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BXPERDBlf'!S ON NONEQUILIBRItlM, NONSTAXIONARY EXPANSION OF W~ VAPOUR/CAImIER GAS MIXTURE IN A SHOCK TUBE

~

S

SEP. Ja

..

VL1~_ 7L . . ~ _ .. ' v.,!..-L; B~c 0 NEE Kluyverweg 1 - DELFT . Apr1l,

1975

by

s.

P. Kalra

urIAS Report No. 195

(2)

l

EXPERIMENTS ON NONEQUILIBRIUM, NONSTATIONARY EXPANSION

OF WATER VAPOUR/CARRIER GAS MIXTURE IN A SHOCK TUBE

by

S. P. Kalra

Submitted April, 1975

(3)

Acknowledgement

I wish to express my sincere thanks to Dr. I. I. Glass f'or the

continued interest and encouragement throughQut the course of this stu.o.y.

The author ~ppreciates and wishes to thank Dr. J. H. deLeeuw,

Di;rector of the Institute f'or his comments on the manuscript and f'or the

opportunity to stuèl,y at UTIAS •

Tlle ~vice and contributions through many enlightening discussions

with J. P. Sislian are gratefully (l,cknowledged wi th thanks.

, My thanks are also extended to Mr. P. Crouse for his assistance

in fabricating th~ condensation shock tube facility, and to Mrs. Winifred

Dillon for 'typing the manus cript •

This research was supported by the Atomic Energy of Canada Ltd. (ABCL), Cha.1lt River, under AEeL Research Contract and by the U.S. Air Force

Office of Scientific Res~arch, under grant No. AFOSR

72-2274.

Their support

(4)

Abstract

The investigation of condensation process in a nonstationary nonequilibrium expansion of water vapour/carrier gas (ultra pure Nz)

mixture is presented, here. The density variations, pressure variations and onset of condensation due to such expansion, are monitored at two fixed locations in the driver section of the shock tube by using a laser Fabry-Perot interferometer, a differential interferometer and piezotrons transducer devices. The effect of the cooling rate on the supersaturation at onset of condensation and its delay time (nonequilibrium zone) is

determined. An empirical relation is derived between the supercooling and the rate of cooling at onset of condensation. A theoretical analysis is performed using this empirical relation in order to determine the location

of the onset of condensation in such expansions. It is shown that t1:le location of the onset is uniquely determ;i.ned for a given initial driver condition, e.g., (i) relative humidity, ~4, (ii) vapour mass fraction W4, and (iii) temperature T4. A parametric study, using these

3

parameters is also given. The experiment al findings are in agreement with the theoretical prediction of onset.

(5)

TABLE OF CONl'ENl'S ,

Page

Acknow1edgement 11

Abstract 111

<I Tab1e of Contents iv

Symbo1s v

1. INl'RODUCTION 1

2. BASIC PHYSICS OF CONDENSATION PROCESS 2

2.1 Kip.e,t1cs 2

2.2 Gas Dynamics

4

3. EXPERIMENTAL APPROACH 7

3.1 Condensation Shock Tube 7

3.2 D1agnost1c Techniques

8

3.3 Exper1mmtal J;tesults 9

4.

ANALYSIS 11

5.

DISCUSSION OF THE RESULTS 13

REFERENCES

15

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4 a c C G I k L M n N P R S t ' T u

u

v x y p

o

lJ ' w sound speed concentration cQnstant(s) free energy nucleation rate Boltzmann constant latent heat Mach number SYMBOLS

number of molecule~ per ,cluster

characteristics line slope pressure gas constant supersaturaticn time, 'temperature particle velocity

condensation front velocity specific volume

axial coordinates specific heat ratio density

surface tension molecular weight specific humidity

(7)

eXpGnent .

. [ T ,-T

J

cohdensation delay A:; ;s c

AG i'ree -:energy change .

AT

supercoolin~.[

AT =.

(Ts-Tc~

Subscripts and Superscripts

i

c .0 cond~n8a1;ien state

--8 s atura1; ion· state

v vapour.statê

. 1 ini ti8.1 state in the low pressure sectien (channel) of the

shock. tube

4· ini tial state in t~e high ·pressure section (chamber) of the

shock. tube

4,1 ratio-of the specified property between chamber and channel

P4 (Le., P41 :; p~ )

. 1

(8)

---~

1. INTRODUCTION

In science and technology we find many problems of interest dealing with the condensation process from its supersatur'ated, state viz,

(i) the formation of aerosols, (ii) the application of the cloud chamber technology to nuclear and high energy physics, (iii) the èxpansion of

steam in turbine nozzles, (iv) the expansion of vapour into high 'V'acuum when spacecraf't are vented, (v) the expansion of condensable vapour in propulsion devices, (vi) supersonic and hypersonic wind tunnel d~signs,

(vii) two-phase-:flows associated with water-cooled nuclear-power-.reàctor design and many others. Although condensation of vapour ocçurring from the supersaturation state instead of from its e'1uilibrium saturated' statee

has been observed for almost three-'1uarters of a century (Refs ~ 1 and 2), recently renewed efforts are being made to provide '1uantitative predictions of condensation rates, associated relaxation times and to perform reliable experiments, e.g., Hill (Ref. 3), Deych (Ref. 4), Barschdroff et àl (Ref.

5).

Condensation of vapours may be initiated by either a heteroge-neous nucleation or a homogeheteroge-neous nucleation mechanism. In the former case, the condensation of vapour takes place on foreign nuclei which act as centres for condensation. Their presence leads tocondensation near e'1uilibrium. Homogeneous nucleation results in theabsence of foreign nuclei or in fast transient processes where condensation ac cumul at ion on foreign bodies remains negligibly smalle In this case random collisions may lead to the agglomeration of small numbers of vapour,molecules forming clusters. The theory of homogeneous nucleation initiated by Volmer and Weber (Ref. 6) which predicts the rate of formation of clusters of critical

size, a size that permits unlimited growth of the cluster. These clusters

are-

formed at a high supersaturated state. The condensation due to

homo-geneous nucleation may become much delayed with respect to the e'1uilibrium s'tate. In the present; investigation, the mechanism of homogeneous nuclea-tion results in a phase change process in a highly supersaturated state.

Various techni'1ues have been used in the past to study both the kinetics and the gas dynamics of condensation reaction in gaseous vapours. From among these, the Wilson t s cloud chamber and nozzle expansion, have been used extensively. Oriani and'Sund'1uist (Ref. 7) have discussed. cloud chamber m~asurements where Wegener and Mach (Ref. 8) gave a comprehensive review of condensatiQn in nozzle flows.

Recently, shock tube techni'1ues have been applied for (condensation studies owing to its advantages of providing a wide spectrum of cooling rates for a given experiment al run, al'though Wegener and Lund'1uist (Ref. 9) initiated condensation studies using this techni'1ue; it has been used since then by Glass, Patterson (Ref. 10), Homer (Ref. 11), Kung and Bauer (Ref. 12), Kawada and Mori (Ref. '13) in' various forms. We are also reporting here an experimental shock tube investigation of water vapour condensation procèss. The emphasis is on the effect of rate of cooling on "various parameters of interest viz condensation rates, condensation delay time*, *Condensation delay time is 'd..efined as the delay in onset of condensation

measured from the time of its e'1uilibrium saturation state to the time of condensation (i.e.,tc-t s )

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onset of condensation and corresponding supersaturation, etc. The

experi-mental results are analyzed "to give an empirical relation between rate of

cooling and.condensation delay* (from equilibrium temperature Ts ), i.e.,

(~ = (T s - Tc)/Ts). 'AI! important contribution from this study is the

coupling of the above experimental results with a theoretical analysis,

predicting the onset of,condensation, condensation front velocity, and its

local Mach number at any location in the rarefaction fan 0 f the shock tube

for" a given initial condition in the expansion chamber (driver) of~he

shock" tubes _ The ,initial condi tions are comple tely defined by specifying

initial relative humidity, CP4, vapour mass fraction W4 and temperature T4.

The parametric study ,showing ~the effect of initial param:!ters on the onset

of c"onden:;;ation path in an x-t diagram has also been performed. Ultra-pure

NE wa.s used as a carrier gas in the presen t experiments •

2.

""BASIC PHYSICS OF CONDENSA'rION PROCESS

2.1 Kinetics

When .a vapour is expanded adiabatically its vapour pressure

decre"ases ,as" 'temperature .falls. Generally the vapour pressure falls fastElr than" " its p~essureanq, therefore we expectthe pressure temperature path of

a'flów p~ticle (i.e., isentrope) will intersect an equilibrium saturation

iinEl,as shown in a P-T plot in Figure 1. If phase change occurs in

thermo-dynamic equilibrium, it should follow a saturation line instead of the

isèntrope. " This may happen if the system undergoes a slow change of state

" Grif "f'oreign" nu..clei" al:'e present in sufficient numbers to act as

condensa-"tion centres. " However, in practice adiabatic expansions are generally fast

processes and

8.n

isentrope extends into the supersaturated state, until

s:ponta.ileous condensation by homogeneous nucleation takes place. The

conden-sate "centres formed in the supersaturated state are a result of fluctuations

in the vapoUr itself. Some of them grow into critical size clusters and these may grow further. At this point their further growth depends upon various physical processes, i.e., thermal accumulation, mass ac cumul at ion , heat conduction into the surrounding vapour and diffusion and related processes. Eventually, agglomeration into larger clusters occurs and

thermodynamic equilibrium is established and isentropes approach saturation lines.

In analogy with the "Boltzmann factor" for equilibrium distribu-tions, Volmar and Weber wrote the fOllowing expression for the concentration of critical clusters:

C*

=

C exp (-à}*

/léf )

(1)

where C is the concentration of monorners inthe system and ~ G* is the wo;rk

associated with the forrnation of critical cl,usters.

The classical nucleation rate equation per unit volume per unit

time can therefore be wri tten as (Ref. 6):

*Please note that the condensation delay is defined here in terms of the equilibrium saturation temperature (T s ) and the onset of condensation temperature (Tc).

(10)

,

I

=

K exp (-t:G*/kr) (2)

where K is

a.

factor and its magnitude depends upon the particular

approxi-mation .use_d in deriving the rate equation. The quant i ty t:G*, which is

es~entially a free energy of formation of a critical size nucleus, contains

the effects of: (a)the free energy change of the vapour molecule in

reducing their pressure from p to flat film value Ps, (b) the change in

free energy due to transition from vapour to liquid film, ,and (c). the

surf~ce free energy for the creation of liquid clusters. On combining

tb,es~ contributions to t:G*, it is noted that it has astrong dependence oil surface tension and is also a function of supersaturation ratio S,

temperature T, and molecular volume V C.

The condition for thermodynamic equilibrium is

which is at the maximum of the functio'n t:G (t:G = t:G*). Here n is the

number of molecules per cluster. This equilibrium condition is unusual

as it is associated with the maximum of !::IJ. Therefore it is an unstable

equilibrium, generally known as a metastable state. In analogy wi th

other reactions (e.g., dissociation)

a.n

energy barrier exists and it must

be overcome before further growth becomes possible.

Using Volmer's approach, Wegener (Ref. 14) has expressed

nucleation rate, I, in

e.G.s.

units

1

1 = 5.4 x 10

19

(~)2

(

~)2

exp [-17.6

(~)3 (~c)2 Ln~S l

~'

(4)

We may use Equation (4) to es timate nucleation rates for v~ious

super-saturation values. Wegener (Ref. 14) computed for 'the particular case of

water vapour and results are shown in Fig. 2. As is obvious, fromthese

estimates shown in Fig. 2, the nucleation rate increases by several orders

of magnitude for s:ma.ll change in the supersaturationS. Therefore once appreciable supersa,turation is reached, the condensation will be effec-tively instantaneous. This physical situation we technically calt the onset of condensation.

In a.n expansion cooling process, we define theoretically the

onset point as a point of maximum supersaturation. In nozzle and shock

tube experiments , the corresponding expansion flows do not depart appreciahly from the isentropic flow until the onset is reached. So a slllB.ll deviation

(arbitrary value, say, 1%) from the isen trope will loc ate the onset point.

Although in presenting the analysis of the experimental results , we need not take into account the above described kinetics explicitly; its

consideration helps in understanding the condensation process and for an

initial estimation of the onset point for various S values wi thin the

constraints of the developed expansion fan. Representative values cal-culated by various workers are given in the table below (see Ref. 14):

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TABLE

C0!!IPuted_and Observed Critical 8upersaturation in Water Vapour for J 1

cm-~ sec ~ at T

= 261

0

K

Reference 8 = pip

s Theory

Becker and Doring

(1935)

5.28

Volmer

(1939),

Frenkel

(1946)

5.10

8ander and DariJkomcer

(1943)

4.44

Barnard

(1953)

4.72

Yang

(1963)

4.48

Experiment 8

Volmer and Flood

(1943)

5.03

8ander and Damkohler

4.39

Madonna et al

(1961)

4.22

The en:q:>irical results derived in this report from our shock tube experiments implicitly take into account the kinetics of the process and may be obtained by joining the basic kinetics with the fundamental conservation equation of gasdyn?JDics, equation of s'tate and the ra:te equations. A rigorous theore-tical approach on these lines has been adopted by one of the members of our group

(J.

P. 8islian) whose work will be reported in a separate UTIA8 report and as a Ph.D. thesis of 'this University.

2.2

Gas Dynamics

The rarefaction waves are produced in the driver section of the shock. tube due to expansion of gas into a low pressure channe1. Any fluid partiële in the rarefac'tion zone experiences a cooling effect whose rate

C:depends upon the location from the origin (i. e., di aphragm) • Due to the cooling eff'ect, the sa:üUra'tion ratio of vapour (8

=

pips) increases with

, time (initially vapour is unsaturated). In this nonstationary expansion

.,fan, homogeneous nucleation induces the phase change mechanism andtherefore it does not ,take place at equilibrium saturation ratio 8 = 1. The vapour becomes supersaturated and enters into nonequilibrium state. The nucleation rate also increases with increasing supersaturation 8, until it achieves its critical peak value. At this point onset takes place and both the super-.saturation, 8, and nucleation rate drop very rapidly. The condensation

reaction adds heat intothe flow field thus an increase in pressure and

te~erature a~ the onset point occurs. Until this point in x-t plane, the

flow is assumed as an isentropic flow. This is a fair assumption, especially

for low mas s fractions of water vapour in a mixture.

The shock tube flow is treated as a .one-dim.ensional, nonstationary , flow and is illustrated on an x- t diagram for three different cases in

Fig.

3:

(i) frozen flow; no phase change occurs, (ii) equilibrium flow;

(12)

- - - -- - - -- - - - --- --- - --

-.

.

(iii) nonequilibrium flow; phase change occurs in the supersaturation state. The condensation front is shown in the rarefactlon fan by a thick line. We rnay note that the heat addition due to the condensation reaction tends to

curve' the straight characteristics lines such that their slope changes in

the direction of increasing pressure. This is because of the compression effect caused by the additional heat of the condensation reaction. Also it results in an increase in the shock wave strength as shown qualitatively

in Fig •. 3. The, cases of frozen flow and the equilibrium flow are the two

limiting cases •

The x-t diagram presented here in Fig. 3 is an ideal case of an

instant burst of a diaphragm, In reality there is always a finite opening

time for a diaphragm. The appropriate corrections applicable to shock tube

flows for the fini te operrl,.ng time of a diaphragm are discussed by Hall et al

(Ref. 17) and can easily be applied.

If we assume that the diaphragm is removed instantaneously, the rarefaction head will move at the sound speed corresponding to the initial

state of 'the water vapour-gas mixture in the high pressure chamber. The

position of the tail depends on the initial state and the pressure ratio between driver and driven sections. For such an ideal, isentropic expansion, the pressure ratio, density ratio and temperature ratio in the rarefaction

fan are given by (Ref.

18):

274 P = [1 _ 74- 1 (

~

+ 1)

J

74-1

.

-

P4r 74+1 a4t

.e....

~ (~4

t

r4

(5) P4 74-1 T =

(~4)

74 T4

where 74 is the specific heat ratio for the gas (or mixture) in the driver sect~on.

The equilibrium vapour pressure is given by the Clausius Clapeyron equation: dP s dT _ L(Tl ~

(V

-v

)T

v c

For a thermally perfect gas we have

PV = (R/IJ.)T

(13)

Since Vv ~>

v

c (i .,e., specific volume of vapour

»

specific volume of condensates) and assuming latent heat 'L' independent of temperature T, Eqs. 6 and 7 yield

.en ps

= -

~

+ const. (8)

By fitting the data on vapour pressure from standard haudbooks Wegener (Ref. 14) defined the vapour pressure as follows:

(

-~+B)

P = 10 T (9) s where A

=

2263; B

=

6.064 for 273°K

<

T

<

395°K; liquid and A :;:; 2676; B = '7.582 for l75,oK

<

T

<

273°K; solid

By knowing the pressure time history at a given iocation in the driver section of the ,shock tube and for a known value of 74, we eau caJ.culate the corresponding density and,temperature histories at the locations by usihg Eq. 5. The tamperature aud pressure profiles , so determined, can now be used -to evalua'te the supersatur'ation, S, hiiltory with the help of Eq. 9 a~ the corr~sponding ~ocation.

We de fine the temperature, 'i's é;l.'t which the ,vapour is saturated and the temperature , Tc at which the' onset of condensation occurs. Both these temperatures eau be dete'rmined from known (experimental) pressure/ density profiles • The dimensionlè$s quality, b.:

T -T b.=~

T

s

(10) is termed the 'condensation delay' because of the fact that there will always be a delay for the Dnset of condensation unless condensation occurs at equilibrium saturation (Le., Ts

=

Tc, therefore b.

=

0; no delay). At a finite rate of expansion, condensation sets in the supersaturation state (Tc < Ts ) so that fj. is a positive fraction. From the physics of the process we know that the supersaturation will increase in magnitude for higher rates

of cooling. Therefore it is areasonabIe hypothesis that the condensation delay, b. is a monotonically inçreasing function of rate of cooling ,

~ ~~)

(Ref. 19). Therefore '

c

(_

dT

)E

dt

(14)

We can determine the constant C and exponent E from experimental

fitting of the data. Since we can also de fine /:::,. and

~~

from the shock tube flow equations in tpe rarefaction fan as functions of x and t, which leads, . to an equation of motion for the propagation of the. 'onset of condensation front' in an x-t p;Lane. More details for the formulation of above equation are given later in this report in a section for the "Analysis of Experimental Results".

3 • EXPERIMENTAL APPROACH

Extensive experimental research has been done on condensation effects in steady expansions whichincludes the cloud chamber work of Wilson (Ref. 1), Powell (Ref. 20), Pound e·t al (Ref. 21) and Allen and Kassner (Ref. 22); nozzle expansions by Stodola (Ref. 2), Oswatitsch (Ref. 23), Stein ~d Wegener (Ref. 24), Dawanson, Wilson, Hill and Russel (Ref. 25), and Kurshakov, Talmanov and Tkalenko (Ref. 26). Their investiga tions were primarily directed towards conde;nsation kinetics.

Worthy of detailed study are the explosive expansion of steam/water vapour in water-cooled nuclear power reactors resulting from an accidental break in a large pipe (similar to the one-dimensional blast situation) and the blast arising from sudden fuel rod excursions (similar to a spherical explosion) • Very li ttle theoretical and experimental work has been done to date on these types of nonstationary flow problems. Wegener and Lundquist

(Ref. 9) did some light-scattering experiments to cbserve the condensed phase bebind a contact surface in a shock tube. Recently, Kawada and Mori

(Ref. 13) investigated the condensation kinetics of refrigerant vapours using a shock tube.

3.1 Condensation Shock Tube

A shock tube facility was built in order to investigate nonstationary, nonequilibrium two-phase flows. The shock tube is made of square stainless-steel tubing (l".x 1" cross-section). The test section is approximately 10" long and 1" wide and has high optical quality glass windows coated with a nonreflecting coating for He-Ne laser light at a wavelength of

6328R.

Two techniques are used to inject water vapour into the system: (i) af ter

evacuating the system to a desired degree, water is injected into a vertical Pyrex glass cup which can also be heated externally, the water surface·thus exposed' to the vacuum evaporates and the vapour pressure starts rising in the system. When a desired vapour pressure is reached, a valve which isolates both 'systems i,s closed. At this point a carrier gas ('i,iltra pure, nitrogen/air)

is mixed with water vapour to obtain the desired pressure in the driver section of the shock tube; (ii) the alternative is to bubble the carrier gas through ultra-pure water until the desired relative humidity is obtained in the system. A separate regulator is provided for inserting the carrier gas if more pressure is desired ,in the driver section. The high-pressure (driver) and low-pressure

(driven) sections are separated by a cellpphane diaphragm.

A good vacuum is achieved using a diffusion pump befare each experi-mental run in order to have a high degree of purity for a te:ct mixture. A.

schematic diagram and a photograph of the facili ty are shown in Figs.

4

and

5,

respectively.

(15)

3.2 Diagnostic Techniques

Measurements are performed at two ,locations in section of the shock tube. The parameters monitored are gradient, pressure and onset of condensation. Two laser and two piezotron-transducers are used for this purpose. tion of these techniques is outlined below.

the driver

density, density interferometers

A brief

descrip-An external Fabry-Perot (F-P) cavity is formed using two .9ptical

semi-transparent flats (flatness ~ À/50). Two first-surface mirrors fold

the laser beam within the cavity such toot the optical length of the cavity is an integer multiple ofthe laser cavity. This helps to reducethe effect of transverse-mode interference. FOlding of the beam wi thin the cavi ty also increases the sensitivity for measurements by threefold as the beam will make three passes through the test section instead of one. A schematic of the F-P arrangement is shown in Fig. 6a and a photograph in Fig. 6b;,

The transmitted intensity IT of the laser light through the erlernal F-P cavity is a function of the losses within the cavity and can be expressed as follows:

~ =_~l-.._

Io l+F

sin2(~)

.

(12)

where :(;0 is the input intensity of the laser radiation and F is defined by

F

=

and is determined by losses within the cavity as defined by the effective reflectivity, Ref, of the cavity. The value of F is constant for a given

Fabry-Pero"t cavity • Normalizing the above, one can wri te (Kalra, Ref. 27)

I s 5 cos 2('2) =

---....,.

·

---,.5,...

l+F sin2('2)

(14)

The value of Is varies from 1 to 0 as 5 varies from 0 to .". (corresponding

to half a fringe shift). The intensity Ïs is modulated wi th time in

accordance with the phase 5, which changes linearly with density, such that:

5(t)

=

6.".

~

pet)

(15)

where K is the Gladstone-Dale constant, L is the width of the tes t section, À is the He-Ne laser wavelength (6328R) and pet) is the density at each instant of time. Therefore, measurements of the modulation of intensity within the F-P cavity can be used to determine the density profiles through

a rarefaction wave. These intensity modulations are measured by a photo-multiplier "tube (EMI 9558B).

(16)

To align and calibrate the Fabry-Perot cavity, one of the flat plates of the cavity is rigidly attached with a piezoe1ec'tric crystal tube. An oscillating electrical signal is applied tothe crystal which induces translational motion to the flat, thus introducing a path change within the cavity. This path change (or phase change) modulates the

output intensity. These modulations are observable only if goed alignment is achieved. This piezoelectric crystal oscillator also serves the

purpose of calibrating for fractional fringe reasurement (Kalra, Ref. 27). Figure 7 shows an output from the oscillator (upper beam) and the roodulated intensity (lower beam). The calibration curve and reflectivity effects are shown in Fig. 8a, 8b. App1ication of this technique for density measurene nts in strong shock waves in helium has been established by Kalra (Ref. 28).

A differential interferometer is designed by splitting the laser beam into two c1osely-spaced parçl.llel beams (separation ::: 0.1 cm) and then recombining them with another similar spli tter. This system is similar to the Mach-Zehnder interferometer system and registers the density change occurring within 1 mm distance and also a sharp gradient in densi ty •.

Figure

9

gives the schema:tic of the differential interferometer.

In addition to the measurements of density and density gradients, these optical devices give very accurate records of-the onset of condensation

(spatial resolution ~ 50 nsec, Le., limits of the recording device). Two low-pressure piezotron transducers (Kistler Model 206) are used at the same two locations to monitor pressure profiles. These special transducers have very high sensitivitd::es (~0.5 mm Hg/mV) and frequency response (rise time ~ 3 I-lsec) but with very low output iIr!Pedances. There-fore, piezotron couplers (Model 504D) are used to convert the low output iIr!Pedances into high-output iIr!Pedances for recording purposes.

The opening time af a diaphragm is als 0 moni tored optically by

having the laser light fall on a photo diode as soon as the diaphragm bursts. The photodiode is hooked to a device which triggers the oscillos-copes, thus giving an accurate zero time reference for the traces • A

typica1 experimenta1 arrangemmt including oscilloscope traces are shown in Fig. 10.

3.3 Experimerrtal Results

In the rarefaction fan, the expansion is shown by a decrease in pressure with time from the head of the wave H to the onset of condensation F (Fig. lla). The sudden release of la·tent heat due to the phasetransfor-mation from vapour/steam to water increases the pressure as depicted by the sudtlen jUIr!P to S, typical of a shock front. The traces , a and c are the output of the two piezotrons transducers located at 17.1 cm and 35.1 cm from the diaphragm, respecti vely. The pressure jUIr!P at the onset of

condensation (F to S) at the 17.1 cm location is relatively sharp and more in magnitude c0Ir!Pared to the jUIr!P at 35.1 cm. This is what is expected al:! the coo1ing rates are higher a:t locations closer to the diaphragm. The differential interferometer (registers density gradients) traces, show a smooth variation near the head of the rarefaction wave and an instant varia:tion at the onset because of the formation of the condensed vapour at

(17)

history is recorded by F-P laser interferometer. This interferometer

records density change of the order of 1.6432 x 10-5 gm/cc per fringe

shift. Tt is evident from the traces that initially there are larger density variations for a given time and the change slows down as time progresses. A unique feature of the interferometer is a detection of the onset point shown as a very sharp streak on the oscilloscope tracer. This is due to the fact that a large density gradient at the onset location throws the beam out of alignment temporarily because of the schlieren effect. This again helps us to locate very accurately the onset location. Some additional representative oscilloscope traces are shown in Fig. llb

and llc. Figure lld is the oscilloscope recording in dry N2.

Tt was desired later to monitor onset location for an additional point within the test section in order to have an idea regarding the

curvature of the locus of the onset front in x-t plane. For this purpose, the laser beam acting as an input to the differential interferometer was split in two forming an additional 2-beam interferometer. Therefore the e xperimental traces shown in Figs. 12a, 12b, 12c, 12d and 12e at location

17.1 cm have 3 tracers instead of two. The third tracer is at 26.1 cm

and is obtained by chopping the lower trace of the dual beam oscilloscope.

All the traces have a time base of 200 ~sec/per large division. There is

a time delay (500 ~sec) between the s tart of trace at 35.1 cm with respec t

to the trace at 17.1 cm.

As explained earlier at the onset point we expect an appreciable

departure from the isentropic flow (ie e., appreciable heat is added at

this point in the flow field). Therefore, the experiment al curve departs

from the theoretical equilibrium isentropes as expected and as shown in

Fig. 13. Initially, there is no appreciable variation in the experimental

and theoretical density profiles. This is because of the very low initial

mass fraction of the water vapour

«

2%).

However, once condensation occurs

the deviation becomes qui te rnarked.- Figure 14 shows a density profile •.

Two representative runs are plotted in Fig. 15. The onset of

the condens at ion locations are shown on 'the pressure- temperature diagram

along wi·th the equilibrium curve Ps(T) defined by Clausius-Clapeyron

equation. It is readily seen that the onset of condensation doe snot

occur at the intersection of the isentrope with the equilibrium Ps(T) curve, but at a supersaturated state.

The temperature and the corresponding supersaturation variation at two locations in an expansion fan are shown in Fig. 16a. The location closer to the diaphragm has a larger rate of cooling and hence large supersaturation is expected. A few more results are also shown in Fig.

16R. The condensation delay time, also called trelax, must depend upon

the rate of cooling. To provide a quanti tati ve insight, we did measure-ments at two locations in the rarefaction zone of the shock tube with different rates. The dispersion of the experimental results exhibiting this effect is shown in Fig. 17. A mean condensation time is thus estimated and is indicated in this plot. The condensation delay times have astrong dependence on the rate of cooling. That is, at the station near the diaphragm the delay is about half of what it is at the station which is twice as far and is independent ofthe diaphragm pressure ratio

(18)

From the experimental results , an en:;pirical relation between adiabatic

1 · " d th t f 1· dT . d . d .

supercoo ~ng, Ll, an . era· e 0 coc ~ng dt' ~s er~ve v~z:

T -T

(

)0.387

D,

= ;

c

=

1.73

X

10-

3 _

~;

s

(16)

where Ts is equilibrium saturation ten:;perature and Tc is the ten:;perature at the onset of condensation. The en:;pirlÎ:cal equation and ,the experim:mtal results , another relation between supercooling ~(~ = Ts-T c ) and

super-saturation S is derived for prediction of the onset. It is gi ven by

t:fr. =

18.321 (8_1)0.311 •

Therefore for a given supersaturation,

8,

one can

estimate supercooling required to initiate onset within the experimental constraints • As one expects at 8 = 1, i.e., condensation at saturation time will yield t:fr.

=

O. The experimental and theoretical prediction shown in the above equation are shown in Fig.

19.

4.

ANALY8I8

The en:;pirical equation (Eq.

16)

expressing the relationship between the adiabatic supercooling of ,the water-vapour/nitrogen mixture

an~ the cooling rate in the nonstationary rarefaction wave in a shock tube, rnay be rearranged into an equation for the location of the condensa-tion front in such a rarefaccondensa-tion wave. The flow being isentropic up to the onset of condensation, the cooling rate a particle of the gas mixture would experience on passing through this wave is (Ref.

18):

where T4 and a4 denote, respectively, the ten:;perature and the speed of sound of the mixture in the driver section, and )'4 is the ratio of specific heats of the mixture and is equal to

Cpi, CPv, Cvi, Cvv being the specific heats for constant pressure and constant volume of nitrogen and water vapour respectively; W4 is the specific humidity in the driver. It can be seen from Eq.

17

that the greatest cooling rate occurs at the head of the wa;ve, where x/a4t = -1 and becomes unlimi ted near the origin (t - t 0) •

hence

In addition, from Ref.

18

T D,=1-....5: T s

(18)

(19)

(20)

(19)

where xS/a.ts·is the nondimensional sldpe of the characteristic along

wm.ch sè,turation occurs 0 The equat·ion of the éondensation f.ront is then

1 x _2_,+ _',_s_ 7.4-1 8.4~s

.

0.387

x

10-3 (_

d~)

I , . " dt dT ' • ' . d T ·

.and.

dI

can bé fOMa, from Eq. 17. From thecondition that

dE

.-+·· a s

(21)

t :--*

ca,

it followsthat the co~d~nsation front 'Will tend' asymptotically to

: ··.the charac'teristic' xs/a..a.ts along whic,h equilibrium conden~a.tion ~ceurs 0 ' .

On the other hand, ,the ~owest 'temperature , . tne. parti.cj.es óf the. gas mixture

can' attain, is reached at .'thètail ó!'the wave;

and:

.

the cQndensatiön .front

. will begin a·t somepoint' o!\, th~ line bec~use of

the

rarefe.ctiQn mechanism,

ceases . aftsrwards • . 'rhe. ve1ocitJ(; of the front is obtained from Eq. 21. ailti 1.&

0.387

[ 1

{zfï~ ~)

.

.

..

~

.

J

.

(22)

~

=

U = ~. _ -:-___ - - - -_ _ _ _ _ _ .~2'

...

1t..,-..;;;1~-.,..a;;,.;;40=:.t.;..ils~--,·-_ _ _ ~ ... ,. _ _ ~_ . 2( .2 . x - 'a4t

.

\

·

74--J-xs,

)2

a4't s

where ~4

=

(r4-1)/(r4+1)

and ~4

=

2/(74+1). The Mach number relativeto the

front is

u-U

M =

-a I (23)

u is the partiele velocity, and a the .speed of sound at the point consideredo

Equation (21) shows that the location of t~e condensation front

depends on W4 (through 74 and

a4),

T4 and Ks/t S • For fixed values of T4

and W4 in the driver section, the ratio xs/a4ts ='Ns depènds only on CP4,

'the rela:tive humidity of the water vapour in the driver, in the following

'way (24)

.

,

,;

'

1

s

the munera;tor in the expressions for CP4 being the nondimensional water

(20)

depends on T4, W4 and ~4, i.e., on the parameters which determine the'

condition of' the mixture in'the driver section. '

The onset equation (21) is numerically solved using Eq. 17 and Newton's iteration technique f'or the pair of' values of' x, t, satisf'ying Eq. 21._ The velocity and Mach nurober f'or the onset f'ront are al'sQ

computed simultaneously f'róm Eqs. 22 and 23. For these computations, T4, W4 and ~4 are used as input parameters and the propagation of onset of

condensation f'ront in x-tplarie is determined for a wide range of' these parameters. These parameters essentially define the initial state of mixture in the driver section.

Figures 20, 21 and 22 show the location of' the condensation f'ront when two of the three parameters T4, W4 and ~4 are kept f'ixed and the third is varied. The supersaturation attained in the condensation fron t and Mach nurober are shown in Fig. 20 for one particular case. The experimental point for the onset of condensation is also shown f'or a typical experimental run. The results from this parametric study are indicated in the following section.

5.

DISCUSSION OF THE RESULTS

The present investigation of homogeneous (nonequilibrium)

condens~tion of' water vapour/nitrogen mixtures in nonstationary raref'action waves in a shock tube show the following facts:

1. ' The expansion is isentropic up to the onset of' condensation, i.e., within the experimental accuracy the rèsults show no signif'icant

departure f'romwell known isentrqpic flows in a shock tube expansion f'ai1 until the onset is reached.

2. In the narrow condensation zone a spontaneous change of' state in the gas mixture occurs giving ri se to condensation f'ront, af ter which f'low rapidly approaches the equilibrium expansion conditions.

3.

Two empirical relations viz (a) between the nondimensional adiabatic

T -T 0.387·

supercooling and the cobling rate (6

=

;s c

=

1.73 X

10-3(_~~)

~

and (b) the supercooling and the supersaturation (~

=

Ts-T c

=

18.321 0.311

(S-l). ) are derived f'rom the experimental results.

4.

The empirical relation (a) above is inserted in the theoretical

e,xpression f'or the cooling rate in an isentropic expansion in a shock tube; in order to formulate a general analytical expression f'or the propagation of' the onset of condensation front in an x-t plane.

5. The onset of' condensation f'ront propagates in x-t plane such that its slope with respect to x-axis decreases until i't approaches asymptotically parallel to the saturation characteristics line,.

6.

The onset of' condensation is most sensitive to relative humidity

(21)

in the driver section (keeping l'4 and w4 constant) results in a shorter condensation delay ti~ at a given'location in the shock tube expansion fan.

7.

An increase in the specific humidity W4 (keeping T4 and CP4 constant) displaces the condensation front such 'that condensation occurs at lower 'temperature zone ' of the rarefaction fan.

8.

The variation of T4 alone (while W4 and CP4 are fixed) has little effect on the loca'tion condensation front.

9.

'l:he diaphragm pressure ratio, P41, across the driver andthechannel section of the shock tube has no effect on 'the location of tl1e conden-sation front as it does not change the rate of cooling. By increasing P4J,.'the amplitude of the rarefaction fan increases and the condensation'

front line propagates further towards thetail of 'the fan.

10. The validity of the kinetics of the nucleation process can be examined knowing the functional dependence of critical supersatUration versus

't~llIJierature, and it should be approximately linear between Ln s and

T 3{2 (Ref.

14).

This dependence is also examined in the present

investigation and shown in Fig.

23.

This shows a very good agreement for the ,classical nuclea.tion theory developed by Volmer and Weber

(Ref~.

6

'

,

16).

11. We·find that the shock tube results (nonstationary flow) show a good qualitati ve ggreem:mt with the nozzle flow (steady flow) experiments • But these resul'ts extend quantitatively in providing condensation from higher supersaturation state of vapour and varying cooling rates for an experiment of specified initial conditions. As a matter of fact, this extra degree of freedom (Le., varying rates of cooling) obtained in shock tube flows is because cf ~the addi tional dimension of time 'tl which is absent in nozzle flows.

(22)

1. Wils on, C.T.R. 2. Stodcüa, A. 3. Hi11 , P. G. 4. Deych, M. 'E. Stepanchuv, V. F. Saltanov, G. A. 5. Borschdroff, D. Dunning, W. J. Wegener, P. P. Wu, B.J.C. 6. Volmer, M. L. Weber, A. 7. Oriani, R. A. Sundquist, B. E. 8. Wegener, p. P. Mach, L. M. 9. Wegener, P. P. Lundquist, G. 10. Glass, :1;. I. Patterson, G. N. 1l. Homer, J. B. 12. Kung, R.T.V. Bauer, S. H. 13. Kawada, 1I. Mori, Y. 14. Wegener., P. P. 15. Becker, R~ Doring, W. 16. Volmer, M. 17. Hall, J. G. REFERENCES

(i) Trans. Roy. Soc. (London) 189, 265 (1897) "SteamGas Turbines", McGraw Hill, N.Y., 1927 J. F1uid Mech. 25, 593 (1966)

Heat Transfer - Soviet Research (Eng, Trans.)

-*,

196 (1969)

Nature-Physical S.cience, 240, lp6 (1972)

Phys. Chem. 119, 277 (1926)

J. Chem. Phys. 38, 2084 (1963)

Adv. App. Mech.

2,

307 (1958)

J. App. Phys. 22, 233 (1951)

J. Aero. Sci. 22, 73 (1955)

8th International Shock Tube Symposium, I~erial

College, London, U.K. (1971)

Proc. 8th Int. Shock Tube Symp~, Imp. College, London (Ed. by J. L. Stol1ery, 1971)

Bulletin of J.S.M.E. 16, 1053 (1973)

"Gasdynamics of Nonequilibrium Flows", VOl. 1, Part 1 (Chapt. IV) Ed. by P. P. Wegener , Pub. by Marcel Dekkov

Ann. Physik, 24, 719 (1935)

"Kineti~ der Phasenbi1dung", Steinkopff, Dresden Leipzig (1939)

(23)

18. Glass, I. I. Hall:, J. G. 19. Kantrowitz, A. 20. Powell , C. F. 21. Pound, G. M. MadoIll1a, C. A. Sciulli, C. M. 22. Allen, L. B. Kassner, J. L. 23. Oswatitsch, K. 24. Stein, G. Wegener, P. P. 25. Dawanson, D. D. Wils on, E. J. Hill, P. G. Russell, K. G. 26. Kurshakov, A. V. Talmanov, H. A. Tkalenko, P. A. 27. Kalra, S. P. 28. Kalra, S. P. Measures, R. M.

"Handbook of Supersonic Aerodynamics", Section 18 - Shock Tubes. NAVARD Rep. 1488 (Voil:. 6) "A Bureau of Naval Weapons Publication" (1959)

J. Chem. Phys. 19, 1097 (1951) Proc. Roy. Soc. Al19, 553 (1928)

Proc. Conf. on Interfacial Phenomena and Nucleati on,"

Vol. 1 11

Conference on Nucleation", Ed. by H. Reise, AFCRC Rep. No. 55-211, 85 (1955)

Jour. of Collisions and Interface Sci. 30, 81 (1969)

Zeit fur Angewandte, Math. Mech. 22, 1 (1942) J. Chem. Phys. 46, 3685 (1967)

J. Chem. Phys. 51, 5389 (1969)

J. App. Mech.

&

Eng. Physics (in Russian), No. 5, 117 (1971)

University of Tor.onto Institute for Aerospace S'tudies (UTIAS) Report 181, 1972

(24)

p P4 - - - _. -I I I ~b.T~ I I Supply T4 T

FIG. 1 A TYPICAL VAPOUR PRESSURE CURVE AND ISENTROPE WITH DEFINITIONS

3

o~ __ ~ __ ~ __ ~ __ ~ __ ~~

200 210 220 230 240 250 260

TOK

(25)

~lv ~~ ~ !-...Q

~

t1J

~

~

t

FROZEN

FROZEN , NONEQUIUBRIUM , ' ' ' : ... EQUIUBRIUM

"

./'"

1;,9

, " /

"

.

-x

X20 XIO

o

FIG. 3

x-t

DIAGRAM FOR A SHOCK TlI3E FLON

( i ) WITHOUT CONDENSATlON ( - )

(ii) WITH NONEQUIUBRIUM CONDENSATION (---)

/ / /

"

-':/

,

'

.

~

(iii) EQUIUBRIUM CONDENSATION WIL!. ~ ALDNG Teq CHARACTERISTICS. SHOCK WAVE AND CONTACT SURFACE ARE SHOWN BY _._._.

(26)

VACUUM

a

PRESSURE GAUGES LASER~ WATER VAPOUR INJECTION SYSTEM C!!"' J H EATER VACUUM

a

PRESSURE GAUGES

DIAPHRAGM OU MP CHAM BER

MECHANICAL DIAPI:!RAGM BURSTING DEVICE GLASS WINDOW _ _ _ _ '< ~.I.< _ _ _ _ _ _ _ _ _ - - J PHOTODIODE TO GAS CYLINDER TEST SECTION STAINLESS STEEL TUBE i i TO VACUUM PUMP

(27)

W

al

:::>

o

t-~

U

o

:L

en

z

o

t-<t

en

z

w

o

z

o

u

W

:I:

t-lJ...

o

3:

w

->

...J ...J

<t

I

0:::>-

Wt>

-o:::!

u

z~

<tLL.:

LO

l!5

-

LL..

(28)

1. 1. fobry-Perot Plotes (2)

tw

M l ELEVATION Shock Wave

t

PLAN M4 Mirrors (2) Stops (2) Norrow Band Filter Photomultiplier

(29)
(30)

UPPER TRACE OSCILLATING MIRROR SIGNAL

LOWER TRACE MODULATED INTENSITY SIGNAL

BOTH TRACES REPRESENT MODULAION

OF INTENSITY SIGNAL

(31)

o 1

o

- - - cos· (

l-)

Approximatlon ~ Theoretica I ~ A Experlmental \

\

\

\

,I

\

\

\

,2

\

\

\

\

\

\

\

\

\

,3

\

\

\

~ ,4 ,5 '11' PIlo.. CIIartQe. s ,6

FIG. 8 A CAL I BRATI Drl CURVE

TT PHASE SHIFT

,7 ,8 ,9 lP

(32)

LASER

SEMITRANSPARENT

SURFACES

RAREFACTION

WAVE

SLir

OPTICAL FILTER

PHOTOM U LTI PLI ER

TUBE

TO

OSCI LLOSCOPE

(33)

CONDENSATION SHOCK WAVE,si. ~ RAREFACTION WAVE x .. P!EZOTRON PIEZOTRON 2 §ERJ~)~-~--_·J.--_· F.P.

DIFFERENT!AL LASER INTERFEROMETER

FIG. 10 CONTACT SURFACE/

C

~ SHOCK WAVE DIAPHRAGM

/

S ~x PIEZOTRON 2; 100 Torr/cm r ------- - , F.P. LASER INTERFEROMETER; 1.6432 x 10-5 gm/cc/Fringe Shift PHOTODIODE PIEZOTRON 1; 87 Torr/cm

DIFFERENTlAL LASER INTERFERQr-1ETER . . . • 6p 10-5 gm/cc 'Sens~t~v~ty --- ~

6x cm

BASIC ARRANGEMENT FOR STUDYING 'IW}-PHASE-F:U::MS IN A COODENSATIOO SH<Xl< TUBE OSCILLOSCOPE '2' TIME SCALE 200 \lsec/cm DELAYED TRIGGER SCALE OSCILLOSCOPE '1'

(34)

(b)

(C)

(dl

FIG· I1 a TYPICAL EXPERIMENTAL RESUL TS

P4 : 680 TORR,

p,:

8.4 TORR '14: 92% T4= 200 C

P4= 680 TORR, PI: 0.25 TORR '14= 61. 7 % T4= 200 C

Q. PIEZOTRON PRESSURE TRACE AT XI

b. DIFFERENTlAL LASER INTERFEROMETER OUTPUT

c. PIE ZOTR ON PRESSURE TRA CE AT Xt

(35)

x = 11.1 \,;m X· 35.ICm Scale 200 fLSec/C m p." 680 TORR 1/4084 'Ya FIG. 11 b PI "0.2 TORR T. "292.2 "K x = 17.1 Cm X" 35.1 Cm Scal. 200 fLSec/Cm p. 0 !l80 TORR '/. "58 'Ya FIG.llc PI "0. 15 TORR T." 296 oK x = 17.1 Cm x-35.1 Cm Scal. 200 fLSec/Cm P.-680 TORR !/.oO'Ya

DRY NITROGEN RUN FIG. lid

Pi "0.3 TORR

(36)

X- 17.1 Cm X' 26.1 Cm--x = 35.1 Cm Scale 200 P. Sec/Cm P4 -400 TORR IJ 4 -64.32 'ro FIG. 12a PI-2.3 TORR T4-297.8 oK x • 17.1 Cm X' 26.1 C m _ X=35.1 Cm Scale 200 P.Sec/Cm P4• 400 TORR tf 4' 65.44 'ro FIG. 12b PI -3.85 TORR T4 -297.4 oK X-17.1 Cm X =26.1 C m _ x = 35.1 Cm Scale 200 p.Sec/Cm P4 - 424 TORR '14 -78.03 'ro FIG. 12c PI -QI TORR T4 -293.6 OK

(37)

X =17.1 Cm

x

= 26.1 Cm •

x

= 35.1 Cm Scale 200 fLSecl Cm P4 • 600 TORR

«14-

88.4 % FIG . . 12d . PI -100 TORR T4 - 297.75 OK

x ..

17.1 Cm X- 26.1 C m -X .. 35.1 Cm P4 • 440 TORR

'14

-91.60 % Scale 200 fLSec/Cm FIG. 12, PI • 100 TORR T4 - 29S.35°WC

(38)

P

Po

(1

e, •

Gal

TORR

T

o

=

293.5

t<

~

=

61.7%

- THEORETICAL ISENmOPES

1.0

I

o.

~

o

ExPERH18ITAL

Porrrrs

AT locATION

Xl

0.9

0.8

0.7

0.6

"D

,

A

"

"C\

"

"

D ExPER IMENTAL

PDItrrS

AT l.ocAnoN

X2

---- PRESSURE BLt1P DUE TO CONDENSATION ftM)

HENCE DEPARTURE FROM I SENTROPE

0.5'

Y ci'>r " Y "

o

0.2

0.4

0.6

0.8

1.0

1.2

1.4

1.6

1.8

t

(m. sec. )

FIG. 13 THE THEORETICAL (EQUILIBRIUM) ISENTROPES AND EXPERIMENTAL RESULTS

(39)

P Po 1.0 0.8 0.6 0,4 25 20 15 ~

...

... 0 ~ ~ U.J S Cl) Cl) .... 10 If et::: 0 Cl. ~ 5 Po = 6m T~ To = 293.9? I~ ~ =(j.l.77.

ExPERltt::NTAL POltfTS AT LOCATION ~

a

FIG. 14 DENSITY PROFILE AT 35.1 CM FROM THE DIAPHRAGM IN THE RAREFACTION

FAN OF THE SHOCK TUBE

1.2 A X=35.lcm • X=17.lcm

ONS ET A ON SET A

t ONSET 1.4 1.6 1.8 20 t(m .• ic.) s= 14.17 (at 17.lcm) 6=3.67 (at35.1cm) A

A A

..

A ONSET PV4 • .-7.62 (atl7.1crN

A

,.A

6"521. (at 35.1cm) \

FIG. 15 THE EQUILlBRlUf~ PRESSURE THIPERATURE OIAGRN·1 AND

SUPERIMPOSED EXPERUlEfHAL RESULTS FOR EXPANSION OF WATER VAPOUR/NZ MIXTURE IN A RAREFACTION ZONE OF nlE SHOCK TUBE

250 260 270 280 290 300 310

(40)

300 2 8 280

1

7 T (OK)

I

S 6 270-ts 4 :3 2soJ 2 T x= 17.1 cm X= 35.1 cm

/~

#320474 T S trelax x o

*

• '389 696 fl sec flsec P4 = 650 Torr ~ = 4 Torr

4>4.

51.84"0 1.114' 0.0115 T4 a 24.O"C

/s

25°12

i I I I i I X-I"Zlcm 0.3 0.4 O!l oe 01 Q8 0.9 X-35.1 cm 08 0.9 1.0 1.1 1.2 1.3 l4 UI 1.6 t (msec)

..

0 1.1 '300 290 16

280~

T(OK) 14S 12 270

r

8 6 260

1

4 2 250 X-17.1 cm.0.4 0.5 X:35.1 cm. .9 I .0 0,6 1.1 0.7 1.2 T S trein # 47!J174 P4 = fffi TORR PI = 75 TORR ~ = 88.931. W4~ fJ.tL99 T4 = 'll..JOC X = 17.\ cm. X

*"

500 JLsec x= 35.1 cm. 0 • 832 JLsec (ij e 0.8 0~9 1.3 1.4 FIG. 16b \.0 1.5 t(m •• c.) 1.6 1.7 1.8

(41)

16

Ie

14 13

1

12 11 10 9 9 8 7 6

e

4 3 2

-x

LOCATlON~ t 35.1 1'7.1 0 x-t diagram

.it

x

X· 17.1 cm. ~ . \ 1 I

I

I

I(l

I

I

j

,

11

I

1 )('

I

I

I

I

I

I

la

I

I

81

I

I

I

I

I

L

I

I

I

1

ol

h

o

0.1 O.~ 0.3 0.4

o.e

0.6 ~~

..

I

I

I

I

'"

~

X

el

9

1

I

13

I

I

I

I

I

I

0.7 0.8 0.9

••••

si "41 W4 x 1'0474 .71' 1100 .0114 0 Sl047f ... 4 lOl .014' 8 •• 0474

...

114 .ol . . 6 410414 .1'1

..

.0111

4"474 ... 1 .4 41'4 V 440474

...

,

.. , .0171

<:r

...,0474

M'

,

.0",

4'0474 ... 4

.oIU

• 'AII IILAXATlO .. TIN"

490 r ' . c (at 17.1 cm)

eSI

r··

c (at 35.1 cm)

1.0

FIG. 17 DISPERSION OF EXPERIMENTAl RESUlTS SHOWING DEPENDENCE OF CONDENSATION DElAY TIME

(42)

48 40 ~ 32 ::ï o 8 AT cr: I&J ~ 24 16 8 .2 0 r - - - - -.18 .16 .14 .12 .02

FIG. 18 ADIABATIC SUPERCDOLING RESULTING COllDENSATlON DELAY, 6,

VERSUS THE RATE OF COOLlNG(

*

î

IN NONSTATIONARY EXPANSION OF WATER VAPOUR/rl2 rUXTURE )N , SHOCK TUBE

°O=---~---L----~----~---~---L----~

2 4

Ei[)

8 10 12 14x10'

\

~J OK/sec

THEORY AT.ra32r (S_rlo.3U EXPERrMENTS • •

FIG. 19 IMPlRICAL RELATION BETWEEN SUPERCOOUNG AN) SUPERSATURATION IN A NON5mTIONARY EXPANSION OF WATER VAPOUR/N2-MIXTURE W A SHOCK TUBE FLOW

(43)

T4 = 295.3°K

W4 =0.0177

'I' cP4

=97.3% '2'

cP

4 = 70.0% '3'

cP4=

40.0%

la EXPERIMENTAL ONSET POINT AT SUPERSATURATION=13.75

FIG. 20 x-t DIAGRAM FOR CONOENSATIDN FRONT SHOWING THE EFFECT

-x(cm}20

Of VARIATION OF RELATIVE HUMIDITY, ~4 WITH TEMPERATURE T4 SPECIFIC HUMIDITY. "4 ARE KEPT CONSTANT, MACH NUMilER SUPERSATURATION ANO AN EXPERIME1HAL ONSET POINT ARE ALSO SHOWN FOR A TYPICAL CASE

18 16 14 12 10 8 6 T 4 =295.3°K c%>4 = 97.3% [J W4 =0.0177 • w4 =0.2 • ~4 =1.0

FIG. 21 x-t DIAGRAM FOR A CO~IDENSATION FRONT WHERE ~ 4 AND T 4 ARE KEPT C01iSTANT AND"4 IS VARlED

4 2 t (m.sec.) 1.6 1.4 1.2 1.0 0.8 0.6 0.4 o tCm.sec.) 0.8 0.7 Q6 0.5 0.4 0.3 0.2 2 4 +x

(44)

..

q,4=97.3% W4=0.0177 • T 4=295.3°K • T 4=320oK • T4=400oK

FIG. 22 x-t DIAGRAfl FOR CONOENSATlorl FRONT WIlERE '" 4 AllO w 4 ARE KEPT CONSTANT AND T4 IS VARIEO

-x(cm) 9 8 3.0 2.5 Ln S 2. 1.5 2.2 7 6 23 5 4 FIG. 22 3 2.4 t (m.sec) 0.7 0.6 0.5 0.4 0.3 2 o 2.5 I x(cm)

(45)

UTIAS REPORT NO. 195

Institute for Aerospace Studies, University of T oronto

EJCPERIME:lfrS 011 1'I00000UILIBRrtJM, I'IONSTATIONARY EXPANSIOII

OF WATER VAPOUR/CARRIER GAS MIXTURE III A SHOCK TUBE

Ka1ra, S. P. 16 pages 23 figure.

~

1. Condensation 2. Water Vapour 3. Ncmequilibrium Expan.ion 4. Shock Tube 5. Laser Interferometer

I. Kalra, S. P. II. llrIAS Report Ilo. 195

The lnvestigatlon of condensation process in a nanstatlonary nonequil1brium. expansion of water vapour/ carrier gas (ultra pure N2) mixture is presented here. The density varlat1ons, pressure variatlons

and onsel:; of condensatlon due to such expansion, are IOOnitored at two fixed locations in the driver sectlon of the shock tube by using a laser Fabry-Perot lntert'eroneter, EL differential interferometer

and piezotrons transducer devices. The effect of the coaling rate on the supersaturation at onset of condensation and its delay time (nonequiUbrium zone) is determ1ned. An empirical relation is derived

between the supercooling and. the rate of cooling at onset of condensation. A theoretical analysis is

performed using this emplrical relation in order to determ1.ne the lcx::atian of the onset of condensation

in sueh expansions • I t i. shown tbat the location of the onset i. unique1y determined for a g1 ven

initial driver eondition, e.g., (i) re1ative humidity, '1'4, (11) vapour mass fraction, "'4, and (11i)

temperature T4 • A parametrie .tudy, using the.e 3 parameter. i. &lso given. The experimental findings are in agreement with the theoretie&l predietion of onset.

UTIAS REPORT NO. 195

Institute for Aerospace Studies, University of T oronto

EXPERIMENTS 01'1 1I000000UILIBRIIJM, I'I<l'1STATIOHARY EXPANSIOl'I

OF WATER VAPOUR/CARRIER GAS MI:X'rURE III A SHOCK TUBE Kalra, S. P. 16 page. 23 figure.

~

1. Ccmdensation 2. Water Vapour 3. IIcnequilibrium Expansicm 4. Shock Tube 5. Laser Interferometer

I. Kalra, S. P. II. llrIAS Report Ilo. 195

The investigation, of condensat1on process in a nanstatlonary nonequilibrium expansion of water vapour/

carrier gas (ultra pure N2) mixture ls presented 'here. The denslty variatlons, pressure variations

and onset of condensation due to such expansion, are monitored at two fixed locations in the driver section of the shock tube by using a laser Fabry-Perot interferoneter J a differential interferometer

and piezotrons transducer devlces. The effect of the cool1ng rate on the supersaturation at onset of condensation and its delay time (noneqUilibrium zone) 1s determined. An empirical relation is derived

between the supercooling and. the rate of cool1ng at anset of condensation. A theoretical analysls is

performed using thi. e';'irieal re1ation in order to determine the location of the onset of eondensation

in sueh expansians. I t i. shown tbat the location of the onset il unique1y determined for a g1 ven

initial driver eondit1on, e.g., (i) re1ative humidity, '1'4, (11) vapour mass fraetion, "'4, and (11i) temperature T4. A parametrie study, using tbese 3 parameters is &l.o given. The experimental fiDd1nga are in agreement with the theoretieal pred1etion of onset.

Available co pies of this report: are limited. Return th is card to UTIAS, if you require a copy. Available co pies of this report: are limited. Return this card to UTIAS, if you require a copy.

llrIAS REPORT NO. 195

Institute for Aerospace Studies, University of T oronto

EXPERDIENTS 011 lIDNEQUILIBRIUM, I'IONSTATIONARY EXPANSIOl'I

OF WATER VAPOUR/CARRIER GAS MIXTURE III A SHOCK TUBE

Kalra, S. p. 16 page. 23 figure.

~

1. Condensation 2. Water Vapour 3. IIcnequilibrium Expansicn 4. Shock Tube 5. Laser Interferometer

r. Kalra, S. P. Ir. llrIAS Report Ilo. 195

The 1nvest1gat1on of condensatlon process in a nanstationary nonequil1brium expansion of water vapour/ carrier gas (ultra pure N2) mixture 1s presented bere. The dens1ty variat1ons, pressure variations

end onset of condensatlon due t.o sucb expans1on, are monitored at two fixed locations in the driver

section of the shock tube by uslng a laser Fabry-Perot interf'ercmeter, a differential interferometer

and plezotrons transducer devices. The effect ot tbe cooting rate on tbe supersaturation at anset of condensatlon and i ts delay time (noneqUilibrium zone) is determined. An empirical relation is deri ved

between bhe supercooling and the rate of' cooling at onset of condensat1on. A theoretical analysis is

'per:tormed using this emp1rlcal relation in order to determine the locatlan of the onset of condensation

in sueh expansions • I t i • • hown that the location of the onset is unique1y determ1ned for a g1 ven

initial driver eond1t1on, e.g., (i) re1ative humidity, '1'., (11) vapour ... fraction, "'4, and (11i) temperature T4. A parametrie .tudy, using these 3 par .... terl ia &lso given. The experimental finding. are in agreement with the theoretieal predietion ot onset.

~vailable copies of this report: are limited. Return this card to UTIAS, if you require a copy.

UTIAS REPORT 110. 195

Institute for Aerospace Studies, University of T oronto

EXPERIMENTS ON NOl'IEQUILIBRIUM, I'IONSTATIONARY EXPANSION

OF WATER VAPOUR/CARRIER GAS MIXTURE III A SHOCK TUBE Kalra, S. P. 16 page. 23 figure.

~

1. Candensation 2. Water Vapour 3. IIcnequilibrium Expansicm 4. Shock Tube 5. Laser Interferometer

I. Kalra, S. P. II. llrIAS Report Ilo. 195

The investigatlon, of condensation process in a nalStationary nonequil1brl\un expanslon of water vapour/

carrier gas (ultra pure N2) mixture is presented here. The densl ty variatlons J pressure variations

and onset of condensation due te such expansion, are monitored at two fixed locatioru: in the driver section of the shock tube by us1ng a laser Fabry-Perot lnterferoneter, a differential lnterferometer

and p1ezotrons transducer devices. The effect of tbe cooling rate on the supersaturation at onset ot

eondensation and i t . de1ay time (nonequilibrium zone) is determined. All empirie al re1ation 1. derived between the .upereool1ng and the rate of eooling .. t onset of eondensation. A theoretiea1 analysi. is

performed using thi. empirie&l relation in order to determine the location of the onset of eorulensation

in .ueh expansions • It i. shown that the 10eation of the onset i. unique1y determined for a g1 ven

initial driver eondit1on, e.g., (i) re1ative humidity, '1'4, (11) vapour ... fraction, "'4, and (11i) temperature T.. A parametrie Itudy, using the.e 3 par .... ter. i. &lso given. The experimental finding.

are in agreement with the theoretieal predietion of onset.

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