https://www.htsj.or.jp/journals/2319.html

115.0

120.0

128.0

121.5

142.5

165.0

Heat transfer coefficient (kW/m2K)

Tsolid (C)

Tsolid (C)

10

600 kW/m

1500 kW/m

600 kW/m2

1000 kW/m2
1200 kW/m2

300 kW/m2

101

Burn out

100 kW/m2

1500 kW/m2

50 kW/m2

Measurement
Simulation
102

800 kW/m2

2

2

0

10

20
T (K)

30

40

50

0.6MW/m2
1.5MW/m2(a) 0.2 MW/m 2

Dry-out
Microlayer

3 mm(b) 0.6 MW/m 2

Dry-out Microlayer
3 mm

20K

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Vol.62

No.258January 2023

CONTENTS
Opening-page Gravure: heat-page
Yohei SATO (Paul Scherrer Institute, Switzerland),Tomohide YABUKI (Kyushu Institute of Technology, JST PRESTO),
Yuichi MITSUTAKE (Saga University),
Ichiro UENO (Tokyo University of Science)

Opening Page

EulogyIn Memory of Dr. Enya
Keiichi KUWAHARA (Office Kuwahara, Ltd.)1

In the Memory of Dr. Shintaro Enya
Masahito OGUMA (Energy Agency Fukushima)

3

Special Issue: Progress in Boiling Heat Transfer
Preface to Progress in Boiling Heat Transfer
Tomohide YABUKI (Kyushu Institute of Technology, JST PRESTO)

6

Numerical Simulation of Boiling Heat Transfer
Yohei SATO (Paul Scherrer Institute, Switzerland)

7

Boiling Heat Transfer Mechanisms Observed by High-speed Infrared Thermometry
Tomohide YABUKI (Kyushu Institute of Technology, JST PRESTO)

13

Microbubble Emission Boiling (MEB)
Ichiro UENO (Tokyo University of Science)18

Measurement Technique and Its Application to Transient Transition Boiling Heat Transfer during
Quenching of Hot Surface
Yuichi MITSUTAKE (Saga University)

29

ReportReport on the Lecture Measurement Technology, Foundation and Application of Temperature
Measurement and Thermal Conductivity Measurement
Kimihito HATORI (Bethel), Koji NISHI (Ashikaga University),
Yoshihiro KONDO (Hitachi Academy), Kenichi P. KOBAYASHI (Meiji University),
Wataru SATO (Hitachi) and Katsuhiro KOIZUMI (Nabtesco)

CalendarAnnouncements
Note from the JHTSJ Editorial Board

35
39
40
51

In memory of Dr. Enya

Keiichi KUWAHARA (Office Kuwahara, Ltd.)e-mail:keiichi@a05.itscom.net

IHI
2019

2
7
87

1935

42

First Material Processing Test

FMPT

IHI
IHI
41

2002

FMPT

-2003
IHI
IHI
LNG

LNG
IHI

1993

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-1-

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1972

IHI

2017

8

NPO
60

2018

7

1961
2

60

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1

-2-

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In the Memory of Dr. Shintaro Enya

Masahito OGUMA (Energy Agency Fukushima)e-mail: oguma@f-open.or.jp
41

7
8

28

22

25
4

1

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J. HTSJ, Vol. 62, No. 258

OB
35
2

OB

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2

-5-

2

J. HTSJ, Vol. 62, No. 258

Preface to Progress in Boiling Heat Transfer

JST
Tomohide YABUKI (Kyushu Institute of Technology, JST PRESTO)
e-mail: yabuki.tomohide556@mail.kyutech.jp

100

MEB
MEMS
MEB

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J. HTSJ, Vol. 62, No. 258

Numerical Simulation of Boiling Heat Transfer

Yohei SATO (Paul Scherrer Institute, Switzerland)e-mail: yohei.sato@psi.ch1Computational Fluid Dynamics CFD simulation
Bubble shape

Interferometer
Temperature
distribution

Temperature drop due to micro-layer

1 Growing bubble (top row), microlayer formed
underneath a growing bubble detected by aninterferometer(middle

row),

and

temperature

distribution (bottom row) [3]

CFD
Critical Heat Flux CHF[1]

CFD
Navier-Stokes NS
50,000 W/m2 K

1,000

5,000 W/m2 K [2]

100

100 m
: 1
2

:

3

1 m
2
3
1
CFD

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J. HTSJ, Vol. 62, No. 258

molecular dynamics

[4]

2

(a)

(b)

Single-fluid model

1 m

CFD
mm

Volume fraction of gas
0.027
0.024
0.021
0.018
0.015
0.012
0.009
0.006

cm
mm

cm
4
/

Bubbly flow simulation using (a) single-fluid

model and (b) two-fluid model.
2

two-fluid model/Eulerian approach
4bSingle-fluid model
two-fluid

model

NS

Volume Of Fluid

Single-fluid modelTwo-fluid model / Eulerian approach
Flow, temperature and volume fraction ofliquid/vapor in bulk (>cm)[5, 6] Level-Set

Large[7-9] Phase-Field/

Liquid-vapor interface / bubbles in bulk (mm~cm)
Bubble growth, sliding and liftoff on wall (~mm)

5Microlayer (< m)Bubble nucleation on wall (~nm)

Tsat

Small

n

Molecular dynamics

2

VOF[10, 11]qv

ql

Length scale of boiling phenomena and(qv +ql)/L [kg/m2s]

corresponding simulation approach.
L [J/kg]NSsource

term
2

Time

3

Boiling off water near hydrophilic zirconium using

molecular dynamics [4]. Because of the hydrophilicity,liquid layer exists underneath vapor phase (yellow
surface).

2023

1

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J. HTSJ, Vol. 62, No. 258

20 mm
Tsat
qv

v

T n

[15]
7

n
ql

l

T

n

1.5 MW/m2
100 kW/m2

5 Heat flux calculation around the liquid-vapor
interface in a single-fluid model [6].
1.2 MW/m2
1.5 MW/m2
1
1

100 m
[16]
[12-14]

0.5 m
3100
512

Bures

[13]

9

75 m

1.3

6

Growing bubble and velocity field in nucleateboiling: (a) whole bubble, and (b-c) magnified viewsaround the micro-layer [12].

2023

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J. HTSJ, Vol. 62, No. 258

through the copper block for the saturated pool boilingsimulation with different applied heat fluxes [15].
Tsolid (C)

Tsolid (C)

115.0

121.5

128.0

115.0

121.5

128.0

102

1000 kW/m2
1200 kW/m2

800 kW/m2
600 kW/m2
300 kW/m2

101

Burn out

100 kW/m2

1500 kW/m2

50 kW/m2

600 kW/m2

100 kW/m2

Measurement
Simulation

Tsolid (C)

Tsolid (C)
115.0

121.5

128.0

120.0

142.5

100

165.0

8

10

20
T (K)

30

40

Comparison of overall heat transfer coefficient

between the experiment [17] and simulation

1200 kW/m2

7

50

.

1500 kW/m2

Bubble shapes and temperature distributions
Condition: Water at 2 bar (Tsat = 120°C), applied heat flux: 1100 kW/m2 (= 90% CHF)
Domain: 351 × 30 × 4 mm3Comparison of wall
temperature between
measurement andsimulation

350
300
250
200
150
100
50

Tfluid (° C)

Measurement
Twall (° C)

Simulation

00

Bubble collapse
TThermal plume

20
40
60
Wall superheat (K)Liquid-vapor
interface+ Temperature
field

9

Bubble nucleationand temperature drop

Around the inlet region
A

160
159
158
157
156
155
154
153
152
151
150
149
148
147
146
145
144
143
142
141
140

124
122
120
118
116
114
112
110
108
106
104
102
100
98
96
94
92
90
88
86
84
82
80

Forced convective subcooled flow boiling simulation using single-fluid model [18].

2023

1

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two-fluid model
10 a
Two-fluid modelNSNSsingle-fluid modelinterfacial forces

two-fluid modelinterfacial

forcesinterfacial heattransfer

10

interfacial force

Upward subcooled boiling flow in heated pipeusing a two-fluid model: (a) volume fraction of vapor, (b)liquid temperatureand (c) comparison between

experimentand simulation[20].

11Two-fluid model

two-fluid modelinterfacial forces

two-fluid model

UCLA

Dhir

11

hopeless task

Boiling flow simulation in a fuel assembly of a

nuclear power plant using a two-fluid model [21].

[19]
Two-fluid model
10
[20]

2023

1

- 11 -J. HTSJ, Vol. 62, No. 258

two-536-545.

fluid model[11] Badillo, A., Quantitative phase-field modeling forsingle-fluid modelboiling phenomena, Physical Review E, 86 (2012)041603.

10[12] Urbano, A., Tanguy, S., Huber, G., Colin, C., Direct
numerical simulation of nucleate boiling in microlayer regime, Int. J. Heat and Mass Trans., 123 (2018)[1] Nukiyama, S., The maximum and minimum values of1128-1137.

the heat Q transmitted from metal to boiling water[13] Bure, L., Sato, Y., On the modelling of theunder atmospheric pressure, J. Jap. Soc. Mech. Eng.,

transition between contact-line and microlayer

Int. J. Heat Mass Transfer, 37 (1934) 1419-1433.

evaporation regimes in nucleate boiling, J. Fluid

[2]

5

,

Mech., 916 (2021) A53.

, 2007.

[14] Bure, L., Sato, Y., Comprehensive simulations of[3] Jung, S., Kim, H., An experimental method toboiling with a resolved microlayer: validation andsimultaneously measure the dynamics and heatsensitivity study, J. Fluid Mech., 933 (2022) A54.

transfer associated with a single bubble during[15] Sato, Y., Niceno, B., Pool boiling simulation using

nucleate boiling on a horizontal surface, Int. J. Heatan interface tracking method: From nucleate boilingand Mass Trans., 73 (2014) 365-375.

to film boiling regime through critical heat flux, Int.

[4] Karalis, K., Zahn, D., Prasianakis, N.I., Niceno, B.,
Churakov,

S.V.,

Deciphering

theJ. Heat and Mass Trans., 125 (2018) 876-890.

molecular[16] Sato, Y., Niceno, B., A depletable micro-layer model

mechanism of water boiling at heterogeneousfor nucleate pool boiling, J. Comput. Phys., 300

interfaces, Scientific Reports, 11 (2021) 19858.

(2015) 20-52.

[5] Hardt, S., Wondra, F., Evaporation model for[17] Gaertner, R.F., Photographic study of nucleate poolinterfacial flows based on a continuum-fieldboiling on a horizontal surface, J. Heat Trans., 87

representation of the source terms, J. Comput. Phys.,(1965) 17-27.

227 (2008) 5871-5895.

[18] Sato, Y., Niceno, B., Smith, B.L., Departure from

[6] Sato, Y., Niceno, B., A sharp-interface phase change

nucleate boiling simulation based on an interface

model for a mass-conservative interface tracking

tracking method, in:method, J. Comput. Phys., 249 (2013) 127-161.

Meeting on Nuclear Reactor Thermal Hydraulics[7] Son, G., Dhir, V.K., Ramanujapu, N., Dynamics and18th International Topical(NURETH-18), Oregon, USA, 2019.

heat transfer associated with a single bubble during[19] Dhir, V.K., Mechanistic prediction of nucleate

nucleate boiling on a horizontal surface, J. Heatboiling heat transfer -Achievable or a hopeless task?,

Trans., 121 (1999) 623-631.

J. Heat Trans., 128 (2006) 1-12.

[8] Son, G., Dhir, V.K., Numerical simulation of nucleate[20] Krepper, E., Kon ar, B., Egorov, Y., CFD modellingboiling on a horizontal surface at high heat fluxes, Int.

of subcooled boilingConcept, validation and

J. Heat and Mass Trans., 51 (2008) 2566-2582.

application to fuel assembly design, Nucl. Eng. Des.,[9] Tanguy, S., Ménard, T., Berlemont, A., A level set

237 (2007) 716-731.

method for vaporizing two-phase flows, J. Comput.

[21] Lo, S., Lecture CFD-4: Eulerian multiphase flow

Phys., 221 (2007) 837-853.

model, https://www.imperial.ac.uk/media/imperial-[10] Takada, N., Tomiyama, A., Numerical simulation ofcollege/research-centres-and-groups/nuclear-isothermal and thermal two-phase flows using phase-engineering/17-CFD-4.pdf

field modeling, Int. J. Modern Phys. C, 18 (2007)

2023

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Boiling Heat Transfer Mechanisms Observed by High-speed Infrared Thermometry

JST
Tomohide YABUKI (Kyushu Institute of Technology, JST PRESTO)
e-mail: yabuki.tomohide556@mail.kyutech.jp

(3)
(4)

[1]

1

1,000fps
100 m/pixelcm[2, 3]
0.6mm

SiO2
20mm
MEMS

[4]

10mm

[5]
0.2MW/m2

2(1)
0.6MW/m2(2)100kW/(m2 K)

60kW/(m2 K)

1MW/m212023

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2

[2]

30kW/(m2 K)

3

10%
30%

Sato & Niceno
[6]

3
(a)

(b)

[2]

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35%

1.2mm

89

2

1/2~1/3

sites/cm

1.2mm

Su

[7]

10 m
1.2mm

Zupan i

[8]

[3]
2

1.2mm

89 sites/cm
589 sites/cm2
[3]

150 m
1K

1MW/m2100 sites/cm2

[9]

24

318

sites/cm2
72

4

0.6 MW/m

5
Bare
89

130 sites/cm2
20kW/(m2 K)

6

30 m
(a)

(b)
Sakashita

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6(a)
0.1~0.9MW/m(b)2

0.1 MW/m2[3]

4

0.6MW/m2

[10]
[3]
50 m

300 m

Haramura and Katto

5

[11]

[3]

7

2023

1

[3]

- 16 -J. HTSJ, Vol. 62, No. 258

Heat Mass Transf., 170 (2021) 121006.
[3] Yajima, S., Nanako, I., Miyazaki, K., Yabuki, T.,
Heat flux partitioning and macrolayer observation inpool boiling of water on a surface with artificial
nucleation sites, Int. J. Heat Mass Transf., 194(2022) 122924.
[4] Yabuki,

T.,

Nakabeppu,

O.,

Heat

transfermechanisms in isolated bubble boiling of waterobserved with MEMS sensor, Int. J. Heat Mass
Transf., 76 (2014) 286-297.
[5] Baba, S., Saito, S., Takada, N., Someya, S.
Visualization of flow boiling heat transfer using
temperature sensitive paint with high spatial andtemporal resolution, Int. J. Heat Mass Transf., 197(2022) 123367.
[6] Sato, Y., Niceno, B., Pool boiling simulation using aninterface tracking method: from nucleate boiling tofilm boiling regime through critical heat flux, Int. J.
Heat Mass Transf., 125 (2018) 876-890.
[7] Su, G.-Y., Wang, C., Zhang, L., Seong, J.H.,
Kommajosyula, R., Phillips, B., Bucci, M.,
Investigation of flow boiling heat transfer andboiling crisis on a rough surface using infrared
thermometry, Int. J. Heat Mass Transf., 160 (2020)
120134.

35%[8] Zupan i , M., Gregor i , P., Bucci, M., Wang, C.,
Aguiar, G.M., Bucci, M., The wall heat flux
partitioning during the pool boiling of water on thinmetallic foils, Appl. Therm. Eng., 200 (2022)
117638.
[9] Wang, C.H., Dhir, V.K., Effect of Surface Wettability
on Active Nucleation Site Density During Pool
Boiling of Water on a Vertical Surface, J. Heat
Transfer, 115-3 (1993) 659-669.
[10]Sakashita, H., Ono, A., Nakabayashi,

Y.,

Measurements of critical heat flux and liquidvapor
structure near the heating surface in pool boiling of
2-propanol/water mixtures, Int. J. Heat Mass Transf.,
53 (2010) 1554-1562.
[1][11]Haramura, Y., Katto, Y., A new hydrodynamic model
J. HTSJ

57-239 (2018) 20-25

of CHF applicable widely to both pool and forced[2] Tanaka, T., Miyazaki, K., Yabuki, T., Observation of

convection boiling on submerged bodies in saturated

heat transfer mechanisms in saturated pool boiling of

liquids, Int. J. Heat Mass Transf., 26-3 (1983) 389-

water by high-speed infrared thermometry, Int. J.

399.

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Microbubble Emission Boiling (MEB)

Ichiro UENO (Tokyo University of Science)e-mail: ich@rs.tus.ac.jp

microbubble emission boiling,

Stomry-MEB S-MEB

MEB

Calm-MEB C-MEB

2

S-MEB
CHF

S-MEB IS-MEB II

2

[16]
MEB
MEB
[11,12,14,15]
1980
[1-4]
Fig. 1
Fig. 2

[1]

[2]
[3]

MEB
[4]

MEB

[5]
[1-4]

MEB
Fig. 1

Boiling curves under Tsub = 30 K.

(Reuse of Fig. 6 in [1]: permitted by the JSME)Hz[6-13]

MEB
Ando et al. [7]MEB
Fig. 2[5,11-15]

Schematic image of microbubble emission

from heating surface.

[5](Reuse of Fig. 17 in [2]: permitted by the JSME)

2023

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Horiuchi et al. [11]

MEB
C-

MEB

S-MEB

MEB

MEB
[17]

[18]

[19]
[20-22]

Fig. 3 Boiling curves under Tsub = 40 K and 60 K.

[10]
MEB

Test liquid is distilled water, and the heating surface[23]

is made of copper, whose diameter is of 10 mm.
(Reuse of Fig. 3 in [12]: permitted by the Elsevier)

MEB

Tsat

MEB

MEB
Tsub = 60 K
Tsat

q"

MEB

q"CHF

2

MEB
Tsub

Fig. 1
Fig.
3

[16]

10 mm
Tsub

Tsat
S-MEB Iq"
Tsub = 40 K

Tsub

Tsat

60 K

S-MEB II
Tsub = 40
MEB

[1]
CHF

K

MEB

Tsub = 60 K

MEB

q"

Tsat

Tsat

q"

10 mm

Tsub = 40 K

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J. HTSJ, Vol. 62, No. 258

(c) MEB
Fig. 4

Fig. 3Tsub(c) MEB(a)(b) CHF[6-13]
Fig. 5Tsub= 40 K Fig. 3'7'

Fig. 4

Successive images of the behavior of thevapor bubbles on a copper heated surface of 10 mm
in diameter underTsub = 20 K for (a) nucleateboiling, (b) near CHF, and (c) MEB. The time-

Fig. 5averaged wall superheat and heat flux are (a) Tsat =under different conditions ('1' ~ '13') under Tsub = 40219.8 K, q" = 2.56 MW/m , (b) Tsat = 28.1 K, q" =K, and (bottom) zoomed view of spectrogram for2.82 MW/m2, and (c)Tsat = 53.4 K, q" = 3.38

state for '13'. The onset of the MEB is realized under
the condition of '7'. Test liquid is distilled water, and2

MW/m . Test liquid is distilled water.
(Reuse of Fig. 8 in [7]: permitted by the Elsevier)

2023

1

(top) Boiling-sound spectrogram for 20 s

the diameter of the heating surface is of 10 mm.
(Reuse of Fig. 5 in [12]: permitted by the Elsevier)- 20 -J. HTSJ, Vol. 62, No. 258

'11' ~ '13'
[12]
1.0 mmFig. 6r = 0 mm
r=

5 mm

'ai'
i

Fig. 5MEB
Fig. 6'a11'~ 'a13'MEB
Fig. 6'a7' ~ 'a10'

MEB
Fig. 6

Spatio-temporal behaviors of vapor bubbles

over heat transfer surface under different conditions
MEB('a5' ~ 'a13') as illustrated in Fig. 5. Dark regions[12]

correspond to the vapor bubbles passing through themonitoring line at 1 mm above the heat transfer
MEB

surface. The position r = 0 mm corresponds to thecenter of the heating surface.

MEB(Reuse of Fig. 8 in [12]: permitted by the Elsevier)Fig. 7

MEB

5 mm

MEB

Tsub = 20 K

2Tsat ~ 65 K q" ~ 4.8 MW/m
MEB[ms] = t0

t

CHF
MEB

MEB
[1,15,24] MEB
MEB'7'~ '11'

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1- 21 -J. HTSJ, Vol. 62, No. 258

Fig. 7

Successive images of condensing andcollapsing vapor bubbles on the heated surface intransition process from nucleate boiling near CHF to
MEB under Tsub = 20 K. Test liquid is a distilledwater, and the diameter of the heated surface is of 5mm.
(Reuse of Fig. 8 in [7]: permitted by the Elsevier)tt0 + 10t = t0 + 11t[1]

t0 + 13

Fig. 2MEB(a)(b)
Fig. 8Fig. 8

Temporal variation of (a) temperature and(b) quasi-heat flux under (1) Tsub = 10 K, (2) 20 K,
and (3) 40 K. Rows (1), (2) and (3) indicate theresults with the heating surface of 10 mm in diameter,
and Rows (2) and (3) with the heated surface of 5
mm in diameter.
(Reuse of Fig. 11 in [7]: permitted by the Elsevier)
MEB
MEB

Tsub

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CHF
T(cp)
(a)
(b)

MEB

MEB

(b)

S-MEB
MEB
C-MEB

C-MEB
Fig. 9Temporal variations of

S-MEB

T(cp) = Ts(c) - Ts(p)under (a) Tsub = 10 K and (b) 20 K. Here Ts(c) andTs(c)Ts(p) denote the temperature at the center and at theTs(p)periphery of the heating surface, respectively. FramesT(cp)= Ts(c) Ts(p)(a)(a) and (b) illustrate the results without and withT(cp)transition to the microbubble emission boiling(MEB), respectively.
(Reuse of Fig. 8 in [11]: permitted by the John Wiley(b)

and Sons)
MEB

b4

T(cp)

S(cp)

MEB

T

MEB
MEB

Fig. 7

MEB

MEB
MEB
[24-28]

MEB

MEB

CMEB
[11]
MEB

[5]
T(cp)

[11]
Fig. 9

15 mm

C-MEB
T(cp)

(b)

10 mm

5 mm

MEB
Tsub

[11]
Tsub = 10 K

2023

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(a)

(b)

20 K

MEB

- 23 -J. HTSJ, Vol. 62, No. 258

K

MEB
f0

f0
MEB
20

MEB

70

MEB

MEB

(cp)

T

MEB

Tsat
q"

Tsub
Tsat
Tsat
MEB

MEB
[29-34][29,35-37]

MEB

Tsat

Tsub

MEB
[5]

Fig. 10(a) Tsub = 40 K (b) 50 K(c) 60Fig. 10 Fundamental frequency f0 against corresponding boiling curve for (a) Tsub = 40 K, (b) 50 K,
and (c) 60 K. The data of f0 are plotted against q" andTsat on the vertical planes. Note that thefundamental frequency in the MEB regime only is plotted. Another note that upward and downward
triangles correspond to the data point obtained in the processes of increasing and decreasing the power
input, respectively. Test liquid is the distilled water, and the diameter of the heating surface is of 10 mm.
(Reuse of Fig. 4 in [13]: permitted by the JSME)

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[12]
f0
400 HzMEB

4500 HzFig. 5[12,13]

Tsub
q"
MEB

MEB

Tsat
q"
f0 - q"[41,42][43,44]2006
microbubble emission boiling,

Spoleto6th International Conference on Boiling Heat

MEB

Transfer

MEB

[1-4]
q ~ 102
MW/m2

[45]
CHF

MEB

MEB

[38]
MEB

[7,39,40]

[6]
MEB

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Reports, 6 (2016) 33454.

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Measurement Technique and Its Application toTransient Transition Boiling Heat Transfer during
Quenching of Hot Surface
Yuichi MITSUTAKE (Saga University)e-mail: mitutake@me.saga-u.ac.jp

CHF

MHF

80
CHF

CHF

qTB
1

(1)

N
Tsat

qw

qNB
ONB

MHF
SC

CHF

FB

qTB =

3
NB

qFB

TB

(1)

4

qNB + (1
CHF

)

qFB

(1)

MHF

Tsat

0
qTB

Tsat
1
qs
D-E
(qw

Tw
qs)
C-D

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J. HTSJ, Vol. 62, No. 258

Tw
[1]

4
MHF

A

V

Tw

ck

T

h
T
MHF

Tw

MHF
2

(2)

a)-c)
b)/c)

h

MHF
MHF
1
[2]

2

2
[3]
TSHL

302

199

[4]

3

Tb
Tw

4
2
1

(a)

(b)

(c)

Biot

2

0.1
T
Tb(t)

Tw

(2)

3

Tb(t)

5

3

2023

Tw(t)

89 mm
[5, 6]

1- 30 -2D

J. HTSJ, Vol. 62, No. 258

r = 10 mm

Tw

qw
MEMS

20 s

Tw

qw

[7]

IR

[8-11]

MHF
TSHL
5(a)

1
qw

10 kHz

Tw
Tw

IR
Tsub

MHF

MHF

Si

MHF
TSHL

200

5(b)

36 mm

[8, 11]
MHF

TSHL

300
Tw

MHF

TSHL

180
MHF

2(b)

1
MHF

TSHL

Coaxial Thermocouple

6

TSHL

Carbon steelEthanol2
G = 6 kg/m /s
Tbo= 300
r = 10 mm

300

: Tw
: qw
FB

TBNB SCMHF point

200
Tsu b
= 65 K

100

2

1
0.8

100

Carbon steel-Ethanol

Tbo = 300 2
G = 6 kg/(m s)Tsub, K20
40
65

r = 10 mm

0.6

TS HL=199

0

Tsu b= 20 K

100

200

t,s

0.2
0
300

a

20 s

4

SC NB

TB

FB

3

r , mm10
20

Copper
Tbo = 400
- Ethanol
Tsub = 60 K 2
Tw G = 12 kg/(m s)
M HF p oint
300

2
qw

4

100

0

FB

200

TB

400

600

(b)

NB

800 1000
t,s

f1/2

(3)

Interval of symbols
t = 20 s

TB2

TB 1

1/2

[13]

MHF
point

TSHL=199

Quech point0ek

Tbo = 400
Cop per-Ethanol
Tsub = 60 K 2
r , mm
G = 12 kg/(m s)1020
Quenchpoint

1k = (f /a)1/2

f

102 Tsat , K 5

101

[5]

400

100

[12]

10-1 Interval of symbols

(a)

200

CHF

MHF point
Quench point

0.4
Tsu b
= 40 K

60

-1

10
8 101

NB

TB2 TB1
TB

FB

102 Tsat , K 5

[6]

6

5

CR-Ni
[14]

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1

Ni

Cu

f1/2 = 100 kHz
m

7.8

[20]

22.3 m

7, 8

Cu

= x1

Ni

Ro - r 1

CR(3)

f1/2 = 0.480 a/
6

Ni

50 mm

SiO2

t 5 mm0.32 mm
3 m

CR

7(a)

Ni

T w, q w

CR-Ni[15,16]CRe (=( ck)1/2)

SiO2

Ni
Ni

SiO2
[14]
70 s

400

1
Material
Ni
Cu
ChromelSiO2 (300 K)ae (600 K)e, Ws1/2/cm2/K
1.86
3.72
0.983
1.80

a, mm2/s
12.7
103.9
5.62
0.81

Tw

7

1D

8

2D

qw

IHCP
Beck

/

/

9

Laplace[17,18]Ts0 = 350

7, 8

1D

2D

dj = 1 mm

Tl = 50uj =9.4 m/s

0.54 sr =1D

2D

7.5 mm
9
SC

NB

ONB
NB

rb

mm

WF:

Wetting Front
TB

TB

WF

[14,19]2023

1- 32 -J. HTSJ, Vol. 62, No. 258

WF

qw

WF
Plateau-RayleighWF
j = 4.508dj

twf

WF

qw

tq

FB, TB, NB, SC
tMHF

ONB

F2

WF

twf

: MHF

Maximum Heat Flux

tONB

[21]
F2
10 Hz

TB

K

10
10 MW/m2

Tw

qw
10

Ts0 = 370

30-50 K, uj = 6-10 m/s, Tsub =

5

F5

Tw

F1

j /uj

r = 7.5 mm
[16]

TB
Tsub

uj

NB

WF

FB
5

tWF

tq

Tw

WF
TWF

280

310

TSHL
Tq
TSHL

230

260

Tsub

uj

Tq
5
9
(Ts0 = 350, Water, Tsub = 50 K, ui = 9.4 m/s)(a) Tsub = 70 K
Tsub = 70 K,
uj = 8.0 m/s
Tsub = 50 K,
uj = 6.0 m/s
Tsub = 50 K,
uj = 8.0 m/s
Tsub = 50 K,
uj = 10.0 m/s
Tsub = 30 K,
uj = 8.0 m/s

10

Ts0 = 370

Ni(b) Tsub = 30 K

[16]

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J. HTSJ, Vol. 62, No. 258

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987.
[3] Berenson, P.J., Trans. ASME, J. Heat Trans.,83(1961)) 351.

T w, q w
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5 ms

Press (1970) 108.
[5]
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B
qc

75-758 (2009) 1917.

[6]

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rb
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CHF

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[15]Illias, S., et al., Therm. Sc. Eng., 22-2 (2014) 21.
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[18]Monde, M., et al., Int. J. Heat Mass Trans., 46 (2003)

WF
WF

2135.
2(b)

[19]Woodfield, P.L., et al., Int. J. Heat Mass Trans., 49(2006) 2864.

s[20], 107-7 (2021) 577.
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Report on the Lecture Measurement Technology, Foundation and Application of Temperature Measurement andThermal Conductivity Measurement

Kimihito HATORI (Bethel), Koji NISHI (Ashikaga University), Yoshihiro KONDO (Hitachi Academy),
Kenichi P. KOBAYASHI (Meiji University), Wataru SATO (Hitachi) and Katsuhiro KOIZUMI (Nabtesco)

2019
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2023
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E-mail: symp2023@htsj-conf.org
FAX: 092-802-3017

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33rd International Symposium on
Transport Phenomena (ISTP-33)

ISTP-33
nwatanabe@mec.sojo-u.ac.jp

International Gas Turbine Congress 2023
Kyoto
(IGTC2023 Kyoto)

E-mail: gtsj-office@gtsj.org- 39 -J. HTSJ, Vol. 62, No. 258

60

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1

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Full size manuscript
Abstract manuscript

PDF
PDF

140mm
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J. HTSJ, Vol. 62, No. 258

140 mm

Guide for the manuscripts (The case of MS-Word (Times New Roman 12pt)
Times New Roman 12pt)

(1

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Taro DENNETSU (Times New Roman 10pt)
Dept. of Mech. Eng., Dennetsu Univ., 5-1-5, Kashiwanoha, Kashiwa, 277-8563(1)
5English abstract ......
Times New Roman 10pt, 100(1)
Key Words: Heat Transfer
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140 mm

Guide for the manuscripts (The case of MS-Word (Times New Roman 12pt)
Times New Roman 12pt)

(1

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[

]

12pt
(1

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Taro DENNETSU (Times New Roman 10pt)
Dept. of Mech. Eng., Dennetsu Univ., 5-1-5, Kashiwanoha, Kashiwa, 277-8563(1)
Key Words: Heat Transfer
Times New Roman 10pt, 3 5
(1
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institutions, locations, abstract and keywords in order, lay out so that it fits within the width of 140 mm. If there are
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Times New Roman, 46 lines per one page. Color display is possible. References should be indicated by numbers withbrackets (1) on the right shoulder of cited parts in the text, and should be listed together at the end of the text as follows.
Example: (1) T. Dennetsu et al., J. Thermal Sci. Technol., 12-345(2018), 1234.
The template file of MS-Word format can be downloaded from the symposium's website.

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140 mm

Guide for the manuscripts (Main title: Times New Roman 14pt)
The case of MS-Word (Subtitle: Times New Roman 12pt)(blank line)*Taro DENNETSU (Authors: Times New Roman 12pt, Mark * at the head of
speakers name)(blank line)
Dept. of Mech. Eng., Dennetsu Univ., 5-1-5, Kashiwanoha, Kashiwa, 277-8563 (Affiliations:Times New Roman 10pt)(blank line)
Abstract of approximate 100 words is written by Times New Roman 10pt. Five blankcharacters are inserted as the indent.
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Key Words: Heat Transfer (Keywords: Times New Roman 10pt, 3 to 5 words)(blank line)
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Abstract Manuscript
As shown in the square enclosure below, the manuscript is composed of a title, a subtitle, author names, affiliation
institutions, locations and keywords in order, lay out so that it fits within the width of 140 mm. If there are multiple
authors, please mark * in front of the speaker and distinguish the affiliation institution and address with superscripted
numbers. Following the title part, please prepare the abstract as a guide with a single column of 10 point Times New
Roman, 46 lines per one page. Color display is possible. References should be indicated by numbers with brackets (1)on the right shoulder of cited parts in the text, and should be listed together at the end of the text as follows.
Example: (1) T. Dennetsu et al., J. Thermal Sci. Technol., 12-345(2018), 1234.
The template file of MS-Word format can be downloaded from the symposium's website.
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The case of MS-Word (Subtitle: Times New Roman 12pt)(blank line)*Taro DENNETSU (Authors: Times New Roman 12pt, Mark * at the head of
speakers name)(blank line)
Dept. of Mech. Eng., Dennetsu Univ., 5-1-5, Kashiwanoha, Kashiwa, 277-8563 (Affiliations:Times New Roman 10pt)(blank line)
Key Words: Heat Transfer (Keywords: Times New Roman 10pt, 3 to 5 words)(blank line)
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Note from the JHTSJ Editorial Board

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