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(1)

.5 Dimental Analysis and similan.ly

I Planning , pantatm.mterpetatmofexplCFD.ua

9, µ

ㅇ缸

F. F - f ( t.V.9.pe )

FI_i.fi#' at

Least 10 datap.im

stt0 "

(God V. 9. µ) (E points for b each L. V.

f.M.BAA wereda are Nation to

唜一 이땄

)

弑潞

OE
(2)

Edimeansmod

analysis ,

%faae-stoexpsaiy.l.EE

RefRm.ae = RMtotype G mode = G.pro

totpe.no/rmfelllf.Er5.2.Pmcrpleofdmensmalhomogenei

ty .

in te same of , each adaHe term should

have are same dina위다.

( ftftv.ttgo.tlIst[ ㄴ] Cha Falling)

(3)

1 ¥ .it gz = constant (Bernardi q)

/ ' iii] S

dimental variable : S. V. t.pe z . .

( a constant : So , , g, . . .

- Pure constants

nodimensia.eguatiin_dmsiadeeseguiuo.intanalysis

non_dimental form

5.3 .

[email protected]ion in variable

( n : diMenand variable

( k : " loss variable ( TI )

(4)

reaction

j = n - k < number of

dimensrousnecessangtodescribed.imemotional variable

atitaf.E.TL?reductrmj=5-

=f

a' cnv.em.net 3 k 32 .

G. . g ( Re ).fr?T=G.Tz=Re

Find The reaction

Ni = fwz.rs. .V5 ) 7=5

if 3 diMasters [ M.LT arevequired.kz?

T.wsask.US. .me i]

gdimen.si예의s

(5)

E = www.iwaf V5 = LM0T 1

I

form Pi Group by Power Product of

these variable that to not form a Pi

(mi mi Nd = cnet.my 세대

receptor

a= b =C = 0

diMensuit analysis oilI tail .

:

F

:

=

:

f

:

( L . v

:

. 9

:

)

:

T-T

:

:

-choosedensity.ve/ocityadIengjodonotputturodependentvariable as

(6)

reaction variable

.

ex) E = ftp.L.U.ru ). N- 5 .

F = [ MLFT

/

.LT 5k£ 3

L - ]

8.32.0 4 kt 2.

V2 CLI'

t.fi[ ME3] j variableS .

µ .fm 幽巧 L

. V . 9 .

( ftp.CNET?a.b.C? )

T.tt CE = (LIKE 'J M I[ MLE

= [ int53

f"? M

= [ TN

a-2.be -2, C = - 1 .

(7)

i. T-T V29" F =

唜泄

G)

石一一 ftp.fmiija#=C-l_ee.

石二唜 一恨

. ( ' - '

佑二

Re )

LG.ge?nedspractiee!fmi3S=fcPcL.E

.IT ""

豺 .it?.E.&SttnyfMLiI

iii]

( j - 5 - k£3 . E32 .

(8)

Can'tb And to groupS , because P and

E contan M and F but also same Power

of Mad T . E230

T.ME" S

(

퍄샤탸

P E. = 8

恁悠

_ . )

形二

池邨工

Gene!) Q #.mn#CMeLcTR.

. 4 - £ 3

EarlI Group : T.it#dQ=CM F]

(9)

Q = AV d,

퍄 公器八

= constant = c

r T

M = HR

惚心

GQ.ci .it (

邨仙

) .

- 9 Q .

9 9

54 alon-dimeoodizatmofthebasiceqwtms.in

inwmpressibkflowi.wntmity.FI = 0

( - its equation : 9

慶一加

tre

a material denrate

ISNon - dimensimdizo.tn i.

characteristietalesneededl.LIU )

,

(10)

5. 4. Non- domensrnalizatoan 0f thebasiiegn

mnompresibleftoror

ontonuity : OOA- = 0

* mtm : aptuO9 -matewalOO- derivative

o*

we need charaoterstr scale .

b velocity , length,

A ( ω ) CL )

e - q ) =

*

= -

, YA=

,

E

*

= E ,

A

= P

t * = =

. P 9 ω
(11)

- ( 2-=2α((vuLx* ) = = 1. 보한*

9 - ( = -D9D((t*UI

*) ) =9

A

I

MoOP=== MoEA* ( p**(e

어스

) = - ) 0=

( JXPd*

짜서르서

)

**

* =

-[90중식 * tM*

르으

* [ UA

* = -*p *

+ LO**

. P =

앓 홉

1

(12)

d = -Mertia

Nscousforc

2

*+ (

:O *)L *= - Oxp* * + ke* 8A

로서

ADomenstonal Parameters

. Re = ~9( Reynoldsmomker))

. Fr = CFroude number) ~ shipriver, sea

We= - f(Webernumber)- interfacialflowr

liqurd droplet .

- surface fenson

Maz ( Machnumber)

(13)

st= - ( strmhalnumherx

frequency

O O

요 법

, sensor O

L Kanman vortex shedding

나스 W . coscft )

.

= uA = ws ( ft

대는

)

= cos ( st. t* ) ,

(14)

- pr =

uc ( Prandtl namber) [ FU -A

thermalconductivity g = - k -

=

불며

0) G = -ieurAOndrag,

1 Lift ( (항력 ) .

lift (양력) drag coeffrcieut

wefftcient

- O~

8w C " §

P = P

- P

e

( pressure oefficiewA))

(15)

5.5 . Mo .delingandSimplantyy ( 상사성)

ππ= f(π iπ 3 )

5π 2m= π p, π 3m zp, ⇒π im = πiP ,

* GeometreEimilavity [ L ]

a mmodel and Protofype ane gmetically similan

ifand onlyif all body dimensins in all three

coordinateshaethesamelMear -sealerato :

> all angles are presened, all flow directronsane

preservedd

co~ -00EX

(16)

* Kinemafic 9imflarty [ L . T ]

themofionsofftwo systems ane Simiplar

model ndfprofotype hal tle same

C

length- and fime - scale

ratocC

-+AP (속도)

AM

1 CM

~Hp

Perod: Tp

~4m Tm m

Froude number , 2

Fvm =

했다

=

-. -5

(17)

Dt : vm = VD Vm = rav

Tm = raTr

y [ TJm, .

namme* similaity

- Same lenyth - , fime - , and mass (force)

-scale rattos,

P

> m

; Am, 9 m O

. 9p "

m

Renp OL'=-fpvoplup,Rem =-µn/m

[ f dm = adp, same fluid, m =

AP
(18)

Realflows ~> lab tests . CCED , EXP)

*

nwmpressibe flow . Re

( compressibe flow : Re & Mas

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