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A NEW CORRELATION FOR ROUND DUCT AND UNIFORM HEATING-COMPARISON WITH WORLD DATA ySw PIÜ1P L. BIASI**, G.C. CLERICI**, S. GARRIBA***, R. SALA* and A. TOZZI** 1967 EURATOM/US Agreement for Cooperation EURAEC Report No. 1874 prepared by ARS, SpA Società Applicazioni Ricerche Scientifiche, Milan - Italy Euratom Contract No. 106-66-12 TEEI 'M
Transcript

A NEW CORRELATION FOR ROUND DUCT AND UNIFORM HEATING-COMPARISON WITH WORLD DATA

ySw PIÜ1P

L. BIASI**, G.C. CLERICI**, S. GARRIBA***, R. SALA* and A. TOZZI**

1967

EURATOM/US Agreement for Cooperation

EURAEC Report No. 1874 prepared by ARS, SpA Società Applicazioni Ricerche Scientifiche, Milan - Italy

Euratom Contract No. 106-66-12 TEEI

'M

RfiÍítá'HSBiAÍ l ^ ' 1 F .1 r r r i-cinn , uocument was prepared under the sponsorship ot the L-ommission o

the European Atomic Energy Community (Euratom) in pursuance of the joint programme laid down by the Agreement for Cooperation signed on 8 November 1958 between the Government of the United States of America and the European Atomic Energy Community.

_uratom Commission, nor the Government contractors or any person acting on their behalf :

It is specified that neither the E of the United States, their contrae

i akes any warranty or representation, express or implied, with respect to the accuracy; completeness, or usefulness of the information contained in this document, or that the use of any information, apparatus, method, or process disclosed in this document may not infringe privately owned right,; or %3Si Assume any liability with respect to the use of, or for damages resulting from the use of any information, apparatus, method or process disclosed in this document

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ilKiililllliîSiiii^ ¿t.::*!·!*!

MÉjgjtóí ι,«?

This report is on sale at the addresses listed on cover page 4

at the price of F F 7. FB 7 0 . - D M 5.60 Lit. 870 FI. 5

ι·»*» »I

When ordering, please quote the EUR number and the title, whic

indicated on the cover of each report indicated on Tne cover or eacn repon.

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SMEETS

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tøj

This document was reproduced on the basis of the best available Co

!« Mm*» ■sm ^-'VWftm rkif'iiL·'^ Mà&

;U,.*$íi ä-ö?!} fctfíi

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EUR 3376 e

A NEW CORRELATION FOR ROUND DUCT AND UNIFORM HEATING - COMPARISON WITH WORLD DATA by L. B1ASI** G.C. CLERICI**, S. GARRIBA***, R. SALA* and A. TOZZI*

*ARS, SpA **ARS, SpA and University of Milan

***CESNEF

European Atomic Energy Community - EURATOM EURATOM/US Agreement for Cooperation EURAEC Report No. 1874 prepared by ARS, Spa Società Applicazioni Ricerche Scientifiche, Milan (Italy) Euratom Contract No. 106-66-12 TEE1 Brussels, September 1967 - 56 Pages - 37 Figures - FB 70

A new correlation, having a large range or validity and applicable

EUR 3376 e

A NEW CORRELATION FOR ROUND DUCT AND UNIFORM HEATING - COMPARISON WITH WORLD DATA by L. B1ASI** G.C. CLERICI**, S. GARRIBA***, R. SALA* and A. TOZZI*

*ARS, SpA **ARS, SpA and University of Milan

***CESNEF

European Atomic Energy Community - EURATOM EURATOM/US Agreement for Cooperation EURAEC Report No. 1874 prepared by ARS, Spa Società Applicazioni Ricerebe Scientifiche, Milan (Italy) Euratom Contract No. 106-66-12 TEEI Brussels, September 1967 - 56 Pages - 37 Figures - FB 70

A new correlation, having a large range of validity and applicable

EUR 3376 e

A NEW CORRELATION FOR ROUND DUCT AND UNIFORM HEATING - COMPARISON WITH WORLD DATA by L. BIASI** G.C. CLERICI**, S. GARRIBA***, R. SALA* and A. TOZZI*

*ARS, SpA **ARS, SpA and University of Milan

***CESNEF

European Atomic Energy Community - EURATOM EURATOM/US Agreement for Cooperation EURAEC Report No. 1874 prepared by ARS, Spa Società Applicazioni Ricerche Scientifiche, Milan (Italy) Euratom Contract No. 106-66-12 TEEI Brussels, September 1967 - 56 Pages - 57 Figures - FB 70

A new correlation, having a large range of validity and applicable

to circular ducts with uniform heat flux distribution, shall be presented. This correlation is compared with most burnout data with negative inlet quality (X < O ) existing in the world. The mean quadratic errore, over

in 4551 experimental data coming from various laboratories, is 7.26 %, and the 85.5 % of these data has an error less than 10 %. At last 576 data, which are external to the validity range, are examined and some corrective factors are suggested in order to extend the validity range of the correlation.

to circular ducts with uniform heat flux distribution, shall be presented. 1 his correlation is compared with most burnout data with negative inlet quality (X < O ) existing in the world. The mean quadratic error π , over

in 4551 experimental data coming from various laboratories, is 7.26 %, and the 85.5 % of these data has an error less than 10 %. A t last 576 data, which are external to the validity range, are examined and some corrective factors are suggested in order to extend the validity range of the correlation.

to circular ducts with uniform heat flux distribution, shall be presented. This correlation is compared with most burnout data with negative inlet quality (X < O ) existing in the world. The mean quadratic error a, over

in 4551 experimental data coming from various laboratories, is 7.26 %, and tbe 85.5 % of these data has an error less than 10 %. At last 576 data, which are external to the validity range, are examined and some corrective factors are suggested in order to extend the validity range of the correlation.

EUR 3376 e

EUROPEAN ATOMIC ENERGY COMMUNITY - EURATOM

A NEW CORRELATION FOR ROUND DUCT AND UNIFORM HEATING-COMPARISON WITH WORLD DATA

by

L BIASI**, G.C. CLERICI**, S. GARRIBA***, R. SALA* and A. TOZZI**

*ARS, SpA

* * ARS, SpA and University of Milan

'**CESNEF

1 9 6 7

EURATOM/US Agreement for Cooperation

EURAEC Report No. 1874 prepared by ARS, SpA Società Applicazioni Ricerche Scientifiche, Milan - Italy

Euratom Contract No. 106-66-12 TEEI

SUMMARY

A new correlation, having a large range of validity and applicable to circular ducts with uniform heat flux distribution, shall be presented. This correlation is compared with most burnout data with negative inlet quality (X < O ) existing in the world. The mean quadratic errore, over

in 4551 experimental data coming from various laboratories, is 7.26 %, and the 85.5 % of these data has an error less than 10 %. At last 576 data, which are external to the validity range, are examined and some corrective factors are suggested in order to extend the validity range of the correlation.

KEYWORDS

BURNOUT TUBES STATISTICS ERRORS HEATING NUMER1CALS HEAT TRANSFER

Correlation function

TABLE OF CONTENTS

$ 1- Introduction pag. 5 $ 2- Critical heat flux correlation pag. 7 t 3- Range of validity pag. 12 I 4- Comparison with the experimental

data. pag, 13 $ 5- Examination of the data vhich are

external to the validity range pag. k3

Nomenclature pag. 53 Bibliography pag. 54

ACINOtfLEOHENT

Prof.M.Silvestri gave his time generously to discuss the program during the course of the investigation. Prof.S.Albertoni provided encouragement and suggestion in the writing of this report.

INTRODUCTION

1 2 3 4 In some previous works ' * ' the most important burnout

correlations ­ for circular ducts, uniform heat flux di­

stribution and positive outlet quality ­ have been exa­

mined. In these works it has been pointed out that nearly

all the correlations may be reduced, by means of suitable

transformations, to a common analytic form which consists

of one or two straight­lines in the plane φ^Χβ· Tlle

study

of the correlations thus transformed gave us the idea of

predicting the burnout data by means of the following expe­

riments:

for low quality

M 4.45-1?

4 . Q-^5H

?' ^_ A-xQ) 0 r

f t Wn°

: s /p-G \y \ '

1.056· H^ [ox

for high quality

<*

. 0.4 for D>1 y 0 f o r D>1

^ 0 . 6 fo r D<1 0.2 for D<1

As predicted value of the critical heat flux the higher

value of the two, obtained by intersecting eq. (1) */ith

the heat balance equation, was chosen. This correlation

has been compared with 2000 experimental burnout data

in the range: 30 ata^P^MOO ata, 0.35 cm¿ D* 3cm, 20 gr/cm 2

sec.^G^560 gr/cm sec, 20 cm ̂ L ^ 500 cm, X. ¿. 0, X 0 > 0

Manuscript received on July 12, 1967.

The main aims that we want to attain in the present work are the following:

i) To simplify the form of eq. (1) ii) To increase the parameters validity range. iii) To increase the number of the experimental burnout

data for the comparisons, iiii) To improve the accuracy of predictions.

2. CRITICAL HEAT FLUX CORRELATION

The empirical correlation proposed is the following!

Φ. >1·βς?3· 4<f

D" G V« yfp)

φ . 3.7810^(Ρ) % ij4 G06

Vi

1 - Xo

- ΧΌ for low quality

w i t h o< /

\

0.4 for D>1

0.6 for D O

fa) for high quality

Eq. (2) consists of two straight-lines, whose intersection point does not take place at constant outlet quality, but depends on pressure Ρ and mass flowrate G:

2.CH · h M M

As "a.priori"it is not possible to divide the validity range of these two straight-lines, we have thought of taking, as the predicted burnout point, the higher of the two values obtained by means of the intersection of eq.(2) with the heat balance equation:

t- -̂ τφο-*.») (4)

8

In fig. 1 the trend of the correlation, for a typical group

of values of the parameters is showed. In the same diagram

the heat balance equation and burnout points, defined by

means of the previous rule, are also reported.

With regards to eq. (ï), the new correlation shows a dif­

ferent dependence on Lhe pressure and a more simple form

of the trend at high quality. The two functions y(Ρ) and

h(P), whose trend in the range 2 ata^P^ 140 ata is showed

in figs. 2­3, are defined by means of the following equa­

tions:

-Ü.032D /__\

y(p) * 0.?249 + O.o99pe \ß J

h (Ρ) = ->Ι.159+αί49·ρβ~ ' P+ 8.99 Ρ ($)

40+F* V J

In order to extend the validity range of the pressure, we have been, obliged to give up the dependence on the pres­sure as Η , previously used. In fact whilst in the range 30 ata ¿P 4100 ata the turnout critical heat flux is well represented by means of a monotonously decreasing function

of the pressure as Η , extending che validity range at

pressures lower than 30 ata, an inversion of the dependence

on the pressure appears. For this reason xe have given up

the representation by means of a quantity having a physical

meaning, adopting two analytic functions of the pressure.

The high quality correlation has heen modified with regards

to the dependence on G and D in order to simplify its use

and have an analytic form of eqs. (2) as simple as possible.

φ.

•i

Pa72 a t a G=S219 gr /cm s e c

D=0.918 cm L=139.9 cm

300

predicted burnout heat flux

100

0.2 ƒ 04 predicted exit quali cy fig.. 1

TO

50 100

f i g . 2

h(P)

50 100

f i g . 3

II

The main aims that we want to attain in the extension of the correlation are the following:

a) To obtain an expression valid in a large range of varia­bility.

b) To arrive at a simple analytic form, which allows us a quick prediction.

In order to obtain this simplicity we have preferred to give up the accuracy, avoiding the introduction of more corrective factors or more correlations which are valid only in a restricted range, even it they have an higher accuracy. The use of some corrective factors has been adopted only for the interpretation of burnout data external to the validity range: most probably these data are referred to a different motion path.

12

3. RANGE OF VALIDITY

The correlation (2) is applicable in the following range

of validity:

0.3 cm

20 cm

2.7 ata

10 gr/cm sec

Λ

¿ è

4

• ¿

<

D

L

Ρ

G

¿ 4

^

4

χ. <£

m χ« <

3.75 cm

600 cm

140 ata

600 gr/i

0

1

"♦V?, The restriction Χ. ¿ 0 has been laid in order to avoid

the dependence on L and on the inlet conditions which is

a characteristic of many data with X. > 0. The upper restri­

ctions of D, L, P, are not effective restrictions as they

have been introduced only for the lack of comparisons with

the experimental data in this range. The restiction on Xe

is equivalent to exclude the data with X ^0.5: this restriction

has been introduced as for little X a different type of

motion appears. Nevertheless, as we will show afterwords,,

the correlation gives good predictions also at Χβ*>/ 0 for

nearly all the experimental data found in the literature.

The lower restrictions of P, L, D, and the restrictions

of G, on the contrary, are effective restrictions of the

correlation. We must also observe that for G ¿30 gr/cm sec.

it is necessary to use only the second eq. (2), as the first

one may give an outlet quality greater than 1.

13

4. COMPARISON WITH THE EXPERIMENTAL DATA

a) Source of data.

The correlation has been compared with as great a number

as possible of experimental data ( A ^ 5000) of which 4500

are internal to the validity range. Most" of them have been

5

derived from Macbeth , with the exclusion of the data ha­

ving Xe < 0, Ρ Λ/ 1 ata and advised as inconsistent. Besides

we have also considered the data assembled by Becker, coming

from Aktiebolagt.Columbia, tfinfrith and Harwell laboratories, 9

in references 6­r8, and the data of laboratories of Sorin 10

ana M.A.N.

From these data we have removed 10 data which do not satisfy

the heat balance equation­probably for an error of transcrip­

tion, and 9 data which crive an outlet quality greater than 1,

even if satisfy theheat balance equation. All the data co­

ming from reference 5 have been quoted as Macbeth data,

whilst we have kept the name of the laooratory which they

corne from, for the other ones.

For reason of clarity the groups of data have been arranged

as in table 1. For every group the validity range of the

most important parameters has been quoted also. The number

of the data examined is lower than the total number contained

in the various references, as some data of reference 6­r10

were still present in reference 5· Notwithstanding our at­

tention to excluding these double data, some data have been

certainly considered twice.

b) Examination of the error.

Once the inlet conditions (P, G, Χ·η) and the channel geo­

metry (L, d) are fixed, the values of Ò and Xe are pre­

dicted by means of eq. 2 » in the way previously described.

SOURCE

Macbeth-Thorn,

t a b l e 2 - 3 - 4 - 5

t a b l e 6

t a b l e 7 - 8 - 9

t a b l e 10

t a b l e 15

t a b l e 15

t a b l e 15

t a b l e 15

B e n n e t t

PRESSURE

RANGE

7 - 5 3

70

90-126

140

4 . 5 - 3 8

3 . 7 - 4 1 . 5

2 . 4 - 4 0

6 . 4 - 3 6 . 5

71

RANGE OF

DIAMETERS

0 . 1 1 - 1 . 0 8

0 . 4 6 - 3 . 7 5

0 . 4 6 - 1 . 9 8

0 . 4 6 - 1 . 1 1

0 . 3 9

0 . 7 8

0 . 9 9

1 .

0 . 9 2 - 1 . 2 6

RANGE OF

LENGTHS

7 . 6 - 1 7 3

2 1 . 6 - 3 6 6

2 2 . 9 - 1 5 2 . 4

2 3 . 9 - 1 8 3

1 0 3 . 9 - 3 1 1 . 9

1 0 3 . 9 - 3 1 1 . 9

5 9 . 9 - 3 1 1 . 9

100-250

1 7 2 . 7 - 5 5 6 . 3

RANGE OF

MASS VELOCITY

1 . 3 - 1 0 4 3

2 . 8 - 1 3 3 7

2 . 8 - 4 1 2

3 . 8 - 7 4 7

50-191

2 2 - 1 4 1 . 5

1 4 . 4 - 2 4 1

10-251

65-584

No. OF EXPTS

ORIGINAL

315

603

198

396

162

247

539

628

174

No. OF EXPTS

ACTUAL

232

102

148

194

162

247

516

627

174

1

2

3

4

5

6

7

8

9

TABLE 1

SOURCE

tfinfrith

tfinfrith

Columbia

Becker

Becker

Becker

MAN

SORIN

t o t a l

PRESSURE

RANGE

70

70

5 2 . 7 - 7 0

2 8 - 9 6

2 . 7 - 2 2 . 7

70

3 2 . 5 - 1 4 1 . 5

8 0 . 7 - 1 4 5

RANGE OF

DIAMETERS

0 . 9 5 - 1 . 1 8

0 . 5 6 - 1 . 1 5

0 . 6 2 - 3 . 7 5

0 . 3 9 - 2 . 4 9

0 . 6 - 1 . 3 1

1 .

0 . 7 - 1 . 5 0

1 . 0 2 - 1 . 7 1

RANGE OF

LENGTHS

8 4 . 1 - 3 6 6

2 1 . 6 - 2 0 0 . 7

6 1 - 1 9 7 . 2

4 0 - 3 5 0

4 0 - 3 0 0

500

2 8 - 9 8

7 8 . 5 - 1 3 1 . 7

RANGE OF

MASS VELOCITY

1 9 9 - 4 1 1 . 5

4 0 . 5 - 4 4 0

6 4 - 5 5 8 . 6

1 4 . 4 - 5 0 0

1 0 . 2 - 2 6 4

7 2 . 5 - 3 0 5

9 3 . 8 - 3 6 1 . 5

4 8 - 3 1 4

No. OF EXPTS.

ORIGINAL

136

303

196

928

312

10

261

153

5561

No. OF EXPTS.

ACTUAL

132

284

167

917

311

10

230

98

4551

10

11

12

13

14

15

16

17

H

TABLE 1 (CONT.)

16

The error percent is determined with the following equation:

C; m S m 7 Φ° .100 where φ is the experimental value CPm ,

of the critical^burnout heat flux, whilst φ is the calcu­

lated one. The mean error £ and the mean quadratic error O*

have been calculated as £ · ^ Síí δ*« ƒ - í í

η V η

In table 2 there is the total number of data, the number

of data having an error less than 1%, the number of

data having an error between 1% and 2% and so on.

The results are Summarized in table 3, and in fig. 4 are

compared with the normal distribution of Gauss.

Out of 4551 experimental data we have a mean er­

ror £ » ­ 0.124, a mean quadratic error O" = 7.26% and the

85.5/4 of the data exhibits an error less than 10%.

c) The error distribution versus tae various parameters.

For the sake of semplicity,the dependence of the errors on the

various parameters has been examined only for a restricted

range of the data. The error distribution versus D, G, L,

X. , for Ρ = 70 ata and 0.2 <X0< 0.3 is given in figs.

5 * 1 2 . Examining the diagrams in which the data of all the

laboratories are reported, it appears that the systematic error is

negligible, whilst the data of a single laDoratory exhibits

(figs. 9­Í­12) a separation of the errors: for instance at

Ρ = 70 ata, 0.2*Xo<0.3 Becker's data are overestimated

whilst Man's data are underestimated. For this reason it

is possible to improve the error of a single laboratory ap­

preciably, but it is very difficult to improve the accuracy

of the predictions on the whole, if we give the same weight

to the various laboratories. For example a group of 132 data

of tfinfrith, which has at present a mean quadratic error

equal to 7.75%, gave an error Ç equal to 6% with a correla­

tion previously checked.

17

Fig. 13 gives the error distribution versus P, P<70 ata and

0.2¿X9<0.3, figs 14­f"15 give the error distribution versus

P, P O O ata and 0.7^Χβ<0·8. Fig. 16 gives the error di­

stribution versus P, P>70 ata and 0.2­<Xo< 0.3. Fig. 17

gives the error distribution versus β, at Ρ » 140 ata and 0.2< X0<

0.3.Obviously it is questionable to consider only the data

with O.2^X0<O.3 as this can point out systematic errors

which are not present out of the all of data in general when

th<° critical heat flux is not a linear function of X# and,

on the contrary, hides some errors which are present. The only

justification for this way of proceeding, is the difficultv

in handling a great number of data* and the lack of clearness

in a diagram which contains many points.

The form of representation adopted makes the comparisons

amongst the various groups of data easier.

d) Examination of the errors in the single groups of data.

In table 4 we have reported the mean error £ , the mean

quadratic error 5 for every group of data, following the

subdivision of table 1. Figs. 18 4*31 give the values of the

fluxes calculated Versus the experimental ones in a biloga­

rithmic scale. In table 4 one can see that few groups have

a mean quadratic error higher than 10%. Sometimes this er­

ror is so high in owing to the presence of few data having

a strong shifting from the predictions. For instance 94 data

over 98 on the whole of the Sorin laboratory are predicted

with a mean quadratic error 0" equal to 8.7%, whilst the

remaining ones exhiuit errors equal to 25%, 27%, 47/¿, 51 >>.

18

TABLE 2

0 4 i< 1

Κ ί 4 2

2< ε¿3

3 4 f ¿ 4

4 4 £ 4 5

5 * é ¿ 6

6 4 £ 4 7

7 4 6 4 8

8 4 ë 4, 9

9< £ < 1 0

1 0 4 6 4 11

^^ <£<^2

1 2 4 6 4 13

1 3 4 6 4 1 4

1 4 4 € 4 1 5

1 5 * * ¿ 16

1 6 < 6 4 17

17 4 Í 4 18

18 4 É 4 19

19 4 6 4 20

204 64 21

21 4 ¿4 22

2 2 4 6 4 23

2 3 4 * 4 24

2 4 4 6 4 25

304

262

249

229

204

167

133

96

90

94

79

68

67

22

22

24

20

10

13

8

7

9

6

3

1

6.68%

6.20%

5.47%

5.03%

4.48%

3.67%

2.92%

2.11%

1.98%

2.07%

1.74%

1.49%

1.47%

0.48%

0.48%

0.53%

0.44%

0.22%

0.29%

0.18%

0.15%

0.20%

0.13

0.07%

0.02%

- 1 4 6 4 0

- 2 4 f 4 - 1

- 3 4 Í 4 - 2

- 4 < f 4 - 3

- 5 4 6 4 - 4

- 6 4 6 4 ^ 5

- 7 4 €4 - 6

- 8 4 É 4 - 7

- 9 4 6 4 - 8

- 1 0 4 6 4 - 9

- 1 1 4 6 4 - 1 0

- 1 2 4 64 -11

-13 4 6 4 - 1 2

- 1 4 4 6 4 - 1 3

- 1 5 4 6 4 -14

- 1 6 4 6 4 -15

- 1 7 4 6 4 -16

-18 4 f 4 - 1 7

- 1 9 < £ 4 _ 1 8

- 2 0 4 6 4 - 1 9

-21 4 6 4 - 2 0

-22 4 64 -21

- 2 3 4 6 4 -22

- 2 4 ¿ 6 < -23

- 2 5 4 6 4 -24

295

286

288

289

252

191

145

133

100

66

57

51

39

27

10

18

13

8

12

9

6

4

5

8

4

6.48%

6.28%

6.33%

6.35%

5.54%

4.20%

3.19%

2.92%

2.20%

1.45%

1.25%

1.12%

0.86%

0.59%

0.22%

0.40%

0.29%

0.18%

0.26%

0.20%

0.13%

0.09%

0.11%

0.18%

0.09%

19

TABLE 3

RANGE OF ζ

ERROR

- 5 4 6 4 5

- 1 0 4 6 4 1 0

- 1 5 <ί< 15

- 2 0 4 ί< 20

- 2 5 4 6 4 2 5

No. OF EXPTS.

PREDICTED

2678

3893

4335

4470

4523

ΡERC. OF TOTAL

EXPTS. DATA

58.84%

85.54%

92.25%

98.22%

99.38%

20

t%

-20 -15 -10 -5

f ig . 4

20

10

-10

-20

|100 *

f i g . 5

Bennet t ( 9 ) + Columbia(42) O Wlnfr i th [AO) Δ tfinfrith (44) ro M

20

10

* ! 4-

A +

Ä +

Δ

4*100 * 300'

:

I s +

500

-10

t ι

-20 f ig . 6

20

10

Δ £ +·

■ΟΔΔ

V t • ·

αΓ · · · Sí ft°8·^ ° ^

0.5 +

-X in

O o

8

, ° 8

-10

ο ο

20

20

f i g . 7

• Bennet t (9)+Columbia(l2)o tfinf r i t h (ΙΟ)Δ Vinfr i th (Ί4) ro ro

10

-10

ft i

0.5< 1.5

+ +■

-f 2.5 -F D

-20 f ig. 8

20

10

- 1 0

!IÛOJ - * -

#

300 Α. ji

ι I ΐ *

500

20

20

f i g . 9

lMacbeth(2)* MAN(16)ZBecker(13) ro

10

-10

^ i-i 200

Î ζ ζ

i î 400

k

-20 f ig . 10

15

L * *

Jk- 0.2 0.4 0.6 -Xin ' ι

- 5

-15

* ι '

ΐ

ι ι ι* ζ ζ

f i g . 11

I Macbeth (2) * MAN (16) "Ζ Becker (4 3 )

ζ ζ ζ ζ ζ ζ

ro -ρ»

15

- 5

-15

0.5 Ι

* β» je Ι* f i!

i» * *

1.5

*

2.5

r D

f ig . 12

15

5

- 5

-15

o

<*> ° * * v V.!

10 30¡

§ f i g . 13

• Macbeth ( 4 )ΔΜΑΝ(16)ο Becker(14-) *Macbeth( 7

· ·

t t #

) zBecker(4 3 )

% ? 501

1 Macbeth( 8 )

Ρ

15

- 5

-15

o

8

10* ♦ V * * * o° * % 30 50 *> **fe, — ^ # ¿ H ^ OD * O o 0 Of * * * *

f ig . 14

° * «S

ro

5>

1 5 ¿Macbeth( 5 ) Z B e c k e r ( 4 3 ) *Macbeth( 6 ) I Macbeth( 8 )

ζ

<* lb ™ \¿, Ι ι ·* ZZZI ,| il ,| z

i ef ff 'li " · I t i ' ι '* f? 1 ^ ^ * Δ Δ* « " h * * * ' *

ι ,»Λ * Α Λ Δ Δ Δ ^ Δ * z z z

* f i g . 15

Γ . ι _ Δ . . Δ» . « * * » * ΑΑ - ζ * ζ

i « tl

* *ΜΑΝ (46)vsorinf l?)oMacbeth(3) ZBecker (43)

15f I

t i* α> ° o

co o o

-8 . · -ΗΒΓΛΡ * w

o v

f 90? ° 110 *» W-I30 - 5| v ■ v * >° 0 s,

^ v * * o 8

V

V v

v V

-15 f ig . 16

ζ

IO

xMacbeth(4)*MAN(i6)o s o r i n g )

15

o o

X X

- 5

-15

χ x

k100 200 « «

ro

o

χ \ X

f i g . 17

28

TABLE 4

REF.ACCORDING

TABLE 1

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

TOTAL

No.OF EXPTS.

232

102

148

194

162

247

516

627

174

132

284

167

917

311

10

230

98

4551

MEAN DEVIATION

%

7 .82

- 0 . 8 8 4

0 . 4 4 3

- 0 . 9 3 2

- 3 . 6 8

- 5 . 2 4

3 .72

- 2 . 3 2

- 2 . 4 9

- 4 . 4 5

4 . 7 6

- 2 . 0 4

- 0 . 6 9 2

- 0 . 1 6 8

- 7 . 2

3 .197

- 7 . 3 2

- 0 . 1 2 5

RMS ERROR

%

12.07

8.51

5.79

10.08

6.82

10.49

6.76

4.72

6.52

7.75

9.16

6.25

4.54

5.98

8.44

7.24

11.76

7.26

29

10 5 -

7.oa r

s.oo

«t.oo 3.G0

3.00

Z.50

2.03 Γ­

Ι.SO -

10 Ζ

7.00

5.00

«.90 3.ςο '

3.00

Z.SO

2.03

Í.SO . !

10 ι

Ci li.

N i t O

o

* j

. O l

O

u>

o o

o i d

FOL

fig. 18

10 9 r

30

7.00

■s.oo

1.00

3.50

3.00

2 . »

2.00

i.50

10 2

7.00

S.OO

4.00

3,50

3.00

Ζ.ΐΟ

2.00

l . S O . »

10 ι

hj »s; u> ω ·*.

o o u W W ' • » O O Γ)

POL

fig.19

31

10 9

10 z -

Fig.20

10 9

7.00

S.00

32

1.00 3.30 3.00 2.S0

2.C0

l.SO

10 2

7.00

5.00

1.00 9.5P 3.00

Ζ .50

Z.CO

E iL·

l .SO - ·

10 ι o o η o r»

FOL

u w « Q l i Γ3 ca o * *

O

fig.21

33

10 3

7.00

t.OO 3.S0

3.00

2.S0

2.09

l.SO

E u. 10 2

fig.22

34

10 9

7.00

5.00 '

«.oc

3.S0

3.00

2.50

2.S3

l.SO

10 e

7.00

s.oo

* .03

3.50

3.00

2.50

2.03

l.SO J»

8

10 ι ι o o o

—i—ι—r—

tí u ^ 'n ¿n ò υ o r>

O

POL

fig. 23

35

10 3

7.00

S.00

1.00 3.50

3.00

2.50

2 . CO

1.50

10 2

7.00

5.00

1.00 3.50

3.03 Î;

2.50

O u.

<j w -« 1« CO

f

w k O O

1 1

3 1

o o

• 1

FOL

f'rg.24

36

10 3

7.00

5.00

1.00

3.50

3-00

2.50

2.03

1.50

102

7.00 -

6.00 -

1.00 ■

3.50 r

3.00

2.60

10

. . . O l/t O

α

S —τ

-

FOL

frg.25

37

10 3

7.0O

5.00

1.00

3.50

3.00

2.50

2.00

1.50

10 2

7.00

5.00

1,00

3.50

3.03 ;

2.50

a:

11

POL

fig.26

38

10 9

7.00

5.00

1.00

J.50

3.00

2.50

2.C0

l.SO

10 2

7.00

5.00

1.00

3.50

3.00

2.SO

2.C0 f

ι > « I

. .50 ï-

12

3 — ί ­

ο o -ι—r-

8 W -c vi Ci

FOL

fig.27

39

10 9

/.OC

5.00

1.93

3.50

3.00

¿.■Vt

Z.C3

l.SO ■

10 2

7 . « ■

'-.00 ■

1.93 ■

i.5Q ■

3.00 -

2.50

2.C3 h

l.SO φ

10 1

E u

13

Ν» ta UÌ Λ . . . . yi -3 t,. o

O O O '■ 'a

—r- — » —

* . i j

FOL

fig.28

is 40

14 10 9

7.00

S.00

H.OO

3.50

3.00

2.50

2.00

l .SO ë

10 ζ

7.00

5.00

1.00

3.50

3.00

_ . Οι

o I

FOL

ta

• Q C]

1

. tn O

1

t *

3

»

tf rfr

• * v/* O

O o

%fi • s 1

« i

. 8 1

o ta

\

fig.29

41

16 10 9

7.00

5.00

1.03

3.50

3.00

Z.SO

2 . CO

1.50

10 2

7.00 -

5.00 -

1.00

3 .50

3.00

Ζ. 50

Ζ.03

1.50

l O ι

i\J 'S. W U' .*

O O f >

V tv t.' Λ

FOL

fig.30

1000

42

17

FOM

100

100 FOL 1000

fig.3i

43

5. EXAMINATION OF THE DATA JUICH ARE EXTERNAL TO THE VALIDITY RANGE

There are 576 data excluded from the previous examination, as external to the validity range. These data have been subdivided into four groups according to the pressure. Such subdivision has oeen introduced in order to point out if there is a coupling amongst the pressure and the parame ters used time by time. In the same table ve have also re ported the results obtained by the examination of these da­ta by means of the coxrelation

TABLE 5

Runs 0"

Ρ 70 ata 85 16 P= 70 ata 169 11.27 80ata <Ρ < 130 ata 115 14.35 P=140 ata 216 15.41

In the complex of the data excluded some data are present wich are characterized by very different condition,for instance!

D L P G Xin φοπι Xom

11.9 0.824 526.7 0.012

where the specific mass flow rate G changes from 1.4 gr/cm sec 2 to 1043.3 gr/cm sec.

tfe did not think it possible to predict also these data with our correlation .In fact it is probable that at such extreme conditions a different motion path will raise

0.46

0.57

23.9 62.5

7

32.9 1.4

1043.3 -0 .054 -0 .116

44

and different relation between the critical heat flux and

the various parameters will be set up. In any case the 576

data, external to the validity range, have been compared with

the predictions of the correlation. The shafting has been

examined by collecting the data in accordance with the rea­

sons of the exclusion: G<10, G >600, D<£0.3, L<^20, X0<

As some data are external to the validity range for more than

a parameter, we have established an order of precedence first

collecting the data excluded for G, and then the data exclu­

ded for D, for L and for Xe.

G>600

In fig.J2 we have reported the data with G>600 (33 data):

for values of G so high there are very low outlet qua­

lities, so that many of chese data are excluded also for X0

which is less than 1/(1 ♦ **/γ„ )· The difference amongst the

flux experimentally measured and the flux predicted by the

correlation is strongly positive, except for three data.

A very simple correction may be introduced by multiplying

the critical heat flux, calculated by means of eq. 2, by

the corrective factor 1.15. In sucn a way the mean quadra­

tic error changes from 19.2% to 12.35/É, obviously the great

value of the error is owing to the presence of the tree da­

ta with strongly negative errors.

p

G O O gr/cm sec.

2 The 78 data with G<10 gr/cm sec. are reported also in

fig. 32,. Also in this case the error of the predictions

exhibits a constant sign and most of the data is overesti­

mated, indipendent of the pressure. As we have found no de­

pendence of the error on some parameters, we have tnought

**H

45

it was sufficient to multiply the predicted values by a

constant. Putting φ ffi*fo)"0.9Ó .the mean quadratic error

C changes f rom 14.1% to 7.1%

L<20 cm, D< 0.3 cm

The data ^ith L<20 cm have also D<0.3 cm. The errors

of these 134 data are given in fig.JJ versus X. in order

to have a better separation. Some data, indicated with (·)

in fig.JJ have also G O O . The corrective factor introdu­

ced, 0.9 as a multiplying constant, changes the mean qua­

dratic error (J from 14.2% to 6.25%.

X 0 < 1/(1 + $ / ^ )

The greatest number of data external to the validity range

consists of the data with X0< 1/(1 + *&/$· )· θ Λ the whole

there are 437 data for a large range of geometrical parame­

ters and inlet conditions. Fig. J4 gives, versus G, the data

at P=70 ata, 0.01<X0< 0.03. In fig.J5 always versus

G the data at P=140 ata and 0.08«¿ X0< 1/(1 + ?e/^« ) are

reported. From these two figures it results that the error

of the predictions depends on G. The correlation, applied

to the data with Χ0<'ί/|Ί+#)overestimates the critical heat 2 flux for G ̂ 300 gr/cm sec, and underestimates the 2 critical heat flux for GJ5 300 gr/cm sec. Such different

dependence on G, for very lo*/ outlet quality, has been already considered by us in reference (2), (4)· An attempt to correct it has been made multiplying the critical heat

46

flux predicted by correlation by the corrective factor 0 15

η = 0.425 G .In figs. 36 and 37, we have reported the errors for the same points of figs. J4 andJ5-, after the introduction of the corrective factor. The mean quadratic error changes from 13.85% to 9.9%. In all the cases considered, when some corrective factors are introduced, it is necessary to calculate the outlet quality again.

20

10

-10

-20

h

I

à' *ιο

1 ** i·} ¿

Δ

? r i •

· ·

100

Ät

# o

o

o o

1000 ft

o

- 3

f i g . 32

-5

- 15

- 2 5

• • ·

0.2

( · ) ( · )

0.4

<·> C·)

0.6 - X i n

-Ρ» OD

f i g . 33

-15

f i g . 34

8

15

- 5

100

8

8 o 88

-o θ -

8

o o o o o

300

o o

°o 8

θ

%

500 -t*

15

- 5

-15

100 200 . ·300 · - I — r 500

o

• * . . · # * t / " ·

% ·

f ig . 35

20

10

-10

20

\ %

100

-

8

% o

0 . ö—■

8

8

8̂-ώ H

300 500 *

8

f i g . 36

20

10

-10

-20

% · ' · ·

100 ¿^Λ ι» ·

300 500

: · « · · .

f ig . 37

53

NOMENCLATURE

D diameter" cm

G specific mass flowrate gr/cm sec

H latent heat of vaporization joule/gr

L heated length cm

Ρ pressure ata

X. inlet quality in ^ J

X outlet quality

X volume flowrate quality

Ρ density gr/cm

φ critical heat flux watt/cm

Subscripts

g steam

1 liquid

54

BIBLIOGRAPHY

(1) - G.C.CLERICI-S.GARRIBA-R.SALA-A.TOZZI MA catalogue of burnout correlations for forced convection in the quality region·· EUR 3300.e - december 1966.

(2) - G.C.CLERICI-S.GARRIBA-R.SALA-A.TOZZI "Studies on linear correlations.Part 2M

To be printed as EUR report (3) - G.C.CLERICI-S.GARRIBA-R.SALA-A.TOZZI

"Alternative forms for some burnout correlations·· ENERGIA NUCLEARE -Volume 14 May 1967 Number 5

(4) - G.C.CLERICI-S.GARRIBA-R.SALA-A.TOZZI "Comparison between Beker correlation and some alternative linear forms" ENERGIA NUCLEARE -Volume 14 June 1967 Number 6

(5) - B.THOMPSON-R.V.MACBETH "A compilation of world data with accurate correlations" AEEW-R 356 1964.

(6) - K.M.BECKER"An analytical and experimental study of burnout conditions in vertical round tubes" AE-RTL-778 January 1965.

(7) - K.M.BECKER"A comparison of two burnout correlations" AE-RTL-799 August 1965.

(8) - K.M.BECKER»some remarks on correlating the Harwell round tube burnout data"AE-RTL-855 May 1966.

55

(9) ­ F.BIANCONE­A.CAMPANILE­G.GALIMI­M.GOFFI

"Forced convection burnout and hydrodynamic

instability experiments for water at high

pressure.Part 1" Rapporto τ/363 Marzo 1965. EUR 2^90. e.

(lO)­F.MAYINGER­O.SCHAD­E.WEISS "Investigation

into the critical heat flux in boiling"

Report N°090301 Contract N°05761RDD q.d.N°III.1.8

May 1966.

¿UR 33V?. e

¡m Κ^ΓιΓ

ifcjfi rt

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