HEAT TRANSFER AND PRESSURE DROP MEASUREMENT IN
MINICHANNELS
Jiří HEJČÍK, Mi osla JÍCHAx
Abs ac : This pape desc ibes he sui able echniques o he hea ans e and
p essu e d op measu emen in smoo h ubula channels wi h he in e nal diame e
less han 5 mm. The i s expe imen al da a a e men ioned and hei e alua ion is
p esen ed.
1. INTRODUCTION
The e o o achie e g ea e alues o hea ans e coe icien has accompanied design
enginee s o hea ing equipmen o almos 100 yea s [1]. P obably he easies way o
inc easing i is o dec ease he channel diame e (a leas acco ding o he classical
co ela ions). Al hough his me hod seems o be e y simple, i s applica ion is
echnologically e y challenging, hus his me hod has only been used in special
applica ions (e.g. mili a y and ai c a indus y) e en hough o a long ime. The wide
use o i occu s only in he las 20 yea s because o he g owing in e es in highly
e icien and compac hea exchange s; mainly because o he need o cool a sh inking
and mo e powe ul elec onics. The p oblem o hea ans e in channels o such a small
diame e has g own in impo ance and some di e en ca ego ies we e es ablished du ing
he las decade. P obably he mos applied classi ica ion was de ined in 2002 by
Kandlika [2] who di ided he channels in o 3 ca ego ies. The i s ca ego y is called a
con en ional channel and con ains channels wi h hyd aulic diame e s g ea e han 3 mm.
Nex ca ego y called minichannels con ains hose wi h hyd aulic diame e s diame e in
he ange 200 μm - 3 mm, and inally he las ca ego y is called mic ochannels whe e he
channels ange om 10 μm o 200 μm.
The minichannel ca ego y is e y in e es ing mainly o mechanical enginee s because i
allows designing small and e ec i e hea exchange s which a e no hype sensi i e o he
pu i y o he lowing media. Howe e hese hea exchange s seem o be con enien o
lo s o applica ions, he ac ha he e a e no cu en ly a ailable eliable p ocedu es o
hei design p e en s hei u ilisa ion. The p oblem wi h a minichannel exchange design
is a ibu ed o he hea ans e a e p edic ion. Al hough Kandlika , e al. [3] s a ed ha
he co ela ions o con en ional channels could be used, he esea ch done on
minichannels is no so clea .
x Ing. Jiří Hejčík, Ph.D.; Ene gy Ins i u e, Facul y o Mechanical enginee ing, B no Uni e si y o
Technology, Technická 2896/2, 616 69 B no; email: hejcik@ me. u b .cz
p o . Ing. Mi osla Jícha, CSc.; Ene gy Ins i u e, Facul y o Mechanical enginee ing, B no Uni e si y
o Technology, Technická 2896/2, 616 69 B no; email: [email p o ec ed]u b .cz
EPJ Web o Con e ences , 0101 (2012)
DOI: 10.1051/epjcon /2012250101
© Owned by he au ho s, published by EDP Sciences, 2012
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pe mi s un es ic ed use, dis ibu ion, and ep oduc ion in any medium, p o ided he o iginal wo k is p ope ly ci ed.
A icle a ailable a h p://www.epj-con e ences.o g o h p://dx.doi.o g/10.1051/epjcon /20122501021
2. TEST RIG
A minichannel es ig was buil o p o e he possibili y o he con en ional channel
co ela ions applica ion o ubula channels wi h inne diame e in ange o 0.25 – 5 mm.
Comp essed ai was used as a es medium. I is s o ed in an ai -p essu e ank and i
lows h ough he p essu e educing al e and he hea e o he p essu e/ empe a u e
heade , whe e a empe a u e senso is moun ed as well as a p essu e po o p essu e
d op measu emen . A e ha he ai goes h ough a es sec ion, whe e a es ed
minichannel is moun ed and cooled by wa e o an ice-wa e mix u e. The nex
empe a u e/p essu e heade is loca ed a e he es sec ion o acili a e he
empe a u e and p essu e measu emen . The comp essed ai mass low measu emen
and egula ion is loca ed behind his head and i e mina ing he comp essed ai low
pa h. The schema ic iew o he ig is shown in he igu e 1.
Figu e 1 Tes ig
Thin wall s ainless s eel ubes we e used as es channels in his es ig. They we e
inse ed in o he es sec ion and joined o he p essu e/ empe a u e heade s. Hence
h ee addi ional empe a u e senso s we e s icked on he minichannel su ace o
measu e he wall empe a u e nea he heade s and in he middle o he minichannel.
The es sec ion was hen illed up wi h wa e o ice-wa e mix u e, so ha he
minichannel was ully subme ged and he es ig was p epa ed o he hea ans e
coe icien o p essu e d op measu emen .
3. HEAT TRANSFER COEFFICIENT MEASUREMENT
The equi ed ai p essu e le el and mass low a e was p ese by he p essu e- educing
al e and he needle al e. Nex , he hea e was u ned on and he sys em hea ed up o
a couple o minu es. A e ha he p essu e le el and mass low a e was uned up o
he equi ed alue and he measu emen s a ed. Tempe a u es, p essu e d op and mass
low a e we e he s o ed da a collec ed e e y second o app oxima elly 10 minu es.
Then he new mass low a e was se and he p ocedu e epea ed.
The hea ans e coe icien , h, is hen calcula ed om he s o ed da a using he
equa ion o cons an wall empe a u e hea ans e (1), which could be used due o he
negligible he mal esis ance o channel walls.
݄ൌെሶή
గήή ή݈݊൬்ೢି்್ǡೀೆ
்ೢି்್ǡಿ ൰ [Wm-2K-1] (1)
whe e ݉ሶ [kg/s] - ai mass low a e, cp [J/kg/K] – cons an p essu e speci ic hea o ai ,
D [m] – channel diame e , L [m] – channel leng h, Tw [K] – wall empe a u e, Tb,IN,
Tb,OUT [K] – comp essed ai inle /ou le empe a u e o/ om es sec ion
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As can be seen in equa ion 1, he hea ans e coe icien depends on he empe a u e
di e ence be ween ai and he wall. I means ha he exac empe a u e measu emen
is c ucial o he used me hod, which could be a p oblem in he case o small empe a u e
di e ences, he e o e he inle empe a u e o comp essed ai has o be as high as
possible o dec ease he unce ain y o he hea ans e coe icien measu emen .
4. PRESSURE DROP MEASUREMENT
The e was no hea e used o he p essu e d op measu emen . Only he equi ed ai
mass low a e (Reynolds numbe ) was se and he p essu e d op ead. The p oblem was
ha p essu e d op measu ed was no he one o he minichannel bu he one o he
comp essed ai lowpa h om one p essu e/ empe e u e heade o he nex one. I
means i also includes some local p essu e d ops. Due o his ano he p essu e d op
measu emen wi h a sho ened minichannel had o be done o elimina e he local
p essu e d op e ec . The minichannel ic ion ac o was hen calcula ed om he
di e ence o he measu ed p essu e d ops (long and sho minichannel) and he leng h o
he cu ed pa o he minichannel.
5. RESULTS
Fi s hea ans e coe icien measu emen wi h 4.8 mm in e nal diame e smoo h
ubula channel was pe o med. The channel wall hickness was 0.2 mm and he channel
leng h was 538 mm. This “con en ional” size channel was made o AISI 304 s ainless
s eel and ins alled o he es ig o p o e hea ans e coe icien measu emen s. The
comp essed ai gauge p essu e was se o 2 ba a he inle side o he channel. The ai
was hea ed up o app ox. 80 °C and he es sec ion was illed up wi h an ice-wa e
mix u e. The ai low a e a ied in be ween 5 and 55 Nl/min o each he Reynolds
numbe alues om 1500 o 15000.
Al hough he cons an wall empe a u e condi ion was supposed du ing he p elimina y
s age o expe imen s, he i s measu emen showed ha we we e no able o mee ha
condi ion. The al e na i e me hod (equa ion 2) based on he loga i hmic mean
empe a u e di e ence was used o calcula e he hea ans e coe icien ins ead o
equa ion (1).
݄ൌሶή
గήή ή݈݊൬்್ǡೀೆି்ೢǡೀೆ
்್ǡಿି்ೢǡಿ ൰ή ்್ǡಿି்್ǡೀೆ
൫்್ǡೀೆି்ೢǡೀೆ൯ି൫்್ǡಿି்ೢǡಿ൯ [Wm-2K-1] (2)
Resul s ob ained using equa ion (2) we e ans o med o he non-dimensional Nussel
numbe and compa ed wi h Gnielinski’s co ela ion which is commonly used o in ube
hea ans e coe icien calcula ion, see igu e 2. The p essu e d op measu emen has
no been inished ye .
EFM11
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Figu e 2 Measu ed da a
6. DISCUSION
Measu ed da a a e in a good ag eemen wi h he Gnielinski’s co ela ion o he Reynolds
Numbe be ween 7000 and 15000 ( igu e 2), whe e he ela i e di e ence be ween
measu ed and calcula ed da a is lowe han 8 %. The e is a big di e ence in measu ed
and calcula ed alues o he Reynolds numbe s lowe han 4000 hough, whe e he
ela i e di e ence almos eaches 40 %. I is p obably caused by low ansi ion om
lamina o u bulen low, bu he e is no physical e idence o i .
The selec ed me hod and measu emen echniques seems o be sui able o he hea
ans e coe icien measu emen , as could be seen om he measu ed and calcula ed
da a compa ison in igu e 2. Bu he e a e s ill some hings o imp o e, mainly in he
ield o da a p ocessing, whe e some di e en echniques e.g. Wilson plo me hod should
be used o he hea ans e coe icien calcula ion.
7. ACKNOWLEDGEMENT
The au ho s would like o g ea ly acknowledge he inancial suppo ecei ed om he
Czech Science Founda ion (unde he p ojec No. P101/11/P538) and om he Facul y o
Mechanical Enginee ing, B no Uni e si y o Technology (p ojec No. FSI-S-11-6).
8. REFERENCES
[1] S einke, Ma k E.; Kandlika , Sa ish G.: Single-phase hea ans e enhancemen
echniques in mic ochannel and minichannel lows. In . P oceedings o he second
in e na ional con e ence on mic ochannels and minichannels, June 17-19, 2004.
Roches e , USA : ASME, 2004. pp. 141-148. ICMM2004-2328.
[2] Kandlika , Sa ish G.: Fundamen al issues ela ed o low boiling in minichannels and
mic ochannels. Expe imen al The mal and Fluid Science. 2002, Vol. 26, Issue 2-4,
pp. 389-407. ISSN 08941777.
[3] Kandlika , Sa ish G., e al.: Hea ans e and luid low in minichannels and
mic ochannels. 1s ed. Ams e dam, Ne he lands : Else ie , 2006. 450 p. ISBN 978-
0-08-044527-4.
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