρρ, and g are not independent., and g are not independent.

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Determination of Pi Terms Determination of Pi Terms 3/123/12

Step 1 List all the variables. Step 1 List all the variables. 22

Let k be the number of variables.Let k be the number of variables. Example: For pressure drop per unit length, k=5. (All Example: For pressure drop per unit length, k=5. (All

variables are variables are pp, D,, D,,,, and V ), and V )

)V,,,D(fp

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Determination of Pi Terms Determination of Pi Terms 4/124/12

Step 2 Express each of the variables in terms of Step 2 Express each of the variables in terms of basic dimensions. Find the number of reference basic dimensions. Find the number of reference dimensions.dimensions. Select a set of fundamental (primary) dimensions.Select a set of fundamental (primary) dimensions. For example: MLT, or FLT.For example: MLT, or FLT. Example: For pressure drop per unit length , we choose Example: For pressure drop per unit length , we choose

FLT.FLT.

12

243

LTVTFL

TFLLDFLp

r=3r=3

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Determination of Pi Terms Determination of Pi Terms 5/125/12

Step 3 Determine the required number of pi terms.Step 3 Determine the required number of pi terms. Let k be the number of variables in the problem.Let k be the number of variables in the problem. Let r be the number of reference dimensions (primary Let r be the number of reference dimensions (primary

dimensions) required to describe these variables.dimensions) required to describe these variables. The number of pi terms is k-rThe number of pi terms is k-r Example: For pressure drop per unit length k=5, r = 3, Example: For pressure drop per unit length k=5, r = 3,

the number of pi terms is k-r=5-3=2.the number of pi terms is k-r=5-3=2.

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Determination of Pi Terms Determination of Pi Terms 6/126/12

Step 4 Select a number of repeating variables, where Step 4 Select a number of repeating variables, where the number required is equal to the number of the number required is equal to the number of reference dimensions.reference dimensions. Select a set of r dimensional variables that includes all Select a set of r dimensional variables that includes all

the primary dimensions ( repeating variables).the primary dimensions ( repeating variables). These repeating variables will all be combined with each These repeating variables will all be combined with each

of the remaining parameters. No repeating variables of the remaining parameters. No repeating variables should have dimensions that are power of the dimensions should have dimensions that are power of the dimensions of another repeating variable.of another repeating variable.

Example: For pressure drop per unit length ( r = 3) select Example: For pressure drop per unit length ( r = 3) select ρρ , V, D. , V, D.

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Determination of Pi Terms Determination of Pi Terms 7/127/12

Step 5 Form a pi term by multiplying one of the Step 5 Form a pi term by multiplying one of the nonrepeating variables by the product of the nonrepeating variables by the product of the repeating variables, each raised to an exponent that repeating variables, each raised to an exponent that will make the combination dimensionless. will make the combination dimensionless. 11

Set up dimensional equations, combining the variables Set up dimensional equations, combining the variables selected in Step 4 with each of the other variables selected in Step 4 with each of the other variables (nonrepeating variables) in turn, to form dimensionless (nonrepeating variables) in turn, to form dimensionless groups or dimensionless product.groups or dimensionless product.

There will be k – r equations.There will be k – r equations. Example: For pressure drop per unit lengthExample: For pressure drop per unit length

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Determination of Pi Terms Determination of Pi Terms 8/128/12

Step 5 (Continued) Step 5 (Continued) 22

cba1 VDp

1c,2b,1a

0c2b:T

0c4ba3:L

0c1:F

TLF)TFL()LT()L)(FL( 000c24b1a3

21V

Dp

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Determination of Pi Terms Determination of Pi Terms 9/129/12

Step 6 Repeat Step 5 for each of the remaining Step 6 Repeat Step 5 for each of the remaining nonrepeating variables.nonrepeating variables.

cba2 VD

1c,1b,1a

0c2b1:T

0c4ba2:L

0c1:F

TLF)TFL()LT()L)(TFL( 000c24b1a2

DV2

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Determination of Pi Terms Determination of Pi Terms 10/1210/12

Step 7 Check all the resulting pi terms to make Step 7 Check all the resulting pi terms to make sure they are dimensionless.sure they are dimensionless. Check to see that each group obtained is dimensionless.Check to see that each group obtained is dimensionless. Example: For pressure drop per unit length .Example: For pressure drop per unit length .

0000002

00000021

TLMTLFDV

TLMTLFV

Dp

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Determination of Pi Terms Determination of Pi Terms 11/1211/12

Step 8 Express the final form as a relationship Step 8 Express the final form as a relationship among the pi terms, and think about what is among the pi terms, and think about what is means.means. Express the result of the dimensional analysis.Express the result of the dimensional analysis.

Example: For pressure drop per unit length .Example: For pressure drop per unit length .

DVV

Dp2

),,,,,( rk321

Dimensional analysis will not provide Dimensional analysis will not provide the form of the function. The function the form of the function. The function can only be obtained from a suitable set can only be obtained from a suitable set of experiments.of experiments.

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Determination of Pi Terms Determination of Pi Terms 12/1212/12

The pi terms can be rearranged. For example, ΠThe pi terms can be rearranged. For example, Π22, could be , could be

expressed asexpressed as

VD

V

Dp2

VD

2

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Example 7.1 Method of Repeating Example 7.1 Method of Repeating VariablesVariables

A thin rectangular plate having a width w and a height h is A thin rectangular plate having a width w and a height h is located so that it is normal to a moving stream of fluid. located so that it is normal to a moving stream of fluid. Assume that the drag, D, that the fluid exerts on the plate Assume that the drag, D, that the fluid exerts on the plate is a function of w and h, the fluid viscosity, is a function of w and h, the fluid viscosity, µµ ,and ,and ρρ, , respectively, and the velocity, V, of the fluid approaching respectively, and the velocity, V, of the fluid approaching the plate. Determine a suitable set of pi terms to study this the plate. Determine a suitable set of pi terms to study this problem experimentally.problem experimentally.

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Example 7.1 Example 7.1 SolutionSolution1/51/5

Drag force on a PLATEDrag force on a PLATE

Step 1:List all the dimensional variables involved. Step 1:List all the dimensional variables involved. D,w,h, D,w,h, ρ,μ,Vρ,μ,V k=6 dimensional parameters. k=6 dimensional parameters.

Step 2:Select primary dimensions M,L, and T. Express Step 2:Select primary dimensions M,L, and T. Express each of the variables in terms of basic dimensionseach of the variables in terms of basic dimensions

)V,,,h,w(fD

1311

2

LTVMLTML

LhLwMLTD

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Example 7.1 Example 7.1 SolutionSolution2/52/5

Step 3: Determine the required number of pi terms. Step 3: Determine the required number of pi terms.

k-r=6-3=3k-r=6-3=3 Step 4:Select repeating variables w,V,Step 4:Select repeating variables w,V,.. Step 5~6:combining the repeating variables with each Step 5~6:combining the repeating variables with each

of the other variables in turn, to form dimensionless of the other variables in turn, to form dimensionless groups or dimensionless products.groups or dimensionless products.

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Example 7.1 Example 7.1 SolutionSolution3/53/5

1c,2b,2a

0b2:T

0c3ba1:L

0c1:M

TLM)ML()LT()L)(MLT(VDw 000c3b1a2cba1

221Vw

D

0c,0b,1a

0b:T

0c3ba1:L

0c:M

TLM)ML()LT()L(LVhw 000c3b1acba2

w

h2

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Example 7.1 Example 7.1 SolutionSolution4/54/5

1c,1b,1a

0b1:T

0c3ba1:L

0c1:M

TLM)ML()LT()L)(TML(Vw 000c3b1a11cba3

wV3

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Example 7.1 Example 7.1 SolutionSolution5/55/5

Step 7: Check all the resulting pi terms to make sure Step 7: Check all the resulting pi terms to make sure they are dimensionless. they are dimensionless.

Step 8: Express the final form as a relationship among Step 8: Express the final form as a relationship among the pi terms.the pi terms.

The functional relationship isThe functional relationship is

wV,

w

h

Vw

D

or),,(

22

321

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Selection of Variables Selection of Variables 1/41/4

One of the most important, and difficult, steps in applying One of the most important, and difficult, steps in applying dimensional analysis to any given problem is the selection dimensional analysis to any given problem is the selection of the variables that are involved.of the variables that are involved.

There is no simple procedure whereby the variable can be There is no simple procedure whereby the variable can be easily identified. Generally, one must rely on a good easily identified. Generally, one must rely on a good understanding of the phenomenon involved and the understanding of the phenomenon involved and the governing physical laws. governing physical laws.

If extraneous variables are included, then too many pi If extraneous variables are included, then too many pi terms appear in the final solution, and it may be difficult, terms appear in the final solution, and it may be difficult, time consuming, and expensive to eliminate these time consuming, and expensive to eliminate these experimentally. experimentally.

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Selection of Variables Selection of Variables 2/42/4

If important variables are omitted, then an incorrect result If important variables are omitted, then an incorrect result will be obtained; and again, this may prove to be costly will be obtained; and again, this may prove to be costly and difficult to ascertain. and difficult to ascertain.

Most engineering problems involve certain simplifying Most engineering problems involve certain simplifying assumptions that have an influence on the variables to be assumptions that have an influence on the variables to be considered.considered.

Usually we wish to keep the problems as simple as Usually we wish to keep the problems as simple as possible, perhaps even if some accuracy is sacrificedpossible, perhaps even if some accuracy is sacrificed

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Selection of Variables Selection of Variables 3/43/4

A suitable balance between simplicity and accuracy is an A suitable balance between simplicity and accuracy is an desirable goal.~~~~~desirable goal.~~~~~

Variables can be classified into three general group:Variables can be classified into three general group: Geometry: lengths and angles.Geometry: lengths and angles. Material Properties: relate the external effects and the Material Properties: relate the external effects and the

responses.responses. External Effects: produce, or tend to produce, a change External Effects: produce, or tend to produce, a change

in the system. Such as force, pressure, velocity, or in the system. Such as force, pressure, velocity, or gravity.gravity.

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Selection of Variables Selection of Variables 4-1/44-1/4

Points should be considered in the selection of variables:Points should be considered in the selection of variables: Clearly define the problem. What’s the main variable of Clearly define the problem. What’s the main variable of

interest?interest? Consider the basic laws that govern the phenomenon.Consider the basic laws that govern the phenomenon. Start the variable selection process by grouping the Start the variable selection process by grouping the

variables into three broad classes.variables into three broad classes.

ContinuedContinued

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Selection of Variables Selection of Variables 4-2/44-2/4

Points should be considered in the selection of variables:Points should be considered in the selection of variables: Consider other variables that may not fall into one the Consider other variables that may not fall into one the

three categories. For example, time and time dependent three categories. For example, time and time dependent variables.variables.

Be sure to include all quantities that may be held Be sure to include all quantities that may be held constant (e.g., g).constant (e.g., g).

Make sure that all variables are independent. Look for Make sure that all variables are independent. Look for relationships among subsets of the variables.relationships among subsets of the variables.

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Determination of Reference Dimension Determination of Reference Dimension 1/31/3

When to determine the number of pi terms, it is important When to determine the number of pi terms, it is important to know how many reference dimensions are required to to know how many reference dimensions are required to describe the variables.describe the variables.

In fluid mechanics, the required number of reference In fluid mechanics, the required number of reference dimensions is three, but in some problems only one or two dimensions is three, but in some problems only one or two are required.are required.

In some problems, we occasionally find the number of In some problems, we occasionally find the number of reference dimensionsreference dimensions needed to describe all variables is needed to describe all variables is smaller than the number of basic dimensionssmaller than the number of basic dimensions. Illustrated in . Illustrated in Example 7.2.Example 7.2.

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Example 7.2 Determination of Pi TermsExample 7.2 Determination of Pi Terms

An open, cylindrical tank having a diameter D is An open, cylindrical tank having a diameter D is supported around its bottom circumference and is filled to supported around its bottom circumference and is filled to a depth h with a liquid having a specific weight a depth h with a liquid having a specific weight . The . The vertical deflection, vertical deflection, , of the center of the bottom is a , of the center of the bottom is a function of D, h, d, function of D, h, d, , and E, where d is the thickness of , and E, where d is the thickness of the bottom and E is the modulus of elasticity of the bottom the bottom and E is the modulus of elasticity of the bottom material. Perform a dimensional analysis of this problem.material. Perform a dimensional analysis of this problem.

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Example 7.2 Example 7.2 SolutionSolution1/31/3

The vertical deflectionThe vertical deflection

E,,d,f,Df

For F,L,T. Pi terms=6-2=4For F,L,T. Pi terms=6-2=4For M,L,T Pi terms=6-3=3For M,L,T Pi terms=6-3=3

212

223

TMLE,FLE

TML,FL

Ld

Lh

LD

L

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Example 7.2 Example 7.2 SolutionSolution2/32/3

For F,L,T system, Pi terms=6-2=4For F,L,T system, Pi terms=6-2=4

D

E,

D

d,

D

h

DD

E,

D

d,

D

h,

D 4321

D and D and γγ are selected as repeating variables are selected as repeating variables

4433

2211

ba4

ba3

ba2

ba1

EDdD

hDD

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Example 7.2 Example 7.2 SolutionSolution3/33/3

For M,L,T system, Pi terms=6-3=3 ?For M,L,T system, Pi terms=6-3=3 ?

A closer look at the dimensions of the variables listed A closer look at the dimensions of the variables listed reveal that only two reference dimensions, reveal that only two reference dimensions, L and MTL and MT-2-2

are required. are required.

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Determination of Reference Dimension Determination of Reference Dimension 2/32/3

,,Dfh

222 T

M

TL

MLL

Dh

L

F

L

FLL

Dh

3

EXAMPLEEXAMPLE

MLT SYSTEMMLT SYSTEM FLT SYSTEMFLT SYSTEM

Pi term=4-3=1 Pi term=4-2=2

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Determination of Reference Dimension Determination of Reference Dimension 3/33/3

2200T

0211L

1100M

Dh

0000T

1311L

1100F

Dh

D

h1

222DD

h

D

Set Dimensional MatrixSet Dimensional Matrix

MLT SYSTEMMLT SYSTEM FLT SYSTEMFLT SYSTEM

Rank=2 Pi term=4-2=2Rank=2 Pi term=4-2=2

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Uniqueness of Pi Terms Uniqueness of Pi Terms 1/41/4

The Pi terms obtained depend on the somewhat arbitrary The Pi terms obtained depend on the somewhat arbitrary selection of repeating variables. For example, in the selection of repeating variables. For example, in the problem of studying the pressure drop in a pipe.problem of studying the pressure drop in a pipe.

VD

V

Dp12

VD

V

Dp2

2

)V,,,D(fp

Selecting D,V, and as repeating variables:

Selecting D,V, and as repeating variables:

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Uniqueness of Pi Terms Uniqueness of Pi Terms 2/42/4

Both are correct, and both would Both are correct, and both would lead to the same final equation for lead to the same final equation for the pressure drop. the pressure drop. There is not a There is not a unique set of pi termsunique set of pi terms which which arises from a dimensional analysisarises from a dimensional analysis. . The functions The functions ΦΦ11 and and ΦΦ22 are will be are will be

different because the dependent pi different because the dependent pi terms are different for the two terms are different for the two relationships.relationships.

VD

V

Dp12

VD

V

Dp2

2

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Uniqueness of Pi Terms Uniqueness of Pi Terms 3/43/4

321 ,

'2223

'211 ,,

EXAMPLEEXAMPLE

b3

a2

'2 Form a new pi termForm a new pi term

All are correct

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Uniqueness of Pi Terms Uniqueness of Pi Terms 4/44/4

V

DpVD

V

Dp 2

2

VD

V

Dp2

2

VD

V

Dp12

Selecting D,V, and as repeating variables:

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Common Dimensionless GroupsCommon Dimensionless Groups 1/2 1/2

A list of variables that commonly arise in fluid mechanical problems.

Possible to provide a physical interpretation to the dimensionless groups which can be helpful in assessing their influence in a particular application.

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Froude Number Froude Number 1/21/2

In honor of William Froude (1810~1879), a British civil engineer, In honor of William Froude (1810~1879), a British civil engineer, mathematician, and naval architect who pioneered the use of towing mathematician, and naval architect who pioneered the use of towing tanks for the study of ship design.tanks for the study of ship design.

Froude number is the ratio of the forces due to the acceleration of a Froude number is the ratio of the forces due to the acceleration of a fluid particles (inertial force) to the force due to gravity (gravity fluid particles (inertial force) to the force due to gravity (gravity forces).forces).

Froude number is significant for flows with free surface effects.Froude number is significant for flows with free surface effects. Froude number less than unity indicate subcritical flow and values Froude number less than unity indicate subcritical flow and values

greater than unity indicate supercritical flow.greater than unity indicate supercritical flow.

3

2222

gL

LV

gL

VFr

gL

VFr

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Froude Number Froude Number 2/22/2

*

*s*

s

2s

ss

s ds

dVV

V

ds

dVV

dt

dVa

s

sV

VV *s*

s

mds

dVV

VF

*

*s*

s

2

I

g

V

g

V

ds

dVV

g

V

F

FrF

2

*

*s*

s

2

G

I

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Reynolds Number Reynolds Number 1/21/2

In honor of Osborne Reynolds (1842~1912), the British engineer In honor of Osborne Reynolds (1842~1912), the British engineer who first demonstrated that this combination of variables could be who first demonstrated that this combination of variables could be used as a criterion to distinguish between laminar and turbulent used as a criterion to distinguish between laminar and turbulent flow.flow.

The Reynolds number is a measure of the ration of the inertia forces The Reynolds number is a measure of the ration of the inertia forces to viscous forces.to viscous forces.

If the Reynolds number is small (Re<<1), thi sis an indication that If the Reynolds number is small (Re<<1), thi sis an indication that the viscous forces ar dominant in the problem, and it may be the viscous forces ar dominant in the problem, and it may be possible to neglect the inertial effects; that is, the density of the fluid possible to neglect the inertial effects; that is, the density of the fluid will no be an important variable.will no be an important variable.

VV

Re

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Reynolds Number Reynolds Number 2/22/2

Flows with very small Reynolds numbers are commonly referred to Flows with very small Reynolds numbers are commonly referred to as “creeping flows”.as “creeping flows”.

For large Reynolds number flow, the viscous effects are small For large Reynolds number flow, the viscous effects are small relative to inertial effects and for these cases it may be possible to relative to inertial effects and for these cases it may be possible to neglect the effect of viscosity and consider the problem as one neglect the effect of viscosity and consider the problem as one involving a “nonviscous” fluid.involving a “nonviscous” fluid.

Flows with “large” Reynolds number generally are turbulent. Flows Flows with “large” Reynolds number generally are turbulent. Flows in which the inertia forces are “small” compared with the viscous in which the inertia forces are “small” compared with the viscous forces are characteristically laminar flowsforces are characteristically laminar flows..

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Euler numberEuler number

In honor of Leonhard Euler (1707~1783), a famous Swiss In honor of Leonhard Euler (1707~1783), a famous Swiss mathematician who pioneered work on the relationship between mathematician who pioneered work on the relationship between pressure and flow.pressure and flow.

Euler’s number is the ratio of pressure force to inertia forces. It is Euler’s number is the ratio of pressure force to inertia forces. It is often called theoften called the pressure coefficient, Cp.pressure coefficient, Cp.

22 V

p

V

pEu

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Cavitation NumberCavitation Number

For problems in which cavitation is of concern, the dimensionless For problems in which cavitation is of concern, the dimensionless group is commonly used, where pgroup is commonly used, where pvv is the vapor is the vapor pressure and ppressure and prr is some reference pressure. is some reference pressure.

The cavitation number is used in the study of cavitation phenomena.The cavitation number is used in the study of cavitation phenomena. The smaller the cavitation number, the more likely cavitation is to The smaller the cavitation number, the more likely cavitation is to

occur.occur.

2

vr

V21

ppCa

221

vr V/)pp(

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55

Cauchy Number & Mach Number Cauchy Number & Mach Number 1/21/2

The Cauchy number is named in honor of Augustin Louis de The Cauchy number is named in honor of Augustin Louis de Cauchy (1789~1857), a French engineer, mathematician, and Cauchy (1789~1857), a French engineer, mathematician, and hydrodynamicist.hydrodynamicist.

The Mach number is named in honor of Ernst Mach (1838~1916), The Mach number is named in honor of Ernst Mach (1838~1916), an Austrian physicist and philosopher.an Austrian physicist and philosopher.

Either number may be used in problems in which fluid Either number may be used in problems in which fluid compressibility is important.compressibility is important.

CaE

VMa

EV

E

V

c

VMa

E

VaC

22

2

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Cauchy Number & Mach Number Cauchy Number & Mach Number 2/22/2

Both numbers can be interpreted as representing an index of the Both numbers can be interpreted as representing an index of the ration of inertial force to compressibility force, where V is the flow ration of inertial force to compressibility force, where V is the flow speed and c is the local sonic speed.speed and c is the local sonic speed.

Mach number is a key parameter that characterizes compressibility Mach number is a key parameter that characterizes compressibility effects in a flow.effects in a flow.

When the Mach number is relatively small (say, less than 0.3), the When the Mach number is relatively small (say, less than 0.3), the inertial forces induced by the fluid motion are not sufficiently large inertial forces induced by the fluid motion are not sufficiently large to cause a significant change in the fluid density, and in this case the to cause a significant change in the fluid density, and in this case the compressibility of the fluid can be neglected.compressibility of the fluid can be neglected.

For truly incompressible flow, c=∞ so that M=0.For truly incompressible flow, c=∞ so that M=0.

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Strouhal Number Strouhal Number 1/21/2

In honor of Vincenz Strouhal (1850~1922), who used this parameter In honor of Vincenz Strouhal (1850~1922), who used this parameter in his study of “singing wires.” The most dramatic evidence of this in his study of “singing wires.” The most dramatic evidence of this phenomenon occurred in 1940 with the collapse of the Tacoma phenomenon occurred in 1940 with the collapse of the Tacoma Narrow bridges. The shedding frequency of the vortices coincided Narrow bridges. The shedding frequency of the vortices coincided with the natural frequency of the bridge, thereby setting up a with the natural frequency of the bridge, thereby setting up a resonant condition that eventually led to the collapse of the bridge.resonant condition that eventually led to the collapse of the bridge.

This parameter is important in unsteady, oscillating flow problems This parameter is important in unsteady, oscillating flow problems in which the frequency of the oscillation is in which the frequency of the oscillation is ωω . .

VtS

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Strouhal Number Strouhal Number 2/22/2

This parameter represents a measure of This parameter represents a measure of the ration of inertial force due to the the ration of inertial force due to the unsteadiness of the flow (local unsteadiness of the flow (local acceleration) to the inertial forces due to acceleration) to the inertial forces due to change in velocity from point to point in change in velocity from point to point in the flow field (convective acceleration). the flow field (convective acceleration). This type of unsteady flow may develop This type of unsteady flow may develop when a fluid flows past a solid body (such when a fluid flows past a solid body (such as a wire or cable) placed in the moving as a wire or cable) placed in the moving stream.stream.

For example, in a certain Reynolds number range, a periodic flow will For example, in a certain Reynolds number range, a periodic flow will develop downstream from a cylinder placed in a moving stream due to develop downstream from a cylinder placed in a moving stream due to a regular patterns of vortices that are shed from the body.a regular patterns of vortices that are shed from the body.

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Weber Number Weber Number 1/21/2

Named after Moritz Weber (1871~1951), a German professor of Named after Moritz Weber (1871~1951), a German professor of naval mechanics who was instrumental in formalizing the general naval mechanics who was instrumental in formalizing the general use of common dimensionless groups as a basis for similitude use of common dimensionless groups as a basis for similitude studies.studies.

Weber number is important in problem in which there is an interface Weber number is important in problem in which there is an interface between two fluids. In this situation the surface tension may play an between two fluids. In this situation the surface tension may play an important role in the phenomenon of interest.important role in the phenomenon of interest.

2V

We

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Weber Number Weber Number 2/22/2

Weber number is the ratio of inertia forces to surface tension forces.Weber number is the ratio of inertia forces to surface tension forces. Common examples of problems in which Weber number may be Common examples of problems in which Weber number may be

important include the flow of thin film of liquid, or the formation of important include the flow of thin film of liquid, or the formation of droplets or bubbles.droplets or bubbles.

The flow of water in a river is not affected significantly by sureface The flow of water in a river is not affected significantly by sureface tension, since inertial and gravitational effects are dominant tension, since inertial and gravitational effects are dominant (We>>1).(We>>1).

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Correlation of Experimental DataCorrelation of Experimental Data

Dimensional analysis only provides the dimensionless groups Dimensional analysis only provides the dimensionless groups describing the phenomenon, and not the specific relationship describing the phenomenon, and not the specific relationship between the groups.between the groups.

To determine this relationship, suitable experimental data must be To determine this relationship, suitable experimental data must be obtained.obtained.

The degree of difficulty depends on the number of pi terms.The degree of difficulty depends on the number of pi terms.

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Problems with One Pi TermProblems with One Pi Term

The functional relationship for one Pi term.The functional relationship for one Pi term.

C1

where C is a constant. The value of the constant must still be determined by experiment.

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Example 7.3 Flow with Only One Pi TermExample 7.3 Flow with Only One Pi Term

Assume that the drag, D, acting on a spherical particle that falls very Assume that the drag, D, acting on a spherical particle that falls very slowly through a viscous fluid is a function of the particle diameter, slowly through a viscous fluid is a function of the particle diameter, d, the particle velocity, V, and the fluid viscosity, μ. Determine, d, the particle velocity, V, and the fluid viscosity, μ. Determine, with the aid the dimensional analysis, how the drag depends on the with the aid the dimensional analysis, how the drag depends on the particle velocity. particle velocity.

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Example 7.3 Example 7.3 SolutionSolution

The drag The drag

),V,d(fD 13

2

LTVML

TFLLdFD

VD

dVCDCdV

D1

For a given particle and fluids, the drag varies For a given particle and fluids, the drag varies directly with the velocitydirectly with the velocity

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Problems with Two or More Pi Term Problems with Two or More Pi Term 1/21/2

Problems with two pi termsProblems with two pi terms

)( 21

the functional relationship the functional relationship among the variables can the among the variables can the be determined by varying Πbe determined by varying Π22

and measuring the and measuring the corresponding value of Πcorresponding value of Π11..

The empirical equation The empirical equation relating Πrelating Π22 and Π and Π11 by using a by using a

standard curve-fitting standard curve-fitting technique.technique.

An empirical relationship is An empirical relationship is valid over the range of valid over the range of ΠΠ22..

Dangerous to Dangerous to extrapolate beyond extrapolate beyond valid rangevalid range

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Problems with Two or More Pi Term Problems with Two or More Pi Term 2/22/2

Problems with three pi terms.Problems with three pi terms.

321 ,

Families curve of curvesFamilies curve of curves

To determine a suitable empirical To determine a suitable empirical equation relating the three pi terms.equation relating the three pi terms.

To show data correlations on simple graphs.To show data correlations on simple graphs.

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Modeling and SimilitudeModeling and Similitude

To develop the procedures for To develop the procedures for designing models so that the designing models so that the model and prototype will model and prototype will behave in a similar fashion…….behave in a similar fashion…….

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Model vs. Prototype Model vs. Prototype 1/21/2

Model ? A model is a representation of a physical system that may Model ? A model is a representation of a physical system that may be used to predict the behavior of the system in some desired be used to predict the behavior of the system in some desired respect. Mathematical or computer models may also conform to this respect. Mathematical or computer models may also conform to this definition, our interest will be in physical model.definition, our interest will be in physical model.

Prototype? The physical system for which the prediction are to be Prototype? The physical system for which the prediction are to be made. made.

Models that resemble the prototype but are generally of a different Models that resemble the prototype but are generally of a different size, may involve different fluid, and often operate under different size, may involve different fluid, and often operate under different conditions. conditions.

Usually a model is smaller than the prototype. Usually a model is smaller than the prototype. Occasionally, if the prototype is very small, it may be advantageous Occasionally, if the prototype is very small, it may be advantageous

to have a model that is larger than the prototype so that it can ve to have a model that is larger than the prototype so that it can ve more easily studied. For example, large models have been used to more easily studied. For example, large models have been used to study the motion of red blood cells.study the motion of red blood cells.

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Model vs. Prototype Model vs. Prototype 2/22/2

With the successful development of a valid model, it is possible to With the successful development of a valid model, it is possible to predict the behavior of the prototype under a certain set of predict the behavior of the prototype under a certain set of conditions.conditions.

There is an inherent danger in the use of models in that predictions There is an inherent danger in the use of models in that predictions can be made that are in error and the error not detected until the can be made that are in error and the error not detected until the prototype is found not to perform as predicted.prototype is found not to perform as predicted.

It is imperative that the model be properly designed and tested and It is imperative that the model be properly designed and tested and that the results be interpreted correctly.that the results be interpreted correctly.

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Similarity of Model and PrototypeSimilarity of Model and Prototype

What conditions must be met to ensure the similarity of model and What conditions must be met to ensure the similarity of model and prototype?prototype?

Geometric SimilarityGeometric Similarity Model and prototype have same shape.Model and prototype have same shape. Linear dimensions on model and prototype correspond within Linear dimensions on model and prototype correspond within

constant scale factor.constant scale factor. Kinematic SimilarityKinematic Similarity

Velocities at corresponding points on model and prototype differ Velocities at corresponding points on model and prototype differ only by a constant scale factor.only by a constant scale factor.

Dynamic SimilarityDynamic Similarity Forces on model and prototype differ only by a constant scale Forces on model and prototype differ only by a constant scale

factor.factor.

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Theory of Models Theory of Models 1/51/5

The theory of models can be readily developed by using The theory of models can be readily developed by using the principles of dimensional analysis.the principles of dimensional analysis.

For given problem which can be described in terms of a For given problem which can be described in terms of a set of pi terms asset of pi terms as

),,,,( n321 This relationship can be formulated This relationship can be formulated with a knowledge of the general with a knowledge of the general nature of the physical phenomenon nature of the physical phenomenon and the variables involved. and the variables involved.

This equation applies to any system that is governed by the same variables.

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Theory of Models Theory of Models 2/52/5

A similar relationship can be written for a model of this A similar relationship can be written for a model of this prototype; that is,prototype; that is,

where the form of the function will be the same as long where the form of the function will be the same as long

as the as the same phenomenonsame phenomenon is involved in both the is involved in both the prototype and the model.prototype and the model.

),,,,,( nmm3m2m1

The prototype and the model must have The prototype and the model must have the same phenomenon.the same phenomenon.

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Theory of Models Theory of Models 3/53/5

Model design (the model is designed and operated) Model design (the model is designed and operated) conditions, also called similarity requirements or modeling conditions, also called similarity requirements or modeling laws.laws.

The The form of Φform of Φ is the same for model and prototype, it is the same for model and prototype, it follows thatfollows that

nmnm33m22 .....

m11

This is the This is the desired prediction equationdesired prediction equation and and indicates that the measured of Πindicates that the measured of Π

1m1m obtained obtained

with the model will be equal to the with the model will be equal to the corresponding Πcorresponding Π

11 for the prototype as long as for the prototype as long as

the other Π parameters are equal. the other Π parameters are equal.

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Theory of Models Theory of Models 4/54/5 – Summary – Summary11

The prototype and the model must have the same The prototype and the model must have the same phenomenon. phenomenon.

),,,,( n321 For prototypeFor prototype

For modelFor model ),,,,,( nmm3m2m1

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Theory of Models Theory of Models 5/55/5 – Summary – Summary22

The model is designed and operated under the following The model is designed and operated under the following conditions conditions (called design conditions, also called similarity (called design conditions, also called similarity requirements or modeling laws)requirements or modeling laws)

The measured of ΠThe measured of Π1m1m obtained with the model will be obtained with the model will be

equal to the corresponding Πequal to the corresponding Π11 for the prototype. for the prototype.

nmnm33m22 .....

m11 Called prediction equationCalled prediction equation

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Theory of Models Theory of Models EXAMPLE 1EXAMPLE 1

Example: Considering the drag force on a sphereExample: Considering the drag force on a sphere..

The prototype and the model must have the same phenomenon. The prototype and the model must have the same phenomenon.

Design conditions.Design conditions.

Then …Then …

m

mmm12

m2

mm

m DVf

DV

F

),,V,D(fF

prototype122

VDf

DV

F

prototypeelmod

VDVD

prototype22

elmod22 DV

F

DV

F

VDf

DV

F122

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Theory of Models Theory of Models EXAMPLE 2EXAMPLE 2

Example: Determining the drag force on a thin rectangular plate (Example: Determining the drag force on a thin rectangular plate (ww ×× h h in size) in size)

The prototype and the model must have the same phenomenon. The prototype and the model must have the same phenomenon.

Design conditions.Design conditions.

Then …Then …

V,,,h,wfD

prototype22

Vw,

h

w

Vw

D

m

mmm

m

m2

mm2

m

m wV,

h

w

Vw

D

VwwV,

h

w

h

w

m

mmm

m

m

m

2

mm

2

m2

mm2

m

m22

DV

V

w

wD

Vw

D

Vw

D

Vw,

h

w

Vw

D22

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Example 7.5 Prediction of Prototype Example 7.5 Prediction of Prototype Performance from Model Data Performance from Model Data 1/21/2

A long structural component of a bridge has the cross section A long structural component of a bridge has the cross section shown in Figure E7.5. It is known that when a steady wind blows shown in Figure E7.5. It is known that when a steady wind blows past this type of bluff body, vortices may develop on the downwind past this type of bluff body, vortices may develop on the downwind side that are shed in a regular fashion at some definite frequency. side that are shed in a regular fashion at some definite frequency. Since these vortices can create harmful periodic forces acting on the Since these vortices can create harmful periodic forces acting on the structure, it is important to determine the shedding frequency. For structure, it is important to determine the shedding frequency. For the specific structure of interest, D=0.2m, H=0.4m, and a the specific structure of interest, D=0.2m, H=0.4m, and a representative wind velocity 50km/hr. Standard air can be assumed. representative wind velocity 50km/hr. Standard air can be assumed. The shedding frequency is to be determined through the use of a The shedding frequency is to be determined through the use of a small-scale model that is to be tested in a water tunnel. For the small-scale model that is to be tested in a water tunnel. For the model Dm=20mm and the water temperature is 20 .℃model Dm=20mm and the water temperature is 20 .℃

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Example 7.5 Prediction of Prototype Example 7.5 Prediction of Prototype Performance from Model Data Performance from Model Data 2/22/2

Determine the model dimension, Hm, and the velocity at which the Determine the model dimension, Hm, and the velocity at which the test should be performed. If the shedding frequency ω for the model test should be performed. If the shedding frequency ω for the model is found to be 49.9Hz, what is the corresponding frequency for the is found to be 49.9Hz, what is the corresponding frequency for the prototype? prototype?

For air at standard condition For air at standard condition For water at 20For water at 20℃℃,,

35 m/kg23.1,sm/kg1079.1

3water

3water m/kg998,sm/kg101

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Example 7.5 Example 7.5 SolutionSolution1/41/4

Step 1:List all the dimensional variables involved. Step 1:List all the dimensional variables involved. ωω D,H,V,D,H,V,ρ,μρ,μ k=6 dimensional variables. k=6 dimensional variables.

Step 2:Select primary dimensions F,L and T. List the Step 2:Select primary dimensions F,L and T. List the dimensions of all variables in terms of primary dimensions of all variables in terms of primary dimensions. r=3 primary dimensionsdimensions. r=3 primary dimensions

TMLTFLLTV

LHLDT2241

1

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81

Example 7.5 Example 7.5 SolutionSolution2/42/4

Step 3: Determine the required number of pi terms.Step 3: Determine the required number of pi terms.

k-r=6-3=3k-r=6-3=3 Step 4:Select repeating variables D,V, Step 4:Select repeating variables D,V, μμ.. Step Step 5~6:combining the repeating variables with each of 5~6:combining the repeating variables with each of

the other variables in turn, to form dimensionless groups.the other variables in turn, to form dimensionless groups.

VDVD

D

HVHD

V

DVD

333

222111

cba3

cba2

cba1

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82

Example 7.5 Example 7.5 SolutionSolution3/43/4

The functional relationship isThe functional relationship is

The prototype and the model must have the same The prototype and the model must have the same phenomenon.phenomenon.

VD,

D

H

V

D

m

mmm

m

m

m

mm DV,

D

H

V

D

Strouhal numberStrouhal number

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Example 7.5 Example 7.5 SolutionSolution4/44/4

The Design conditions.The Design conditions.

Then….Then….

m

m

D

H

D

H

m

mmm DVVD

mm60...DD

HH mm s/m9.13...V

D

DV

mm

mm

Hz0.29...D

D

V

Vm

m

m

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Model ScalesModel Scales

The ratio of a model variable to the corresponding The ratio of a model variable to the corresponding prototype variable is called the scale for that variable.prototype variable is called the scale for that variable.

2

m2

1

m1

m2

m1

2

1

m

V

Vm

V

m

Length ScaleLength Scale

Velocity ScaleVelocity Scale

Density ScaleDensity Scale

Viscosity ScaleViscosity Scale

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Validation of Models DesignValidation of Models Design

The purpose of model design is to predict the effects of The purpose of model design is to predict the effects of certain proposed changes in a given prototype, and in this certain proposed changes in a given prototype, and in this instance some actual prototype data may be available.instance some actual prototype data may be available.

Validation of model design ?Validation of model design ? The model can be designed, constructed, and tested, and The model can be designed, constructed, and tested, and

the model prediction can be compared with these data. the model prediction can be compared with these data. If If the agreement is satisfactorythe agreement is satisfactory, then the model can be , then the model can be changed in the desired manner, and the corresponding changed in the desired manner, and the corresponding effect on the prototype can be predicted with increased effect on the prototype can be predicted with increased confidence.confidence.

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Distorted ModelsDistorted Models

In many model studies, to achieve dynamic similarity In many model studies, to achieve dynamic similarity requires duplication of several dimensionless groups. requires duplication of several dimensionless groups.

In some cases, complete dynamic similarity between In some cases, complete dynamic similarity between model and prototype may not be attainable. If one or more model and prototype may not be attainable. If one or more of the similarity requirements are not met, for example, if of the similarity requirements are not met, for example, if , then it follows that the prediction equation , then it follows that the prediction equation

is not true; that is, is not true; that is, MODELS for which one or more of the similarity MODELS for which one or more of the similarity

requirements are not satisfied are called requirements are not satisfied are called DISTORTED DISTORTED MODELSMODELS. .

m22

m11 m11

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Distorted Models Distorted Models EXAMPLE-1 1/3EXAMPLE-1 1/3

Determine the drag force on a surface ship, complete Determine the drag force on a surface ship, complete dynamic similarity requires that both Reynolds and Froude dynamic similarity requires that both Reynolds and Froude numbers be duplicated between model and prototype.numbers be duplicated between model and prototype.

To match Froude numbers To match Froude numbers between model and prototypebetween model and prototype

2/1p

pp2/1

m

mm

)g(

VFr

)g(

VFr

p

ppp

m

mmm

VRe

VRe

Froude numbersFroude numbers

Reynolds numbersReynolds numbers

2/1

p

m

p

m

V

V

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Distorted Models Distorted Models EXAMPLE-1EXAMPLE-1 2/32/3

To match Reynolds numbers between model and To match Reynolds numbers between model and prototypeprototype

p

m

p

m

p

m

V

V

2/3

p

m

p

m

2/1

p

m

p

m

If If mm/ / p p equals 1/100(a typical length scale for ship equals 1/100(a typical length scale for ship

model tests) , then υmodel tests) , then υmm/υ/υp p must be 1/1000.must be 1/1000.

>>> The kinematic viscosity ratio required to >>> The kinematic viscosity ratio required to duplicate Reynolds numbers cannot be attained.duplicate Reynolds numbers cannot be attained.

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Distorted Models Distorted Models EXAMPLE-1EXAMPLE-1 3/33/3

It is impossible in practice for this model/prototype scale It is impossible in practice for this model/prototype scale of 1/100 to satisfy both the Froude number and Reynolds of 1/100 to satisfy both the Froude number and Reynolds number criterianumber criteria; ; at best we will be able to satisfy only at best we will be able to satisfy only one of them.one of them.

If water is the only practical liquid for most model test of If water is the only practical liquid for most model test of free-surface flows, a free-surface flows, a full-scale test is required to obtain full-scale test is required to obtain complete dynamic similaritycomplete dynamic similarity..

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Distorted Models Distorted Models EXAMPLE-2EXAMPLE-2 1/21/2

In the study of open channel or free-surface flows. In the study of open channel or free-surface flows. Typically in these problems both the Reynolds number Typically in these problems both the Reynolds number and Froude number are involved. and Froude number are involved.

To match Froude numbers To match Froude numbers between model and prototypebetween model and prototype

2/1pp

pp2/1

mm

mm

)g(

VFr

)g(

VFr

Froude numbersFroude numbers

p

pppp

m

mmmm

VRe

VRe

Reynolds numbersReynolds numbers

2/1

p

m

p

m

V

V

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91

Distorted Models Distorted Models EXAMPLE-2EXAMPLE-2 2/22/2

To match Reynolds numbers between model and To match Reynolds numbers between model and prototypeprototype

m

p

m

p

p

m

p

m

V

V

If If mm/ / p p equals 1/100(a typical length scale for ship equals 1/100(a typical length scale for ship

model tests) , then υmodel tests) , then υmm/υ/υp p must be 1/1000.must be 1/1000.

>>>The kinematic viscosity ratio required to >>>The kinematic viscosity ratio required to duplicate Reynolds numbers cannot be attained.duplicate Reynolds numbers cannot be attained.

p

m

mp

pm2/3

m

p

mp

pm

p

m

p

m

/

/

/

/

V

V

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Typical Model StudiesTypical Model Studies

Flow through closed conduits.Flow through closed conduits. Flow around immersed bodies.Flow around immersed bodies. Flow with a free surface.Flow with a free surface.

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Flow Through Closed Conduits Flow Through Closed Conduits 1/51/5

This type of flow includes pipe flow and flow through This type of flow includes pipe flow and flow through valves, fittings, and metering devices. valves, fittings, and metering devices.

The conduits are often circular, they could have other The conduits are often circular, they could have other shapes as well and may contain expansions or shapes as well and may contain expansions or contractions.contractions.

Since there are no fluid interfaces or free surface, the Since there are no fluid interfaces or free surface, the dominant forces are inertial and viscous forces so that the dominant forces are inertial and viscous forces so that the Reynolds number is an important similarity parameter.Reynolds number is an important similarity parameter.

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Flow Through Closed Conduits Flow Through Closed Conduits 2/52/5

For low Mach numbers (Ma<0.3), compressibility effects For low Mach numbers (Ma<0.3), compressibility effects are usually negligible for both the flow of liquids or gases.are usually negligible for both the flow of liquids or gases.

For flow in closed conduits at low Mach numbers, and For flow in closed conduits at low Mach numbers, and dependent pi term, such as pressure drop, can be expressed dependent pi term, such as pressure drop, can be expressed asas

Dependent pi term=Dependent pi term=

V

,,i

Where Where is some particular length of the system and is some particular length of the system and ii

represents a series of length terms, represents a series of length terms, εε/ / is the relative is the relative roughness of the surface, and roughness of the surface, and ρρVV//μμ is the Reynolds number. is the Reynolds number.

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Flow Through Closed Conduits Flow Through Closed Conduits 3/53/5

To meet the requirement of geometric similarityTo meet the requirement of geometric similarity

To meet the requirement of Reynolds numberTo meet the requirement of Reynolds number

mm

i

im

m

mi

m

im

mm

mm

m

mmm

V

VVV

If the same fluid is used, thenIf the same fluid is used, then

/VVV

Vm

m

m

1m

m

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96

Flow Through Closed Conduits Flow Through Closed Conduits 4/54/5

The fluid velocity in the model will be larger than that in The fluid velocity in the model will be larger than that in the prototype for any length scale less than 1. Since length the prototype for any length scale less than 1. Since length scales are typically much less than unity.scales are typically much less than unity.

Reynolds number similarity may be difficult to achieve Reynolds number similarity may be difficult to achieve because of the large model velocities required.because of the large model velocities required.

VVm

/VVV

Vm

m

m

1

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97

Flow Through Closed Conduits Flow Through Closed Conduits 5/55/5

With these similarity requirements satisfied, it follows that With these similarity requirements satisfied, it follows that the dependent pi term will be equal in model and the dependent pi term will be equal in model and prototype. For example,prototype. For example,

The prototype pressure dropThe prototype pressure drop

21V

p

Dependent pi termDependent pi term

m

2

mmp

V

Vp

mpp In general

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98

Example 7.6 Reynolds Number SimilarityExample 7.6 Reynolds Number Similarity

Model test are to be performed to study the flow through a large Model test are to be performed to study the flow through a large valve having a 2-ft-diameter inlet and carrying water at a flowrate of valve having a 2-ft-diameter inlet and carrying water at a flowrate of 30cfs. The working fluid in the model is water at the same 30cfs. The working fluid in the model is water at the same temperature as that in the prototype. Complete geometric similarity temperature as that in the prototype. Complete geometric similarity exits between model and prototype, and the model inlet diameter is exits between model and prototype, and the model inlet diameter is 30 in. Determine the required flowrate in the model. 30 in. Determine the required flowrate in the model.

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Example 7.6 Example 7.6 SolutionSolution

D

D...

VA

AV

Q

Q mmmm

To ensure dynamic similarity, the model tests should be run so that

m

m

m

mmm D

D

V

VVDDVReeR

Same fluid used in the model and prototypeSame fluid used in the model and prototype

cfs75.3)s/ft30((2ft)

(3/12ft)Q 3

m

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100

Flow Around Immersed Bodies Flow Around Immersed Bodies 1/71/7

This type of flow includes flow around aircraft, This type of flow includes flow around aircraft, automobiles, golf balls, and building.automobiles, golf balls, and building.

For these problems, geometric and Reynolds number For these problems, geometric and Reynolds number similarity is required.similarity is required.

Since there are no fluid interfaces, surface tension is not Since there are no fluid interfaces, surface tension is not important. Also, gravity will not affect the flow pattern, so important. Also, gravity will not affect the flow pattern, so the Froude number need not to be considered.the Froude number need not to be considered.

For incompressible flow, the Mach number can be For incompressible flow, the Mach number can be omitted.omitted.

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101

Flow Around Immersed Bodies Flow Around Immersed Bodies 2/72/7

A general formulation for these problems isA general formulation for these problems is

V

,,i

Where Where is some characteristic length of the system and is some characteristic length of the system and ii

represents other pertinent lengths, represents other pertinent lengths, εε/ / is the relative is the relative roughness of the surface, and roughness of the surface, and ρρVV//μμ is the Reynolds number. is the Reynolds number.

Dependent pi term=Dependent pi term=

Model of the National Bank of Commerce, San Antonio, Texas, for measurement of peak, rms, and mean pressure distributions. The model is located in a long-test-section, meteorological wind tunnel.

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102

Flow Around Immersed Bodies Flow Around Immersed Bodies 3/73/7

Frequently, the dependent variable of interest for this type Frequently, the dependent variable of interest for this type of problem is the drag, D, developed on the body.of problem is the drag, D, developed on the body.

To meet the requirement of geometric similarityTo meet the requirement of geometric similarity

22D

V21

DC

The dependent pi terms would usually be expressed in the form of a drag coefficient

mm

i

im

m

mi

m

im

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103

Flow Around Immersed Bodies Flow Around Immersed Bodies 4/74/7

To meet the requirement of Reynolds number similarityTo meet the requirement of Reynolds number similarity

m

m

mm

mm

m

mmm

V

VVV

m

2

m

2

mm2m

2mm

m

22D

V

VD

V21

D

V21

D

The same fluid is used, thenThe same fluid is used, then

/VVV

Vm

m

m

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104

Flow Around Immersed Bodies Flow Around Immersed Bodies 5/75/7

The fluid velocity in the model will be larger than that in The fluid velocity in the model will be larger than that in the prototype for any length scale less than 1. Since length the prototype for any length scale less than 1. Since length scales are typically much less than unity.scales are typically much less than unity.

Reynolds number similarity may be difficult to achieve Reynolds number similarity may be difficult to achieve because of the large model velocities required.because of the large model velocities required.

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Flow Around Immersed Bodies Flow Around Immersed Bodies 6/76/7

How to reduce the fluid velocity in the model ?How to reduce the fluid velocity in the model ?

A different fluid is used in the model such thatA different fluid is used in the model such that 1/m

For example, the ratio of the kinematic viscosity of water to that For example, the ratio of the kinematic viscosity of water to that of air is approximately 1/10, so that if the prototype fluid were of air is approximately 1/10, so that if the prototype fluid were air, test might be run on the model using water. air, test might be run on the model using water.

This would reduce the required model velocity, but This would reduce the required model velocity, but it still may be difficult to achieve the necessary it still may be difficult to achieve the necessary velocity in a suitable test facility, velocity in a suitable test facility, such as a water such as a water tunnel.tunnel.

VVm

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106

Flow Around Immersed Bodies Flow Around Immersed Bodies 7/77/7

How to reduce the fluid velocity in the model ?How to reduce the fluid velocity in the model ?

Same fluid with different density.. Same fluid with different density.. mm>>

An alternative way to reduce VAn alternative way to reduce Vmm is to is to

increase the air pressure in the tunnel so that increase the air pressure in the tunnel so that mm>>. The pressurized tunnels are obviously . The pressurized tunnels are obviously

complicated and expensive.complicated and expensive.

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107

Example 7.7 Model Design Conditions and Example 7.7 Model Design Conditions and Predicted Prototype PerformancePredicted Prototype Performance

The drag on an airplane cruising at 240 mph in standard air is to be The drag on an airplane cruising at 240 mph in standard air is to be determined from tests on a 1:10 scale model placed ina pressurized determined from tests on a 1:10 scale model placed ina pressurized wind tunnel. To minimize compressibility effects, the airspeed in wind tunnel. To minimize compressibility effects, the airspeed in the wind tunnel is also to be 240 mph. Determine the required air the wind tunnel is also to be 240 mph. Determine the required air pressure in the tunnel (assuming the same air temperature for model pressure in the tunnel (assuming the same air temperature for model and prototype), and the drag on the prototype corresponding to a and prototype), and the drag on the prototype corresponding to a measured force of 1 lb on the model. measured force of 1 lb on the model.

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Example 7.7 Example 7.7 SolutionSolution1/21/2

The Reynolds numbers in model and prototype are the same. Thus,

VV

m

mmm

VVmm=V, =V, mm/ / =1/10=1/10

m

mm

mm 10V

V

The same fluid with ρThe same fluid with ρmm=ρ and μ=ρ and μmm=μ cannot be used =μ cannot be used

if Reynolds number similarity is to be maintained.if Reynolds number similarity is to be maintained.

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109

Example 7.7 Example 7.7 SolutionSolution2/22/2

10m

We assume that an increase in pressure does not We assume that an increase in pressure does not significantly change the viscosity so that the required significantly change the viscosity so that the required increase in density is given by the relationshipincrease in density is given by the relationship

10p

p mm

For ideal gas

...DV

D

V

D2

m2

mm21

m22

21

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110

Flow Around Immersed Bodies at High Flow Around Immersed Bodies at High Reynolds Number Reynolds Number 1/31/3

Unfortunately, in many situations the flow characteristics Unfortunately, in many situations the flow characteristics are not strong influenced by the Reynolds number over the are not strong influenced by the Reynolds number over the operating range of interest.operating range of interest.

Consider the variation in the drag coefficient with the Consider the variation in the drag coefficient with the Reynolds number for a smooth sphere of diameter d Reynolds number for a smooth sphere of diameter d placed in a uniform stream with approach velocity, V.placed in a uniform stream with approach velocity, V.

At high Reynolds numbers the drag is often essentially At high Reynolds numbers the drag is often essentially independent of the Reynolds number.independent of the Reynolds number.

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111

Flow Around Immersed Bodies at High Flow Around Immersed Bodies at High Reynolds Number Reynolds Number 2/32/3

The effect of Reynolds number on the drag coefficient, CD for a

smooth sphere with CD = D/ ½ AρV2, where A is the projected area

of sphere, πd2/4.

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112

Flow Around Immersed Bodies at High Flow Around Immersed Bodies at High Reynolds Number Reynolds Number 3/33/3

For problems involving high velocities in which the Mach For problems involving high velocities in which the Mach number is greater than about 0.3, the influence of number is greater than about 0.3, the influence of compressibility, and therefore the Mach number (or compressibility, and therefore the Mach number (or Cauchy number), becomes significant.Cauchy number), becomes significant.

In this case complete similarity requires not only In this case complete similarity requires not only geometric and Reynolds number similarity but also Mach geometric and Reynolds number similarity but also Mach number similarity so thatnumber similarity so that

m

mmm

m

c

c

c

V

c

V

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113

Flow with a Free Surface Flow with a Free Surface 1/81/8

This type of flow includes flow in canals, rivers, This type of flow includes flow in canals, rivers, spillways, and stilling basics, as well as flow around ship.spillways, and stilling basics, as well as flow around ship.

For this class of problems, gravitational, inertial forces, For this class of problems, gravitational, inertial forces, and surface tension are important and, therefore, the and surface tension are important and, therefore, the Froude number and Weber number become important Froude number and Weber number become important similarity parameters.similarity parameters.

Since there is a free surface with a liquid-air interface, Since there is a free surface with a liquid-air interface, forces due to surface tension may be significant, and the forces due to surface tension may be significant, and the Weber number becomes another similarity parameter that Weber number becomes another similarity parameter that needs to be considered along with the Reynolds number.needs to be considered along with the Reynolds number.

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114

Flow with a Free Surface Flow with a Free Surface 2/82/8

A general formulation for these problems isA general formulation for these problems is

To meet the requirement of Froude number similarityTo meet the requirement of Froude number similarity

2i V

,g

V,

V,,Dependent pi term=Dependent pi term=

Where Where is some characteristic length of the system and is some characteristic length of the system and ii

represents other pertinent lengths, represents other pertinent lengths, εε/ / is the relative is the relative roughness of the surface, and roughness of the surface, and ρρVV//μμ is the Reynolds number. is the Reynolds number.

g

V

g

V

mm

m ggm

mm

V

V

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115

Flow with a Free Surface Flow with a Free Surface 3/83/8

To meet the requirement of To meet the requirement of Reynolds number and Froude Reynolds number and Froude numbernumber similarity similarity

m

m

mm

mm

m

mmm

V

VVV

The working fluid for the prototype is normally either freshwater The working fluid for the prototype is normally either freshwater or seawater and the length scale is small. or seawater and the length scale is small. It is virtually impossible to satisfy , so models It is virtually impossible to satisfy , so models involving free-surface flows are usually distorted.involving free-surface flows are usually distorted.

2/3m /

2/3m )(

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116

Flow with a Free Surface Flow with a Free Surface 4/84/8

The problem is further complicated if an attempt is made The problem is further complicated if an attempt is made to model surface tension effects, since this requires the to model surface tension effects, since this requires the equality of Weber numbers, which leads to the conditionequality of Weber numbers, which leads to the condition

22

m2

mmm2

m

m2

mm

V

V

/

/VV

For the kinematic surface tension For the kinematic surface tension σσ//ρρ. It is evident that the same . It is evident that the same fluid cannot be used in model and prototype if we are to have fluid cannot be used in model and prototype if we are to have similitude with respect to surface tension effects for .similitude with respect to surface tension effects for .1

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117

Flow with a Free Surface Flow with a Free Surface 5/85/8

Fortunately, in many problems involving free-surface Fortunately, in many problems involving free-surface flows, both surface tension and viscous effect are small flows, both surface tension and viscous effect are small and consequently strict adherence to Weber and Reynolds and consequently strict adherence to Weber and Reynolds number similarity is not required.number similarity is not required.

Certainly, surface tension is not important in large Certainly, surface tension is not important in large hydraulic structures and rivers.hydraulic structures and rivers.

Our only concern would be if in a model the depths were Our only concern would be if in a model the depths were reduced to the point where surface tension becomes an reduced to the point where surface tension becomes an important factor.important factor.

..

How to overcome this problem ?How to overcome this problem ?

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118

Flow with a Free Surface Flow with a Free Surface 6/86/8

Different horizontal and vertical length scales, which Different horizontal and vertical length scales, which introduce geometric distortion, are often used to eliminate introduce geometric distortion, are often used to eliminate surface tension effects in the model.surface tension effects in the model.

Although this approach eliminates surface tension effects Although this approach eliminates surface tension effects in the model, it introduces geometric distortion that must in the model, it introduces geometric distortion that must be accounted for empirically, usually by increasing the be accounted for empirically, usually by increasing the model surface roughness. model surface roughness. Verification test in the model must be made. Model Verification test in the model must be made. Model

roughness can be adjusted to give satisfactory roughness can be adjusted to give satisfactory agreement between model and prototype.agreement between model and prototype.

..

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Flow with a Free Surface Flow with a Free Surface 7/87/8

For large hydraulic structures, such as dam spillways, the For large hydraulic structures, such as dam spillways, the Reynolds numbers are large so that viscous forces are Reynolds numbers are large so that viscous forces are small in comparison to the force due to gravity and inertia.small in comparison to the force due to gravity and inertia.

In this case Reynolds number similarity is not maintained In this case Reynolds number similarity is not maintained and models are designed on the basis of Froude number and models are designed on the basis of Froude number similarity. similarity.

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Flow with a Free Surface Flow with a Free Surface 8/88/8

A scale hydraulic model (1:197) of the Guri Dam in Venezuela which is used to simulate the characteristics of the flow over and below the spillway and the erosion below the spillway.

The model Reynolds The model Reynolds numbers are large so that numbers are large so that they are not required to they are not required to equal to those of the equal to those of the prototype.prototype.

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Example 7.8 Froude Number SimilarityExample 7.8 Froude Number Similarity

A certain spillway for a dam is 20 m wide and is designed to carry A certain spillway for a dam is 20 m wide and is designed to carry 125 m125 m33/s at flood stage. A 1:15 model is constructed to study the /s at flood stage. A 1:15 model is constructed to study the flow characteristics through the spillway. Determine the required flow characteristics through the spillway. Determine the required model width and flowrate. What operating time for the model model width and flowrate. What operating time for the model corresponds to 1 24-hr period in the prototype? The effects of corresponds to 1 24-hr period in the prototype? The effects of surface tension and viscosity are to be neglected.surface tension and viscosity are to be neglected.

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Example 7.8 Example 7.8 SolutionSolution1/21/2

The width, wm, of the model of spillway is obtained from the length scale

With the neglect of surface tension and viscosity, the dynamic similarity will be achieved if the Froude numbers are equal between model and prototype

m33.115

m20w

15

1

w

wm

m

g

V

g

V

mm

m ggm

mm

V

V

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123

Example 7.8 Example 7.8 SolutionSolution2/22/2

The flowrate

s/m143.0...Q)(Q

VA

AV

Q

Q

32/5m

2mmmmm

m

m

mm

mm V

V

t

t

t

t

V

V

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124

Similitude Based on Governing Differential Similitude Based on Governing Differential Equations Equations 1/51/5

For a steady incompressible two-dimensional flow of a For a steady incompressible two-dimensional flow of a Newtonian fluid with constant viscosity.Newtonian fluid with constant viscosity.

The mass conservation equation isThe mass conservation equation is

The Navier-Stokes equations areThe Navier-Stokes equations are

Has dimensions of 1/time.Has dimensions of 1/time.0y

v

x

u

2

2

2

2

2

2

2

2

y

v

x

vg

y

p

y

vv

x

vu

y

u

x

u

x

p

y

uv

x

uu Has dimensions of Has dimensions of

force/volumeforce/volume

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125

Similitude Based on Governing Differential Similitude Based on Governing Differential Equations Equations 2/52/5

How to non-dimensionalize these equations ?How to non-dimensionalize these equations ?

tt

p

pp

V

vv

V

uu

yy

xx *

0

*****

2*

*2

22

2

*

*

x

uV

x

u

xx

u

x

uV

x

u

0y

v

x

u

The mass conservation equationThe mass conservation equation

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126

Similitude Based on Governing Differential Similitude Based on Governing Differential Equations Equations 3/53/5

22

22

y

v

x

v

VV

g

y

p

V

p

y

vv

x

vu

t

v

V

y

u

x

u

Vx

p

V

p

y

uv

x

uu

t

u

V

22

220

22

20

Strouhal numberStrouhal number Euler numberEuler number

The Navier-Stokes equationsThe Navier-Stokes equations Reynolds numberReynolds number

Reciprocal of the square Reciprocal of the square of the Froude numberof the Froude number

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127

Similitude Based on Governing Differential Similitude Based on Governing Differential Equations Equations 4/54/5

From these equations it follows that if two systems are From these equations it follows that if two systems are governed by these equations, then the solutions (in terms governed by these equations, then the solutions (in terms of u*,v*,p*,x*,y*, and t*) will be the same if the of u*,v*,p*,x*,y*, and t*) will be the same if the four four parametersparameters are equal for the two systems. are equal for the two systems.

The two systems will be dynamically similar. Of course, The two systems will be dynamically similar. Of course, boundary and initial conditionsboundary and initial conditions expressed in expressed in dimensionless form must also be equal for the two dimensionless form must also be equal for the two systems, and this will require complete geometric systems, and this will require complete geometric similarity.similarity.

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Similitude Based on Governing Differential Similitude Based on Governing Differential Equations Equations 5/55/5

These are the same similarity requirements that would be These are the same similarity requirements that would be determined by a dimensional analysis if the same variables determined by a dimensional analysis if the same variables were considered. These variables appear naturally in the were considered. These variables appear naturally in the equations.equations.

All the common dimensionless groups that we previously All the common dimensionless groups that we previously developed by using dimensional analysis appear in the developed by using dimensional analysis appear in the governing equations that describe fluid motion when these governing equations that describe fluid motion when these equations are expressed in term of dimensionless variables.equations are expressed in term of dimensionless variables.

The use of governing equations to obtain similarity laws The use of governing equations to obtain similarity laws provides an alternative to conventional dimensional analysis.provides an alternative to conventional dimensional analysis.