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- . - - - - - - - . . . I , . , , 1. . - . . - . 9. . 9 I . : . . : . . , ; , ' : , , , . . , . I . . . , - . . . . , : , . . , . , -V .. 19 9 . , 9 1 9 , , . ,; . .. . 9 . . I- * , : , . 9 - ': 4 . , I . . 0 , t * 1 , . - . . - . I . : . , . . , . , , 9 . . , - , , I . 9 1 , - : - V . : , , , . - , . , , . K , . , k . . , , - . . , 9. . 9 9 . : : . r - : . . . , . . : - , , Ic 1 9, k . . 9 1 9 . . . 9 9 : - : . ; . : . . . . I- . . . 9 :1 9 , 9 , 9 . 91 9i 1 . . , . : , : : , : . , t , l i : . . . . 1 9 , 9 . ., , . 9, : .t 9 9 . 9 9 I . . . , ! , . . . . . 9 , . .9 1 . 9 . , 9 " . j , 9 9 .. I . I ;,, 9 : 9 . - - , . . . l . , . . , / " I , I ,; 9 I I I . 9 , - . . . . , - : . 9 1 , . . 1 9 . 1. . , : , : : , , , . . % I- - 9 I 9 . 9 . , - . 9 9 . : ::, ! - . 9. - 9 9 9 1 - 9 ; . 9 1 z . 9 1 . . 1 9 . 9 1 . 9 . 9 . 1 9 - - 1 9 . . . 9 . 9 . 9 . , . - - -w . . 1 9 . - I . . . I , -- - . . . I . . : , . . . . . . 9 . . - . . . . I , - . . , . . 9 9 . . . 1 9 9 9 . I . 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Page 1: :i ., R .. ., O DARY

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Page 2: :i ., R .. ., O DARY

BOUNDARY LAYER ON AN AIRFOIL IN A CASCADE

by

CARL R. PETERSON

Under the sponsorship of:

General Electric CompanyAllison Division of General Motors Corporation

Westinghouse Electric Corporation

Gas Turbine LaboratoryReport Number 49

December1958

Massachusetts Institute of Technology

Page 3: :i ., R .. ., O DARY

ACKNOWLEDGEMENTS

This report was originally the authors master's thesis. The

author would like to express his gratitude to all those who assisted on

this project. The advice and guidance of Professors A. H. Stenning, the

thesis adviser, and E. S. Taylor kept the work moving towards the proper

end. The considerable assistance of Mr. Stephen Montgomery is especially

appreciated.

The joint efforts of Mr. Basil Kean and Mr. Herbert Johnston

produc'ed the probe. Mr. Dalton Baugh produced nearly everything else as

it was necessary.

Natalie Appleton did the typing.

Page 4: :i ., R .. ., O DARY

ABSTRACT

A study of the turbulent boundary layer on an airfoil in a

cascade is presented. The major portion of the observations are on the

suction surface of the airfoil. The effect of added diffusion across

the cascade due to a three-dimensional flow is included. Empirical equa-

tions describing the boundary layer in terms of momentum and displacement

thickness growth as a function of free-stream diffusion axe developed.

Shape factor is also related to free-stream diffusion. A reasonable check

with an existing separation criterion is observed. An appendix contains

a discussion of chord-wise integrating of various boundary layer parameters.

Page 5: :i ., R .. ., O DARY

TABLE OF CONTENTS

Acknowledgements

Abstract

List of Symbols

Introduction 1

Description of Apparatus 2

Experimental Procedure

Re sults 7

Data 7

Frictionless Analysis 8

Momentum Thickness Correlation 9

Displacement Thickness Correlation 12

Shape Factor Correlation 13

Conclusions 14

Appendix I - Probe Design and Calibration A-l

Appendix II - Chord Integrating Techniques A-5

Bibliography

Tables T-l

Numerical Figures

Page 6: :i ., R .. ., O DARY

LIST OF FIGURES

1 9/29R1 versus U/UMax correlation

2 5*/ * versus U/LU correlation

5 II versus U/Umax correlation

4 - 5 Presentation of data: 9, g*, versus chord length

6 - 9 Typical velocity profiles: u/U versus y/8

10 Static pressure distributions

11 Probe design diagram

12 Probe total pressure error as function of yaw angle

13 General view of cascade

14 Downstream view of probe in position

15 - 16 Carbon black traces showing probe support wake

TABLES

I Velocity distribution coordinates

II Free stream dynamic pressures

Page 7: :i ., R .. ., O DARY

LIST OF SYMBOLS

1 distance from leading edge to minimum pressure point

p pressure

u velocity in boundary layer

x chordal distance from leading edge

y normal distance from surface of airfoil

H shape factor

U free-stream velocity

boundary laeer thickness (to u/U = .99)

dispwaeement thickness

momentum thickness

kinetic viscosity

Subscript s

max maximum value

o stagnation value

s local static value

Rl theoretical (Blasius) values based on 1 Reynolds number

co far from a flat plate or upstream of the cascade (refer tostatic pressure)

Identification of cascade conditions:

Example: 2D - 55 - 40 - S

First Group - without screen (2D), or with screen (OD)

Second Group - cascade angle

Third Group - percent chord

Last Letter - suction (S) or pressure (P) surface

Page 8: :i ., R .. ., O DARY

DEFINITIONS

Cascade angle

Shape factor, Hl

Displacement thickne ss

Momentum thickness

angle between normal to cascade And flowdirection (stagger angle = 45*)

Ha */@

-Qd ySJ& -5)d

Page 9: :i ., R .. ., O DARY

BOUNDARY LAYER ON AN AIBFOIL IN A CASCADE

INTRODUCTION

In predicting the performance of turbomachine blading, two-

dimensional cascade data is generally used, although the flow is not

two- dimensional. The radial distribution of axial velocity may change

across a blade row. In order to satisfy continuity, this causes a de-

viation of s:reamlines from a cylindrical pattern, as shown in the fol-

lowing sketch.

As can be seen, this in effect imposes an added diffusion near one end

of the blades.

As part of an overall program investigating the effect of this

added diffusion, the behavior of the boundary layer on the blade surface

in such a region is here observed. The added diffusion is brought about

Page 10: :i ., R .. ., O DARY

-2-

by placing an obstruction downstream of the span-wise centerline of a

cascade. The centerline of symmetry then corresponds to one casing wall

in the previous sketch, except that for this investigation it is free of

the complications of wall friction.

DESCRIPTION OF APPARATUS

The Cascade

The investigations are being made on a newly constructed low

speed wind tunnel. The tunnel construction allows continuous variation

of inlet angle at constant cascade stagger over a wide range. The cas-

cade consists of nine blades with 4 7/8 inch chord, 20 inch span, and

NACA 65-410 section. The chord Reynolds number is roughly 3 x 105, cor-

responding to a velocity of 115 feet per second. The turbulence level

has, as yet, not been determined, but it is known to be high.

For a complete discussion of the tunnel design and performance,

see Gas Turbine Laboratory Report Number 43.

The Probe

One of the major objections to total pressure probes for use

in boundary layer studies is one of physical size, as limited by reason-

able response rates. The available pressure sensing apparatus allowed

reasonable response rates even with the very small probe used. The very

availability of this pressure sensing apparatus was a major factor in the

choice of such a probe.

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-3-

Another objection to the use of finite size total pressure probes

is their behavior in a total pressure gradient. It has been shown that the

displacement effect caused by such a gradient is exactly off-set by the in-

terference effect as such a probe approaches a wall (1). Thus no correc-

tion of the data was necessary, either for pressure gradient or for wall

effects. There is an interference effect between a hotwire and a wall so

that the total pressure probe appears to be advantageous in this respect.

The probe used was a three-hole cobra probe with tip dimensions

.018 x .054 inches. The probe design and calibration are discussed in

detail in the appendix.

Pressure Sensing Apparatus

The pressure was sensed by a Dynisco pressure transducer of t.10

psi range. Another such transducer of *.050 psi range is available for

yaw determination. The unbalance of a bridge circuit tbpntaining the trans-

ducer is amplified by a D.C. amplifier produced by the Dynamic Instrument

Company, Caftbridge, Massachusetts. The bridge is balanced, as indicated

by a galvamometer, with a potentiometer in the circuit - the potentiometer

reading then being a measure of the pressure. Thie apparatus was calibrated

against an NACA micromanometer, and found to be linear over the entire

range of allowable pressures. The calibration has been repeated on sub-

sequent occasions and the constant of proportionality found to vary less

than one percent.

Blade static pressures were determined on a sloping mapcmeter

board containing 31 tubes. The inaccuracies due to non-flat boards and

non-uniform tubes were minimized by careful construction and selective.

assembly. The slope of the board and the specific gravity of the manom-

eter oil are such that five inches of oil on the board are equal to one

inch of water.

Page 12: :i ., R .. ., O DARY

EXPERIMENTAL PROCEEDURE

The added diffusion over a central portion of the span was pro-

duced by an eight inch perforated metal screen placed four inches (perpendi-

cular to the cascade) downstream of the blade trailing edges as shown be-

low. The perforations are 1/8 inch diameter holes giving a screen of 40%

open area.

I:

The choice of screen size, geometry, etc., and its effects on

the flow are covered in detail in Gas Turbine Laboratory Report Number 48.

Whenever possible, tests were made at constant velocity as de-

termined by the difference in static pressures between a position just up-

stream of the cascade and the plenum. Velocity was varied by the adjust-

ment of a bleed slot, downstream of the fan. For cascade angles of 520

and 56*, with the screen in place, the velocity could not be maintained

at 115 feet per second, even with the bleed slot fully closed.

Cascade angle was determined by a scale fixed directly to the

cascade support structure.

It was desired to obtain boundary layer traverses at several

chord positions, on both sides of the blade, for several cascade angles,

Page 13: :i ., R .. ., O DARY

-5-

with and without the downstream screen. This was first broken into two

cases - with and without the screen. Following this, since the most dif-

ficult probe adjustment was that of chord position, the data was taken at

each chord position for all cascade angles before moving to the next chord

position. All chord positions except 60 chord were reached from the rear

mounting position of the probe (see appendix for description of probe mech-

anism). The 60% position was reached from the forward mounting position.

Chord position was determined by measuring from the trailing edge of the

blade with an ordinary steel scale. After taking data without the screen,

the procedure was repeated unchanged for the cases with the screen in

position.

As outlined in the appendix, the change of probe-to-blade dis-

tance could be determined with high precision. It was also necessary to

determine one fixed probe position from which to measure all changes. In

the final procedure this was taken as the contact position - that is, with

the probe in contact with the blade surface. Each traverse was started at

the outer limit of the traverse range and continued in to the blade sur-

face. As the tip approached the blade the position increments were de-

creased. Pressure readings were taken at each position until no change

in pressure could be observed for a supposed change in tip position. This

meant that the tip was in contact with the blade, and was not actually

changing position. In regions of steady flow and steep pressure gradient

this was an extremely precise means of determining the contact position.

For unsteady regions or flat pressure gradients (near the trailing edge

at high cascade angles) the technique was not good. However, it was

nearly always possible to determine the contact position at a low angle

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-6-

of attack and use this information for the high angle of attack, since

the runs were made consecutively. It was found that the contact position

did not vary appreciably for two runs at the same chord position. When

it was not possible to run an unsteady traverse in conjunction with a

steady one it was necessary to determine contact position visually. This

resulted in only a slight loss in accuracy, but a great loss in convenience.

The range of probe traVerse was limited by the wedge dimensions

to slightly less than .30 inches. When readings at greater distance were

necessary the probe position was determined visually with gauge blocks,

using one of the adjustments mentioned in the appendix to extend the probe

range.

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-7-

RESULTS

Data

Figures 4 and 5 show the observed values of momentum thick-

ness, displacement thickness, and actual thickness (to u/U = .99).

Actual thickness was read directly from plots of u/U versus y since

the velocity gradients were such that it could be done with little un-

certainty. Momentum and displacement thicknesses were found by graphi-

cal integration of the appropriate areas.

Figures 6 through 9 show typical velocity profiles plotted on

a dimensionless basis. Attempts to plot all chord position curves on

one graph result in confusion, since the curves are very close together,

but not close enough to be considered one curve. Hence, complete velocity

profile data is presented in Table I. The unsteady readings shown are

not a true measure of flow unsteadiness since the probe response was so

slow. They are .a measure of the relative unsteadiness from one run to

another, however.

Figure 9 is of particular interest, since it shows an obviously

separated flow, although the exact shape of the profile near the wall can

only be estimated. The total pressure probe read a steady, low value in

the back-flow region. The probe tip was reversed (pointed downstream)

in this region, and the total pressure was then observed to be a little

higher. This indicated simply that there actually was a back flow. The

pressure readings could not have quantitative value, however, since the

probe tip was reading in the wake of its own support.

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-8-

Frictionless Analysis

In some cases it has been possible to analyze the outer por-

tion of boundary layers on a frictionless basis. In this analysis, the

outer portion of a boundary layer is approximated by a series of stream

tubes, each of constant velocity. Bernoulli' s equation, together with

the known static pressure distribution, and the continuity equation are

then sufficient to describe the downstream development of a given portion

of the profile. This analysis was applied in two cases in an attempt to

predict the 80 and 98% chord profiles, given the 60% profile and the static

pressure distribution. The analysis was found invalid.

Correlations

As with most complex phenomena, empirical correlation methods

are necessary for quantitative description of gross boundary layer behav-

ior. Two parameters are of primary interest; the momentum thickness and

the displacement thickness.

The development of a boundary layer between any point on an

airfoil and some other point downstream might be expected to be a func-

tion of the following:

1) Free-stream diffusion over the interval

2) Boundary layer characteristics at the up-

stream position

3) Skin friction over the interval

The diffusion may be expressed as the free-stream velocity

ratio over the interval. The upstream characteristics may be expressed

Page 17: :i ., R .. ., O DARY

-9-

in terms of the preceding parameters. A simple plot of momentum thick-

ness, 9, versus free-stream velocity ratio U/Umax, results in a good cor-

relation, indicating that skin friction is not an important variable.

Momentum Thickness

To make the experimental results more generally applicble it

is desirable to normalize the momentum thickness in the above plot with

some length characteristic of the flow. As observed by others (N), the

most significant length for this purpose la ae momentum thickness at the

minimum pressure point, since it may be assumed that transition from a

laminar to turbulent boundary layer occurs here. This also accounts for

the use of U as the significant velocity used in the correlation. Co-max

balt chloride tests and the static pressure distributions indicate that

transition and the minimum pressure point both occur very near the lead-

ing edge (on the suction surface), but they do not prcecisely locate the

position of either. It is therefore necessary to make assumpe>ns regard-

ing both the location of the minimum pressure point and the momentum thick-

ness at this point.

For those cases in which the minimum pressure point occurred

farther than 1.7% of the chord from the leading edge, the location and

magnitude of the minimum pressure could be determined with some certainty.

For cases in which the minimum pressure occurred nearer the leading edge

it was assumed that it occurred at 1.7% chord, and that its magnitude was

that value measured at the 1.7% pressure tap. With this imformation it

is possible to compute Umax or at least a good approximation to it.

The minimum pressure point momentum thickness must be calculated,

Page 18: :i ., R .. ., O DARY

-10-

since it is impossible to determine experimentally. Since the boundary

layer is laminar up to the minimum pressure point, one might assume Blasius

flat-plate flow to calculate the momentum thickness.

Then: 0 ,

and4

where x is the surface distance from the leading edge, and 1 is the x

distance to the minimum pressure point. Due to the curvature of the air-

foil, x or 1 is not actually equal to chordal distance, but for these

calculations it may be assumed so. The actual value of U varies from

zero at the stagnation point to Umax at the minimum pressure point. Umax

is of the order of twice the upstream U so a mean U may reasonably be taker

as the upstream U. With these assumptions, QR1 may be calculated.

The characteristic length must satisfy one further condition:

as U/Umax approaches one, 9 must approach the characteristic length. It

was empirically found that 2@Rl satisfied this last condition. In Figure 1

the resulting correlation of 9/29Rl versus U/Umax is shown. The data fits

the following empirical equation quite well:

e()

for

i-f>.51

The exponent, 5, has been observed by others (3).

Page 19: :i ., R .. ., O DARY

-11-

The factor, 2, while quite arbitrary, is only slightly more

arbitrary than the use of QRi. QRl is significant only in that it is

probably a function of the proper variables, , X, and U, . The actual

flow is far from flat-plate flow, and even if it were not, the Blasius

solution does not apply near a leading edge (6).

The actual flow probably included laminar separation followed

by reattachment as a turbulent boundary layer. Transition occurs, on a

flat-plate at least, for x Reynolds numbers of from 3 x 105 to

3 x 106 (6). The actual x Reynolds numbers were of the order of .4 x 104

to 1.4 x 10 , based on chordal distance and upstream velocity. Hence,

transition must have been the result of separation and reattachment.

Reference 3 contains a means of calculating the limiting pos-

sible energy recovery without separation in the form of the following em-

perical equation:

ELI s/FA]

where U2 = free-stream velocity at point of incipient separation

91 = minimum pressure point momentum thickness

L = length of pressure rise

In the present case

91 = 2GR1

Looking at the three- dimensional, 60* cascade angle case as the only ex-

ample of sharp separation, it may be seen from the static pressure or

velocity profile data that separation occurs at approximately 70/ chord.

Page 20: :i ., R .. ., O DARY

-12-

Then:

L 3 5.5 inches

With these figures in the above equation

V- 52

From Figure 1, this is seen to be in agreement with the point

where the momentum thickness increases very rapidly with decreasing U/Uma.

Due to the unusual pressure distribution on the pressure sur-

faces, these correlations can not be expected to apply.

Displacement Thickness

The same type of correlation may be ma, with displacement thick-

ness. Again, for the Blasius flow:

or

' = 2 .41 0 RL

(2)

It was not necessary to use an arbitrary multiple of to bring the dis-

placement thickness ratio to one as the velocity ratio approached one.

There is no reason to expect that a similar factor should appear in the

and 9 correlations, for if it did, it would indicate that the actual shape

factor at the minimum pressure point was equal to the Blasius shape factor.

In this particular case, at the minimum pressure point:

H~~~~; O = =g ea .

Page 21: :i ., R .. ., O DARY

This shape factor is characteristic of a flat-plate turbulent boundary

layer.

The resulting correlation, shown in Figure 2, gives the fol-

lowing equation: 5

L/IuIn both Figures 1 and 2 it can be seen that two sets of data

fall to the right of the curves, but parallel to it. Since the curves

are of the same shape, an error in U/Umax is possible. These two sets

of data are for the highest cascade angles for the two and three-dimen-

sional flows. These correspond to the greatest uncertainty in Umax. The

shift of the two sets of data corresponds to an error in Umax of less than

ten percent. An error in Umax would be an underestimation, tending to

shift the points in the observed direction.

Shape Factor

Equations (1), (2) and (3) may be combined to eliminate the

Blasius parameters, resulting in the following:

/ '.3az5 (t

H -This equation and the corresponding experimental data are

plotted in Figure 3. The equation is seen to be in excellent agreement

with the data over the range .51 < U/U < .81. For U/Umax < .51 the

flow is separated and equations (1) and (3) do not apply. Hence the data

can be expected to deviate. The data for U/Uax > .81 corresponds to

low cascade angles. In these cases transition may be taking place over

-13-

Page 22: :i ., R .. ., O DARY

an appreciable distance rather than occurring suddenly at the minimum

pressure point. Hence the shape factor may be expected to tend towards

higher (laminar) values as U/Uma approaches one in these cases.

Conclusions

Two conclusions may be drawn from these correlations. First,

as mentioned, the growth of the boundary layer is independent of x dimen-

sions or skin friction. Second, the geometry of the diffusion, whether

three-dimensional or two-dimensional, is not important. Both of these

conclusions indicate that free-stream diffusion is the variable of pri-

mary importance in boundary layer development. The conclusions are, of

course, drawn on relatively little data and are strictly valid only for

the geometries investigated. They are, however, in general agreement

with other observations.

The arbitrary nature of the Blasius parameters may be elim-

inated if it is desired to predict the subsequent development of a known

parameter.

Hence, 5

The same is true for displacement thickness:

* ,

Page 23: :i ., R .. ., O DARY

A-1

APPENDIX I

PROBE DESIGN AND CALIBRATION

Design

The probe used in this investigation was a three-hole cobra

probe especially designed to satisfy the particular requirements en-

countered. These requirements may be stated in the form of the four

criteria used in the probe design:

1) Small probe size

2) Flexibility of operating configuration

3) Rigid support for a given operating configuration

4) Accurate determination of probe tip position

A small probe tip was necessary in order to obtain a reasonable

amount of data within the thin boundary layers anticipated. The probe

tip was formed of three tubes of 0.018 inches outside diameter and 0.010

inches inside diameter silver-soldered together in the conventional cobra-

probe configuration. None of the tubes was flattened. -The included tip

angle was 600 for maximum sensitivity (2). Reasonable response rates were

obtained with such a probe tip by using a relatively rigid pressure sens-

ing system of low volume. The probe was connected to Dynisco transducers

with 18 inches of plastic tubing of approximately .025 inches inside di-

ameter. This system responded to a step change in pressure of 2 inches

of water in less than thirty seconds.

The carbon-black traces (Figure 15) show that the probe tip was

well out of the wake of its own support mechanism. The probe probably

altered the overall passage flow a little by its slight blockage of the

Page 24: :i ., R .. ., O DARY

A-2

passage as may be seen in Figure 14. It is assumed that errors due to

this effect are small.

Flexibility of operating configuration and rigid support in

position are slightly conflicting criteria, although they can be realized

simultaneously with careful workmanship. It was desired to use one probe

tip to cover all positions on the airfoil, that is, all chord positions

on both sides of the airfoil. Refering to Figure 11, different chord-wise

positions are attained by sliding the horizontal slide forward or back on

the cross support. The horizontal slide could be mounted as shown or re-

versed, that is, &xtending upstream from the cross support. When in the

upstream position it is necessary to rotate the probe banger 1800 with

respect to the horizontal slide at joint B. In any position the bottom

of the probe could be made tangent to the airfoil by proper rotation at

joint B. In order to span the entire chord it was necessary to provide

two cross support holes and wedge guides in the airfoil. When switch-

ing from side to side of the airfoil (separate airfoils were used for

each side) it is also necessary to rotate the probe tip 1800 with respect

to the probe hanger at joint A. This adjustment also allowed back-flow

measurements with the probe tip facing downstream as mentioned in the

text.

Rigidity in position is attained by insuring tight joints.

Joint A is a tight friction joint, the probe tip lock being a split sleeve

that fits tightly over the mating parts. The probe tip and probe hanger

are shaped in such a way that they mate in only two position, 180* apart.

Joint B is a carefully fitted friction joint. Due to the long slits in

the horizontal slide it was necessary to provide a sets-screw lock for the

joint at C. Joint D is a pinned joint.

Page 25: :i ., R .. ., O DARY

A-3

The traverse motion had to be both delicate and accurate, hence

a screw and wedge combination with considerable mechanical reduction of

motion was devised as shown in Figure 1.I. Contact between the wedge and

the wedge contact pin was maintained by spring in the main probe support.

Fine traverse adjustments were made by moving the wedge (slope of 10:1)

vertically with the wedge traverse screw (40 threads per inch). Coarse

position adjustment could be made by screwing the wedge contact pin in

or out of the wedge block. Very coarse adjustments were made by moving

the wedge block on the cross support, and holding it in position with

a set-screw.

Calibration

In the final configuration, probe position was calibrated as

a function of revolutions of the wedge traverse screw from some known

position. The tip position was calibrated against a series of objects

of known dimensions held against the airfoil, using the completion of an

electrical circuit to determine contact. With care the calibration

could be reproduced to within the uncertainty of the dimensions of the

gauge objects (about .001 inches). It was necessary to calibrate the

probe in this manner for each of the probe support locations. The probe

tip position was a linear function of wedge traverse screw position over

the entire range of about 0.28 inches on the suction side of the airfoil.

It was linear for a range of only 0.15 inches on the pressure side where

the calibration was carried on to a distance of 0.21 inches from the air-

foil surface. The constants of proportionality over the linear portions

differed by about 1.8 from one side to the other.

Page 26: :i ., R .. ., O DARY

The probe' s fluid dynamic characteristics were calibrated in

a small wind tunnel in the Gas Turbine Laboratory. Uniform, steady

flows over a velocity head range of .9 to 2.96 inches of water were at-

tainable. The data for total pressure error versus angle of attack

shown in Figure 12 indicates an error of less than one percent over a

range of about sixteen degrees centered approximately on the probe axis.

Scatter in the data indicates approach to the limiting sensitivity of

the instrumentation rather than inconsistant probe performance.

It was intended that the probe should determine angle of attack

by measuring the unbalance of pressure between the two outer tubes, rather

than physically yawing out the probe. This latter method was, of course,

impossible under the circumstances. Although the probe has not, as yet,

been used to determine angles of flow, it has been calibrated to do so

in the same wind tunnel mentioned above. The relationship between angle

of attack and unbalance in pressure was found to be linear over a range

of plus or minus sixteen degrees. The constant of proportionality showed

a more or less random scatter of about one percent over the range of ve-

locity heads mentioned above.

Page 27: :i ., R .. ., O DARY

A-5

APPENDIX II

CHORD INTEGRATING TECHNIQUES

Reference 4 contains an analytical relation for wake momentum

thickness and suction surface diffusion ratio for cascades of the type

used in this investigation. The relation involves a particular chord-

wise integral of a function of shape factor, momentum thickness and free

stream velocity which could not be evaluated directly. The present data

allows a limited look at the validity of the integrating techniques employed

in the approximate evaluation of the above integral.

The momentum equation for two-dimensional incompressible bound-

ary layers (6),

& =u'). +v

where T, = wall shear stress

= density

can be written in the form:

d e - - H+2F

where r

This can be integrated over the chord from x = 0 to x = c, the chord

length. Thus, C

104e = HF .OT -v

where subscript te denotes trailing edge conditions and the equation is

normalized on the chord length.

Page 28: :i ., R .. ., O DARY

A-6

Attention is here devoted to evaluation of the final integral

on the suction surface of the airfoil. The data indicates that we may

assume Umax occurs at the leading edge. Thus the integral might be

evaluated directly as follows:

C tXaZClt1

The present data allows direct graphical evaluation of this

integral, except that assumptions of the values 9 and H at U = Umax must

be made. 9 may be assumed equal to zero, as is actually the case at the

leading edge, or equal to 2 9Rl, the value indicated at U = Umax by the

preceding work. The difference in the integrated result is negligible.

The shape factor at the leading edge was taken as 1.3 as indicated in the

preceding work. Again, the integration will decrease the effect of an

error in this assumption.

Reference 4 makes a first approximation to this integral in

the following manner, again assuming that Umax occurs at x 0.

with the implied definition of (H + 2) (9/c):

C

Page 29: :i ., R .. ., O DARY

A-7

This, of course, is true only if the averaged quantity is actually a

constant. The data shows that it is far from constant.

A second approximation is made as follows:

(H +2 ZX 91r, ( H + 4RXelrc)

where FT. g~.ti .

The above two approximations may also be graphically evaluated

from the present data, and compared to the direct evaluation. The same

assumptions are valid for H and 9 at the leading edge. Uma was found

as in the preceding work. Ute was taken as the free stream velocity at

the 98% chord position.

With these assumptions, the various integrals were evaluated

with the following results:

Run conditions 9 I(eZ j'

2D - 56 o00218 .00189 (-13.6%) .00721 (-66.9%)

2D - 62 .00715 .01137 (+59.0%) .00739 (+3.4% )

2D - 65 .0146 .0272 (+86.3%) .0167 (+14.4%)

3D - 52 .00400 .00311 (-22.2%) .00226 (-43.5%)

3D - 56 .00857 .01063 (+24.0%) .00696 (-18.8%)

3D - 60 .01292 .0373 (+189% ) .0217 (+68.2%)

Thus it is seen that the second approximation, which was the

one used in Reference 4, is by chance the better one in all but the low

angle of attack cases. It is in fair agreement with the direct evaluation

at medium angles of attack and appears better for the two-dimensional flow

cases.

Page 30: :i ., R .. ., O DARY

A-8

The preceding integral approximation is a step in Lieblein' s

analysis and does not appear explicitly in his final correlation. The

above discussion is, therefore, a look at the validity of a part of his

analysis, rather than his final result.

Page 31: :i ., R .. ., O DARY

BIBLIOGRAPHY

1) Davies, P. 0. A. L.,

"The Behaviour of a Pitot Tube in Transverse Shear", Journalof Fluid Mechanics, Vol. 3, Part 5, February 1958, pp. 453-454.

2) Dean, R. C. Jr.,

"Aerodynamic Measurements", Gas Turbine Laboratory, M. I. T.,

1953.

3) Jones, B. A.,

"Method for Prediction of Boundary Layer Separation and Growthfor Application to Turbine-Blade Design", ASME Paper No. 57-F-30.

4) Lieblein, S.

"Analytical Relation for Wake Momentum Th.ickness and DiffusionRatio for Low-Speed Compressor Cascade Blades", NACA TN 4318,

August 1958.

5) Montgomery, S. R.,

"The Design of a Low Speed Cascade Tunnel", Gas Turbine Labora-

tory Report No. 43, M. I. T., January 1958.

6) Schlichting, H.,

"Boundary Layer Theory", Pergamon Press, New York, 1955.

Page 32: :i ., R .. ., O DARY

Tl

TABLE I

Veloci Profiles

y in inches

2D-55-20-S

U/U7

.030

.022

.018

.017

.016

.015

.014

.013

. 012

.012

.011

.010

.009

1.000.996.980.976.969.959.945.931.918.907.892.882.876

2D-55-20-P

. 028

.019

.015

.012

.010

.009

1.000.993.967. 935.896.871

2D-55-40-S

.089

.067

.046

.037

.033

.029

.024

.020

.016

. 012.009

1.000.999.998.994.986.969.942.896.835.748.716

2D-55-40-P

.051 1.000

7

.043

.034

.025

.021

.016*012.010.009

U/U

.998

.998

.992

.972

.936* 831.750.714

2D-55-60-S

.114

.092

.071

.050

.028

.020

.011

.010

.009

1.000.997. 991.974.912.829. 687.667. 636

2D-55-80-S

.146

.125

.103

.082

.060

.039

.030

.022

.018

.013.012.012.010. 009

1.000. 996.984.955.894.815.776.731.704.671.662.654.642.636

2D-55-80-P

.109 1.000

.087 .997

y U/

.066

.055

.044

.035

.026

. 022

.018

.013

.011

.009

.983

.965

.920

.854

.756

.703

.630

.547

.514

.463

2D-55-90-S

.209

.166

.145

.123

.102

.080

.059

.038.021.016. 012.010.009

1.000.998.993.981.961.913.848.764.694.669.633.608.594

2D-55-90-P

.153

.131.109.087.070.061.053.044.035.026.022.018.013

1.000.991.978.950. 917.897.872.847.814.775.756.735.687

y

.009

U/U

.641

2D-55-98-S

.214.172.150.129.107.086.065.043.035.026.018.013.011.009

1.000.996.984.968.934.880.824.740.702.676.635.602.571. 550

2D-55-98-P

.193

.153

.131

.109

.087

.066

.057

.048

.040

.031

.022

.016

.013

.011

.009

1.000. 995.985.972.951.923.909.894.878.860.835.811.795.773.763

2D-62-20-S

.125

.103

.082

1.000.999.994

Page 33: :i ., R .. ., O DARY

T2

Table I continued

y

.060

.039

.030

.022*013.012.009

.972

.912

.873

.818

. 734

.728

. 710

2D-62-20-P

.028

.019

.015

.012

.010

. 009

1.000.992.978.939.920.888

2D-62-40-S

.152

.131

.109

.088

. 066

.045

.028

.019

.015

.011

.009

1.000.994.985.956.900.805.705.643.629. 602.598

2D-62-40-P

.025

.021

.017

.012

.010

.009

1* 000.992.972. 907.858.754

2D-62-60-S

.243

.200

.157

.136

.114.093.071.050.029.020.016

1.000.996.984.964.927.873.796.704.604.557.532

y

.012

.010

.009

U/U

.496

.476

.468

2D-62-80-S

. 309

.296

.253

.210

.167

.125

.082

.060

.039

.022

.018

.013

.010.009

.998

.992

.982

.942

.874

. 779*628.538.467.409.367.366.360.343

2D-62-80-P

.066

.044

.035

.026

.022

.018

.016

. 013

.011

.009

1*000. 970.918.778.690. 560.493.442.375.307

2D-62-90-S

.369

.349* 329.309.311.294.251.208.166.144.123. 101.080.059.037.020.012

1 * 000.994.989.983.978.972. 942.888.803.744.677. 610.535.470.400.366.316

y

.009

u/t

.302

2D-62-90-P

.J08

.086

.068

.060

.042

.033

. 025.020.016.012.009

1.000.988.966.944.891.852.800. 774.741.686.649

2D-62-98-S

.409

.389

.369

.349

.329

.309

.299

.282

.265

.248

.235

.214

.192.171. 149.128.107.085.064.042.025.017.012.011.009

1.000.998.988.979.970.958.954.935.918.896.880.833.795.738.684*636.553.507.435.380.349.315.285.293*251

2D-62-98-P

.153

.131

.109.087.066.057.048

1.000.998.991.974.953.938.920

y

.040

.031

.022

.018

.016

.013

.011

.009

u/U

. 905

.886*859.851.832.817.794.791

2D-65-20-S

.253

.232

.210

.189

.189

.167

.167.146.146.125.125.103. 103.082.082.060.060.043.043.035.035.026.026.022.022.020.020.018.018.015.015.013.013.011.011.009.009

1.000.996.994.985.994. 985.991.974.985. 958.970.936.948.880.892.813. 826.748.761.720.734.675.694.660.675.644.660.637.644.629.637.620.629.604.620. 604.612

2D-65-40-S

.459

.459.998

1.000

U/g

Page 34: :i ., R .. ., O DARY

T3

Table I continued

U/Uy 7 U/U y u/U y u/U

.409

.409.359.359.309.309.300.300.279.279.236.236.193.193.150.150.107.107.086.086.067.067.048.048.039.039.030.030.022.022.018.018.013.013.011.011.009.009

. 997

.999

.995

.997

.991

.996

.984

.990

.978

.984

.974.984.962.974.939.951.879.892.835.848.789.802.743.752.717.725.702.717.671.679.653.646.643.648*632.638.620.625

2D-65-60-S

.609

.509

.459

.409

.359

1.000.992.995.992.997.983.989.977

.309

.294

.273

.230

.187

.144

.101

.080

.059

.042

.033

.024

.020

.016

.014

.012

.010

.009

.986

.958* 974.958* 974.940.958.914.931.878.904.778.820.678* 714.622.649.561.574.497.510.460.475.434.405.414.383.369.383.366.361.346.356.341

2D-65-80-S

1.009.909

.809

.709

.609

.549

.509

1*000.990.996.986.992.980.986.968.978.962.972.943

.459

.409

.359

.309

.297

.233

.190

.147

.104

.083

.062

.045

.036

.027.019.015.012.009

.953

.922

.943

.903

. 922

.860

. 881

.779

.825

.791

.816

.690

.729

.588.618.502.539. 396.421.332.377.288.319.251.274.243.226.207.198.186.176

2D-65-98-S

1.3591*159

.959

. 809

.559

.459

.409

. 359

1.000.996.992.974.985.952.963.862.884.763.814.678720633

.663

.259

.304

.261

.218

.176

.133

.090

.073

.064

056

.048

.039

. 030

.022

.018

.008

.421

.468

.491

. 527

.400.468.344.400.283.311.158.243.205.215.173.195.158.184.130.158.089.145.130.063.114.000.130000

.114

.063

3D-52-20-S

.036

.028

.024

.021

.018

.016

.014

.012

.010

.009

1.000.997.984.982.958.933.903.856.801.791

3D-52-40-S

.061

.044

.036

1.000.998.994

Page 35: :i ., R .. ., O DARY

T4

Table I continued

y

.027

.018

. 014

.012

.010

.009

u/U

.976

.896

.797

.715.653.639

3D- 52-60-S

.107.086.065

.056

.048

.039

.030

.022

.013

.010

.009

1.000. 994.976.980.962.971.941.949.913.923.867.874.790.793.687.634.613.598

3M-52-80-S

.190

.147.125.104.083

.061

.044

.036

.027

.018.014.010.009

1.000.994.985.964.921.928.844.850.772.740.694.654.616.576.560

3D-52-98-S

.277 1.000

y

.255

.234

.191

.148

.127

.105

.084.063.045.037.028.020.015.012.010.009

U/U

.996.996.989.937* 900.843*772.683.624.592.560.494.463.420.410.381

3D-56-20-S

. 092.071.049

.036

. 028

.019

.015

.013

.012

.010

.009

1.000.989.960.967.932.939.910.918.868.875.826.834.804.812.785.789.754.748

3D-56-40-S

.147

.104

.083. 061

.044

. 036

1.000.995.981.940.946.871.879.835.847

y

.027

.018

.014

.011

.009

u/U

.789

.799

.738

.746

.701

.707

.665

.669.641

3D-56-60-S

.257

.236

.193

.150

.129

.107

.086

,065

.056

.048

.039

.030

.022

.013

.011

.009

1.000.998.998.989. 977.978.946.956.899.910.820.831.787.796. 732.753.683.702.660.667.612.623.565.536. 507

3D-56-80-S

.296 1.000

.274 .9921.000

.232 .974.985

.189 .940.956

.146 .860.877

y

.125

.103

.082

.060

.043

. 035

.026

.018

.013

.009

U/U

.790

.808

.714

.753

.627*658.527.580.46e.499.437.468.402.437.365.387.349.357.323

3D-56-98-3

.509 1.000

.409 .982. 996

.369 .971.985

.339 .952.964

.309 .945.933

.300 .910.930

.278 .870.910

.235 .811.841

.193 .697.746

.150 .592.638

.128 .500* 560

.107 .439.486

.086 .396.414

.064 .317.348

Page 36: :i ., R .. ., O DARY

T5

Table I continued

u/Uy y u/U 7 u/U 7 U/U

.047

.039

.030

. 021

.013

.009

.246.246.246.207.170.027

3D-60-20-S

.286

.244

.222-

.201

.179

.158

.137

.116

.094

.072

.051

.038

.030

.025

.023

.021

.019

.017

.015

.012

.010

.009

1.000.997.996996

.996.982.989.975.982. 954.968.910.925.856.872.764.772.727.736.689.698.676. 680.664. 675.658.664.645.652.632*637.615.621.599.606.592.597*588

3D-60-40-S

.409 .998

.319 .994.998

.297 .984.990

.275 .9801.000

.232 .961.980

.190 .955.967

.147 .913.926

.104 .820.832

.083 .750.769

.061 .673.688

.044 .610*624

.036 .559.566

.027 .524.540

.018 .485.489

.014 .449.454

.011 .417.009 .398

3D-60-60-S

. 509

.459

.409

.369

.329

.289

.257

.236

.193

.9931.000

.988

.995

.961

.972

.940

.966

.918

. 946.888.916. 847.874.817.859.756.788

.150

. 129

.107

.086

.065

.048

.039

.030

. 022.013.011.009

.636

.689

.595

.636

.508

.532

.461

.487

.376

.433

.341

.376

.266

. 310

.257

.285.237.226.200.187

3D-60-80-S

1.009.909

.809

.709

.509

*409

. 369

.339

.309

.297

.275

,232

.190

.147

. 125

1.000.986. 992.981. 992.948.964.814.676.730.766.655.611.616.676. 594.634. 526.594.500.571.417.472.303. 383.266.303.182

.104

.083

.061.044.036.027.018.014.010.009

.245

.105

.164

.105

. 164

.071

.071

.071

.071.000.000.000.000

3D-60-98-S

1.109

1.059

.909

.809

. 709

.609

.509

.459

.389

.349

. 309

.299

.278

.235

.192

.149

.107.021.012.009

.9791.000

. 979

.987

.940

.966

.882

.896

.821

.867

.738

.805

.623

.702

.558

.623

.426

.534

. 359

.426

.323

.359

.278

.323

.228

.323

.160

.278

.000

.167

.000

.123.071

000.000.000

Page 37: :i ., R .. ., O DARY

T6

TABLE II

Free Stream Dynamic Pressures

Cascade angle

2D-552D-622D-653D-523D-563D-60

p0 - p.(inches of water)

2*973.0020992.5020552.69

Page 38: :i ., R .. ., O DARY

90I I

+ All Data for Suction Side

80 -x - 2D-55 Cascade AngleA- 2D-62 0

+ - 2D-65 0

*- 3D-520

70 0 - 3D-56*- 3D-600

60-

50-

40 -Umax

0 2ORL U~

30

20V

10- 0

0.4 0.5 0.6 0.7 0.8 0.9 1.0UUmax

MOMENTUM THICKNESS CORRELATION

FIG. I

I i

Page 39: :i ., R .. ., O DARY

90I

80 Symbols as for Fig I

70

060

V

50

+[ U m a x ] 5

40 U __

30

.20

10

0 I I 9 - + -0.4 0.5 0.6 0.7 0.8 0.9 1.0

UUmax.

DISPLACEMENT THICKNESS CORRELATION

FIG. 2

Page 40: :i ., R .. ., O DARY

4.0 1 1

V Symbols as for Fig.

3.0-

20- 0

1.0- H 1.305

If U /UMa x

0.4 0.5 0.6 0.7 0.8 0.9 1.0UU max

SHAPE FACTOR CORRELATION

FIG. 3

Page 41: :i ., R .. ., O DARY

.02 / .102D-55'- Pressure0

.01 0. 5

0 1

.01 .05;:::9

0 .0

.03 .15

2D-62 0 -Pressure 1

.01-

.10 c ~50

.08 2D -62 0- Su ction .40

.06

.02 .20

0+=0

0 1 2 3 4 5x 0 FIG. 4

Page 42: :i ., R .. ., O DARY

-. o

00, - 1.0

+ -- 0.8

2D-65*- Suction0.3 -- * 068 / 0.6

0.2 -- g.4 o

0.1 0 0 0.2

0 - -- 0

.04 -- .20

.03 3D-52- Suction .15Ole08 le 0.O 0 2 -0 . 10

.01 - .05

0 0

.20 0.48/

.15 3D-56*- Suction 0.3

.0 -00 -- 0.2

.05 -- a - 0 00 0 0.1

0.5 - 1.0

0.4 3D -60*- Suction - 0.8

0.3 0 0.6 O

0.2 7 -- 0.4

0.1 -woo0.2

0 00 1 2 3 4 5

x No FIG. 5

Page 43: :i ., R .. ., O DARY

1.0

0.81

y

0.4{

0.21

0

0. 61-

0.4-

0.2-

1.0

FIG. 6

00

S 2D -55 0 - Suction* 40 % Chord

- 98%

-/000e

0000,000/0

1.0

0.8

0

y8

IIiil1 III-

2D-55*- Pressure940%098%

000000/'

I I 144-

0 0.2 0.4 0.6UU

0.8

0. 6

Page 44: :i ., R .. ., O DARY

0.41

0.21

0

1.0

0.8

0.6 1-

0.41 -

0.2HF-

0 1.0

FIG. 7

1.0

0.8

0.61

y8

2D -62 0 - Suction

* 40 % Chord- 98 %

-7/- -

---

y8

2D-62* -Pressure* 40 %o 98 %

/-00I00"

0.2 0.4 0.6UU

0.8

I

Page 45: :i ., R .. ., O DARY

0.2

0

1.0

0.8

0.6

y

0.4

0.2

0 1.0

FIG. 8

1.0

0.8

0

0.61

y

0.41

2D -65*- Suc t ion* 40 % Chord* 98%

F-r

- --

3D-52 0 - Suction7 ~ .40%

0 980/%

0'0

0.2 0.4 0.6uU

0.8

Page 46: :i ., R .. ., O DARY

0

1.0

0.8

0.61ya

0.41

0.2

0

0.8

0.61

y8

0.4

0.2j

0 1.0

FIG. 9

3D -56 0 -Suction* 40 % Chordo 98 %

0000

1-

-

3D-60* -Suction

* 40 % Chordo 98 %

- -E

-- 9

L_-

0.2 0.4 0.6uU

0.8

.

Page 47: :i ., R .. ., O DARY

1.0

600

I I-

10 2 0 '' 60

--; 0 0 00 do0 5 2 * C a56*

Three CSta ticDistribu

Suction

70 80 90 100 % Chord

scade

Pressuretion

Side only

0.8

0.6

0.4

0.2

0

-0.2

-0.4

-0.6

-0.8

-1.0

-1.2

a 8 a8

0

-

\ N 62*

10 20 30 40 '60 70 80 90 100

5*Two DimensionalStatic Pressure

62 Distri bu tion

+ (650 Cascade Angle

% Chord

0.4 r-

0-. Q8CL a8

0.2,

0

-0.2

-0.4

-0.6

-0.8

-1.0

1.2

1.4

1.6

A ngle

FIG. 10

Page 48: :i ., R .. ., O DARY

Pressure

Main ProbSupport

Wedge Blo

Wedge Co

Probe Tip

Leads-

vvedge TraverseScrew

eWedge

ck

ntact Pin

C

8 Horizon

Probe Hanger

Probe Tip Lock

,,0 FOW

- Cross Support

HorizontalSlide Lock

Slide

FIG. 11 BOUNDARY LAYER TRAVERSE

( PO - Ps)PI--(Po Ps)0

0

8

0

.06

.05

.04-

.03 -

0

0

o o08 0 .02-- 0

-16 -12 -8 -4-2 0 2 4 8 12 16a-Angle Of Incidence

FIG. 12 TOTAL PRESSURE ERROR

PROBE

tal

Page 49: :i ., R .. ., O DARY

Fig. 13

Fig. 14

Page 50: :i ., R .. ., O DARY

Fig. 15

P. E

$055 SUCTION

UL C OP PROPE

71P POsIT)0ct

30- 62-SUCTION

Fig. 16