宇宙航空研究開発機構特別資料
JAXA Special Publication
2011 年 3 月
宇宙航空研究開発機構
Japan Aerospace Exploration Agency
宇宙航空研究開発機構特別資料
東京大学 ロケットエンジンモデリングラボラトリー
(JAXA社会連携講座) シンポジウム
ロケットエンジン解析技術の新展開
" New Horizon of Rocket Engine Modeling and Simulation "
後 刷 集
東京大学工学系研究科
ロケットエンジンモデリングラボラトリー(JAXA 社会連携講座)
宇宙航空研究開発機構 情報・計算工学(JEDI)センター
JAXA-SP-10-010
This document is provided by JAXA.
ᚒ߇࿖ߩਥജࡠࠤ࠶࠻ߢࠆ H 㧙 IIA ߩ LE- 㧣 A ࠛࡦࠫࡦߩࠃ߁ߥᶧࡠࠤ࠶࠻ࠛࡦࠫࡦ ߪᭂૐ᷷ߩᶧ᳓⚛ߣᶧ㉄⚛ࠍផㅴߣߒߡ↪ߒߡ߹ߔ߇ޔΆቶౝߩ᷷ᐲߪ
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․છᢎ శ↵
-i-
This document is provided by JAXA.
ロケットエンジンモデリングラボラトリー(JAXA社会連携講座)
シンポジウム 「ロケットエンジン解析技術の新展開」
目 �
【基調講演】
(1)
キャビテーション流れのマルチスケール解析1
東京大学 工学系研究科 松本洋一郎 教授(2)
ものづくり分野における最先端シミュレーションの展望35
東京大学 生産技術研究所 加藤千幸 教授(革新的シミュレーション研究センター長)
(3)
東京大学航空宇宙工学専攻におけるロケット推進の研究活動61
東京大学 工学系研究科航空宇宙工学専攻 渡辺紀徳 教授【招待講演】
(1) Overview of Pratt & Whitney Rocketdyne Modeling & Simulation
Practices for Liquid Propellant Rocket Engines
81 Dr. Munir M. Sindir, Pratt & Whitney Rocketdyne
(2)Astrium Space Transportation's Liquid Propulsion Heritage
and Simulation Capabilities
97 Dr. Oliver Knab, EADS Astrium
【一般講演】
(1) JAXA
の目指すロケットエンジンシミュレーション115
宇宙航空研究開発機構 情報・計算工学センター 山西伸宏(2)
ロケットエンジン開発における全系解析に向けた取り組み125
宇宙航空研究開発機構 情報・計算工学センター 谷 直樹(3)
再生冷却エンジン燃焼室熱流束を支配する燃焼現象把握およびモデル評価137
宇宙航空研究開発機構 情報・計算工学センター 大門 優(4) Overview of CRUNCH CFD Simulations For Liquid Propulsion Systems 147 Dr. Ashvin Hosangadi, CRAFT Tech
(5)
高解像度コンパクト差分法を用いた超臨界圧環境下における噴流構造の数値解析163
宇宙航空研究開発機構 情報・計算工学センター 寺島洋史
(6)
燃焼振動抑制に向けた取り組み―レゾネータと燃焼器の減衰特性評価―175
宇宙航空研究開発機構 情報・計算工学センター 清水太郎This document is provided by JAXA.
(7) 187
宇宙航空研究開発機構宇宙輸送ミッション本部 エンジン研究開発グループ 冨田建夫
(8) LE-X
エンジンにおけるシミュレーション解析技術の活用195
宇宙航空研究開発機構
宇宙輸送ミッション本部 エンジン研究開発グループ 野田慶一郎
(9) MHI
における液体ロケットエンジン設計へのシミュレーション適用の取組み
207
三菱重工業株式会社 名古屋誘導推進システム製作所 小金澤崇(10)
ロケットエンジン設計解析技術-現在と未来-219
株式会社IHI
都丸裕司(11)
水素の高圧燃焼反応機構231
東京大学 工学系研究科 総合研究機構 越光男 教授(12)
ロケット燃焼解析に必要な熱物性モデルと数値解析239
東京大学 工学系研究科 総合研究機構 清水和弥 助教(13)
推進薬の高圧噴射と微粒化に関連した熱流動現象251
東京大学 工学系研究科航空宇宙工学専攻 姫野武洋 准教授(14)
多重プロセス型キャビテーションモデルの現状と課題267
信州大学 工学部 津田伸一 助教This document is provided by JAXA.
プログラム
【平成22年9月28日(火) 10:30-17:40】
10:30 - 10:40 開会挨拶 北森武彦(東京大学大学院工学系研究科長)
JAXA の目指すロケットエンジンシミュレーション 山西 伸宏(宇宙航空研究開発機構)
ロケットエンジン開発における全系解析に向けた取り組み 谷 直樹(宇宙航空研究開発機構)
再生冷却エンジン燃焼室熱流束を支配する燃焼現象把握およびモデル評価 大門 優(宇宙航空研究開発機構)
10:40 - 12:00 一般講演 1
Overview of CRUNCH CFD Simulations For Liquid Propulsion Systems Ashvin Hosangadi (CRAFT Tech)
高解像度コンパクト差分法を用いた超臨界圧環境下における噴流構造の数値解析 寺島 洋史(宇宙航空研究開発機構)
燃焼振動抑制に向けた取り組み―レゾネータと燃焼器の減衰特性評価―
清水 太郎(宇宙航空研究開発機構)
13:20 - 14:20 一般講演 2
ロケット燃焼器の燃焼試験技術の現状と課題 冨田 健夫(宇宙航空研究開発機構)
LE-X エンジンにおけるシミュレーション解析技術の活用 野田 慶一郎(宇宙航空研究開発機構)
MHI における液体ロケットエンジン設計へのシミュレーション適用の取組み 小金澤 崇(三菱重工業株式会社)
14:30 - 15:30 一般講演 3
ロケットエンジン設計解析技術-現在と未来-
都丸 裕司(株式会社 IHI)
15:40 - 16:40 招待講演 1
Overview of Pratt & Whitney Rocketdyne Modeling & Simulation Practices for Liquid Propellant Rocket Engines
Dr. Munir M. Sindir (Pratt & Whitney Rocketdyne) 16:40 - 17:40
招待講演 2
Astrium Space Transportation's Liquid Propulsion Heritage and Simulation Capabilities Dr. Oliver Knab (EADS Astrium)
【平成22年9月29日(水) 9:00-14:50】
9:00 - 10:00 基調講演 1
キャビテーション流れのマルチスケール解析 松本 洋一郎 教授(東京大学)
10:00 - 11:00 基調講演 2
ものづくり分野における最先端シミュレーションの展望 加藤 千幸 教授(東京大学)
11:00 - 12:00 基調講演 3
東京大学航空宇宙工学専攻におけるロケット推進の研究活動 渡辺 紀徳 教授(東京大学)
水素の高圧燃焼反応機構
越 光男 教授(東京大学)
ロケット燃焼解析に必要な熱物性モデルと数値解析 清水 和弥 助教(東京大学)
推進薬の高圧噴射と微粒化に関連した熱流動現象 姫野 武洋 准教授(東京大学)
13:20 - 14:40 一般講演 4
多重プロセス型キャビテーションモデルの現状と課題 津田 伸一 助教(信州大学)
14:40 - 14:50 閉会挨拶 嶋 英志(宇宙航空研究開発機構 情報・計算工学センター長)
This document is provided by JAXA.
⊒ ౝ ኈ
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䉨䊞䊎䊁䊷䉲䊢䊮ᵹ䉏䈱 䊙䊦䉼䉴䉬䊷䊦⸃ᨆ
᧲੩ᄢቇᎿቇ♽⎇ⓥ⑼
᧻ᧄᵗ ㇢
᧻ᧄᵗ৻㇢
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• න৻᳇ᵃ䈱േ
• ᳇ᵃ䉪䊤䉡䊄䈱േ
• ᵹᯏ᪾䈱䉨䊞䊎䊁䊷䉲䊢䊮䉣䊨䊷䉳䊢䊮 ᵹᯏ᪾ 䉨䊞 䊁
• 䈍䉒䉍䈮 䈍䉒䉍䈮
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䉨䊞䊎䊁䊷䉲䊢䊮䈮䈍䈔䉎䊙䊦䉼䉴䉬䊷䊦䉻䉟䊅䊚䉾䉪䉴
B-B Interaction Volumetric oscillation
Mist
Mist Temperature
Distribution
Internal Phenomena
of a Cavitation Bubble Bubble Cloud Cavitating Flow around a Hydrofoil
Micro Mezzo Macro
of a Cavitation Bubble around a Hydrofoil
Micro Mezzo Macro
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• 䈍䉒䉍䈮 䈍䉒䉍䈮
㻞
This document is provided by JAXA.
Time history of bubble radius Time history of bubble radius
A
A E E
R
R 13 13
A
A B B D D R R 0 0 = 13 = 13 ��m m ff d d = 0.2 MHz = 0.2 MHz pp 0 0 = 100 kPa = 100 kPa
��pp = 50 kPa = 50 kPa
C C
��pp 50 kPa 50 kPa
C C Mist
Mist
240240 840 [K]840 [K]A
A B B C C D D E E
Temperature distribution inside bubble Temperature distribution inside bubble
Assumptions Assumptions
(1)
(1) Gases inside the bubble and the surrounding liquid move Gases inside the bubble and the surrounding liquid move maintaining spherical symmetry
maintaining spherical symmetry maintaining spherical symmetry.
maintaining spherical symmetry.
(2)
(2) Gases inside the bubble obey the perfect gas law. Gases inside the bubble obey the perfect gas law.
(3)
(3) Non Non--condensable gas obeys Henry’s law at the bubble wall. condensable gas obeys Henry’s law at the bubble wall.
(4)
(4) Classical theory for generation and growth of mist under quasi Classical theory for generation and growth of mist under quasi-- equilibrium condition is applied, because the temperature inside equilibrium condition is applied, because the temperature inside the bubble does not change so rapidly .
the bubble does not change so rapidly . (5)
(5) Coalescence and fragmentation of the mist are ignored. Coalescence and fragmentation of the mist are ignored.
(6)
(6) Mist has the same velocity as the gas mixture and the effect of Mist has the same velocity as the gas mixture and the effect of diffusion by Brownian motion is assumed to be small and diffusion by Brownian motion is assumed to be small and ignored.
ignored.
(7)
(7) Viscosity of the liquid is ignored except at the bubble wall. Viscosity of the liquid is ignored except at the bubble wall.
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Governing equations of Governing equations of Direct Numerical Simulation (1) Direct Numerical Simulation (1) ( ) ( )
Using simulation code developed by Takemura & Matsumoto (1994) Using simulation code developed by Takemura & Matsumoto (1994)
䂾
䂾
Full conservation equations in gas phase with mist Full conservation equations in gas phase with mist
Using simulation code developed by Takemura & Matsumoto (1994) Using simulation code developed by Takemura & Matsumoto (1994)
䊶
䊶
Conservation equation of Mass Conservation equation of Mass
䊶䊶
Conservation equation of Momentum Conservation equation of Momentum
䊶䊶
Conservation equation of Energy Conservation equation of Energy Conservation equation of Energy Conservation equation of Energy
䂾䂾
Nucleation rate equation of mist by homogeneous condensation Nucleation rate equation of mist by homogeneous condensation
䂾䂾
Conservation equation of number density of mist Conservation equation of number density of mist
䂾䂾
Energy equation in liquid phase Energy equation in liquid phase
䂾䂾
Diffusion equation of non Diffusion equation of non condensable gas in liquid condensable gas in liquid
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Diffusion equation of non Diffusion equation of non--condensable gas in liquid condensable gas in liquid
Governing equations of Governing equations of Direct Numerical Simulation (2) Direct Numerical Simulation (2) ( ) ( ) Motion of bubble wall
Motion of bubble wall
䂾
䂾 Equation of bubble wall motion Equation of bubble wall motion 䋨 䋨 Fujikawa & Akamatsu, 1980 Fujikawa & Akamatsu, 1980 䋩䋩
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� Considered Considered 䊶
䊶 Liquid compressibility (1st Liquid compressibility (1st order approximation) order approximation) 䊶
䊶 Phase change at bubble wall Phase change at bubble wall
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Time history of bubble radius Time history of bubble radius
R
R = 13 = 13 ��m m R
R 0 0 13 13 ��m m ff d d = 0.2 MHz = 0.2 MHz
100 k 100 k pp 0 0 = 100 kPa = 100 kPa
�� p p = 50 kPa = 50 kPa
㪩㪅㪄㪧㪅㩷㪜㫈㫅㪅 䋭 㪠㫊㫆㫋㪿㪼㫉㫄㪸㫃
㪪 㫀㫋 㪿 㪻 䋭㪪㫎㫀㫋㪺㪿㪼㪻 䋭㪘㪻㫀㪸㪹㪸㫋㫀㪺
Bubble motion Bubble motion
Comparison between simulation and experiment Comparison between simulation and experiment
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Maximum bubble radius Maximum bubble radius
R
R 0 0 = 3 ~ 40 = 3 ~ 40 �� m m ff dd = 0.2 MHz = 0.2 MHz pp 00 = 100 kPa = 100 kPa pp 00
��p p = 50 kPa = 50 kPa
Time histories of bubble radius, temperature Time histories of bubble radius, temperature
and mist density inside bubble and mist density inside bubble and mist density inside bubble and mist density inside bubble R
R 0 0 = 13 = 13 ��m, m, ff dd = 0.2 MHz, = 0.2 MHz, pp 0 0 = 100 kPa, = 100 kPa, ��p p = 50 kPa = 50 kPa
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Distributions of temperature, vapor Distributions of temperature, vapor
concentration and mist density concentration and mist densityyy
A A A A R
R 00 00 = 13 = 13 ��m �� m ff d d = 0.2 MHz = 0.2 MHz pp 00 = 100 kPa = 100 kPa pp 00 100 kPa 100 kPa
�� p p = 50 kPa = 50 kPa
Distributions of temperature, vapor Distributions of temperature, vapor
concentration and mist density concentration and mist densityyy
B B B B R
R 00 00 = 13 = 13 ��m �� m ff d d = 0.2 MHz = 0.2 MHz pp 00 = 100 kPa = 100 kPa pp 00 100 kPa 100 kPa
��p p = 50 kPa = 50 kPa
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Distributions of temperature, vapor Distributions of temperature, vapor
concentration and mist density concentration and mist densityyy
C C C C R
R 00 00 = 13 = 13 ��m �� m ff d d = 0.2 MHz = 0.2 MHz pp 00 = 100 kPa = 100 kPa pp 00 100 kPa 100 kPa
�� p p = 50 kPa = 50 kPa
Distributions of temperature, vapor Distributions of temperature, vapor
concentration and mist density concentration and mist densityyy
D D D D R
R 00 00 = 13 = 13 ��m �� m ff d d = 0.2 MHz = 0.2 MHz pp 00 = 100 kPa = 100 kPa pp 00 100 kPa 100 kPa
��p p = 50 kPa = 50 kPa
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Distributions of temperature, vapor Distributions of temperature, vapor
concentration and mist density concentration and mist densityyy
E E E E R
R 00 00 = 13 = 13 ��m �� m ff d d = 0.2 MHz = 0.2 MHz pp 00 = 100 kPa = 100 kPa pp 00 100 kPa 100 kPa
�� p p = 50 kPa = 50 kPa
Distributions of temperature, vapor Distributions of temperature, vapor
concentration and mist density concentration and mist densityyy
FFFF R
R 00 00 = 13 = 13 ��m �� m ff d d = 0.2 MHz = 0.2 MHz pp 00 = 100 kPa = 100 kPa pp 00 100 kPa 100 kPa
��p p = 50 kPa = 50 kPa
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Maximum bubble radius Maximum bubble radius
R
R 0 0 = 0.3 ~ 4 = 0.3 ~ 4 ��m m ff = 2 MHz = 2 MHz ff dd = 2 MHz = 2 MHz pp 0 0 = 100 kPa = 100 kPa
Spherical bubble model Spherical bubble model
Internal thermal phenomena are considered Internal thermal phenomena are considered
�
� Mass and Mass and heat transfer through the bubble wall heat transfer through the bubble wall
�
� Phase change at the bubble wall Phase change at the bubble wall
�
� Counter diffusion of vapor and non Counter diffusion of vapor and non condensable gas condensable gas
�
� Counter diffusion of vapor and non Counter diffusion of vapor and non--condensable gas condensable gas
�
� Mist condensation and evaporation Mist condensation and evaporation Matsumoto,
Matsumoto, Trans. of JSME Trans. of JSME, 1986. , 1986.
�
� Temperature gradient model at the bubble wall Temperature gradient model at the bubble wall Preston et al.,
Preston et al., CAV2003, CAV2003, 2003. 2003.
Mist
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Governing equations Governing equations
The motion of the bubble wall (Fujikawa & Akamatsu equation)
3 4 3 1 4 2 2 3
1 2
� �
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���
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p R p m p
m m R R m
c R c R m
c m c R R R
R l R l l
l �
�
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2 0 2
1
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�
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c p R p m p
m R c m c R R m
l R r l l
R r l l
l l
l � � � � �
� �
� �
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��
� � ���� � �����
� �
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l l b i i l
l gi vi g v R r l
R m R R p m
p
p �
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2
, �l
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�vi��gi�
Rb R� �l�The energy conservation equation in gas phase with mist
� �
0
2 2
�
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��
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h dM dM h dM
h dM S T
LdM
dt d M p dt d M p dt
T M d C M C M C
c l c g v
c
v v
v g v g
g g c vl v vv g vg
�
�
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�
� 0
��
� �
� �
�
�
�
� � � h dt
dt h dt
h dt S r
L dt g v l
R r
�
The energy conservation equation in liquid phase The diffusion equation of non condensable gas in liquid
The diffusion equation of non-condensable gas in liquid The nucleation rate equation of mist
Present model vs. DNS Present model vs. DNS
Internal gas: nitrogen Internal gas: nitrogen Initial bubble radius: 2 Initial bubble radius: 2 ��m m Initial pressure:
Initial pressure: 100 kPa 100 kPa I iti l t t 293 K I iti l t t 293 K Initial temperature: 293 K Initial temperature: 293 K
DNS: Takemura and Matsumoto, DNS: Takemura and Matsumoto, JSME I J
JSME I J 1994 1994 JSME Int. J.
JSME Int. J.,, 1994. 1994. 100 kPa � 90 kPa � 100 kPa 100 kPa � 90 kPa � 100 kPa
100 kPa � 50 kPa � 100 kPa
100 kPa � 50 kPa � 100 kPa 100 kPa � 10 kPa � 100 kPa 100 kPa � 10 kPa � 100 kPa
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Heating Mechanism of Microbubbles Heating Mechanism of Microbubbles
Energy affecting the heat near the bubble
4 R
2W � � T
l� Heat deposition
4 R W
T�
lr
l� �
� �
�
Viscous dissipation 4
24 R R
R
W
V� �
lR � � � � � Viscous dissipation R
R
Acoustic emission
�
lT
l: thermal conduction : temperature
� �
22 2
2 4 c R
R R
W
A� �
lR � � � � � � Acoustic emission
T
l�
l�
l: temperature : viscosity
: density c
lEnergy escaping to large distances
c
l: sound speed
Energy Radiation Energy Radiation
Frequency : 1.0 MHz Amplitude : 100 kPa Initial radius : 1 10 �m Initial radius : 1 - 10 �m Internal gas : air
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Properties of Microbubbles Properties of Microbubbles
Bubble radius
Ტ᳸ 10�m Უ
Shell
Ტ � Უ
Ტ material, thickness … Უ
Internal gas microbubble
Specific
heat ratio Gas
constant Heat conductivity heat ratio
[-] constant
[J / kg 䊶 K] conductivity [ mW /m
䊶K ]
Argon (Ar) 1 67 208 1 18 2
Argon (Ar) 1.67 208.1 18.2
air 1.40 287.0 26.9
Sulfur Hexafluoride (SF 6 ) 1 09 56 9 14 8 Sulfur Hexafluoride (SF 6 ) 1.09 56.9 14.8
Ar bubble Ar bubble
Frequency : 1.0 MHz A lit d 100 kP Amplitude : 100 kPa Initial radius : 1 - 10 �m Internal gas : Ar (Air bubble)
(Air bubble)
e a gas :
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SF
SF 66 Bubble Bubble
Frequency : 1.0 MHz A lit d 100 kP Amplitude : 100 kPa Initial radius : 1 - 10 �m Internal gas : Ar (Air bubble)
(Air bubble)
e a gas :
Acoustic emission from a microbubble Acoustic emission from a microbubble
Acoustic velocity of water
=1.478 㫏 10
3(m/s)
Emitted acoustic pressure from micro bubble in far field 䋨Fujikawa, 1979䋩
䋨Fujikawa, 1979䋩
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Nonlinear oscillation of a microbubble Nonlinear oscillation of a microbubble
R
R
00= = 1.5 1.5 ��m, m, pp
0 0= = 101.3 101.3 kPa, kPa, ff
00= = 22 MHz, MHz, ��p p = = 100 100 kPa kPa
mbient sure [-]am press
e [-]
bubble radius [
oustic uaco re [Pa]pressu
Time history of ambient pressure, bubble radius Time history of ambient pressure, bubble radius and acoustic pressure from the bubble
and acoustic pressure from the bubble
Nonlinear oscillation of a microbubble Nonlinear oscillation of a microbubble
R
R
00= = 1.5 1.5 ��m, m, pp
0 0= = 101.3 101.3 kPa, kPa, ff
00= = 22 MHz, MHz, ��p p = = 100 100 kPa kPa
bubble radius [-]r
stic e acous [Pa]pressurede [dB]amplitud
Time history of bubble radius and acoustic Time history of bubble radius and acoustic
pressure, and spectrum of the acoustic pressure pressure, and spectrum of the acoustic pressure
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Calculation Conditions Calculation Conditions
2.0 [ � m]
Initial Bubble Radius, R
b0293 [K]
Initial Temperature
101.3 [kPa]
Initial Ambient Pressure, p
�01.34 [MHz]
Ultrasound Frequency, f
0sinus Waveform of Ambient Pressure
[ ]
q y,
00 [kPa] ~ 1 [MPa]
Amplitude of Ambient Pressure
t f
Formula of ambient ultrasound pressure Formula of ambient ultrasound pressure
�
0�
5 00
sin 2 10
500
��
� f t A f t � � p
p �
Bubble Radius Bubble Radius
Time history of bubble radius Time history of bubble radius
Bifurcation diagram of bubble radius Bifurcation diagram of bubble radius
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Acoustic Turbulence Acoustic Turbulence
Power spectrum of bubble radius
Power spectrum of bubble radius Power spectrum of acoustic pressure Power spectrum of acoustic pressure Power spectrum of bubble radius
Power spectrum of bubble radius Power spectrum of acoustic pressure Power spectrum of acoustic pressure
Experiment of PMs in Water
Experiment of PMs in Water (Depth = 30 m) (Depth = 30 m)
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Simulation Model Simulation Model
• Assumption
(1) Gases inside the bubble and the surrounding liquid move maintaining spherical symmetry.
(2) Pressure and temperature inside the bubble are (2) Pressure and temperature inside the bubble are
uniform except the thin boundary layer near the bubble wall.
(3) Non-condensable gas obeys Henry’s law at the bubble wall.
(4) Viscosity of the liquid is ignored except at the bubble wall.
Time History of Bubble Radius Time History of Bubble Radius
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Time History of Pressure Distribution
Time History of Pressure Distribution (p�=400 (p�=400 䌫 䌫 Pa) Pa)
Time History of Pressure Distribution
Time History of Pressure Distribution (p�=400 (p�=400 䌫 䌫 Pa) Pa)
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Time History of Emitted Pressure at 0.7 m Time History of Emitted Pressure at 0.7 m
Bubble Collapse and Shock Wave Formation Bubble Collapse and Shock Wave Formation
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• 䈲䈛䉄䈮
න ᳇ᵃ䈱േ
• න৻᳇ᵃ䈱േ
• ᳇ᵃ䉪䊤䉡䊄䈱േ
• ᵹᯏ᪾䈱䉨䊞䊎䊁䊷䉲䊢䊮䉣䊨䊷䉳䊢䊮 ᵹᯏ᪾ 䉨䊞 䊁
• 䈍䉒䉍䈮 䈍䉒䉍䈮
Model of a bubble cloud Model of a bubble cloud
The following phenomena are considered The following phenomena are considered The following phenomena are considered.
The following phenomena are considered.
�
� Compressibility of the liquid Compressibility of the liquid
�
� Evaporation and condensation Evaporation and condensation of the liquid at the bubble wall of the liquid at the bubble wall of the liquid at the bubble wall of the liquid at the bubble wall
�
� Evaporation and Evaporation and condensation of the mist condensation of the mist
�
� ff
condensation of the mist condensation of the mist inside the bubble
inside the bubble
�
� Heat transfer through Heat transfer through the bubble wall
the bubble wall
Shimada, Kobayashi and Matsumoto (1999)
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Assumptions Assumptions
Assumptions for a bubble cloud Assumptions for a bubble cloud
� The bubble cloud oscillates maintaining spherical symmetry.
� Bubbly liquid inside the cloud is treated as a continuum fluid.
� Bubbles move with the surrounding liquid.
� Bubbles move with the surrounding liquid.
� Coalescence and fragmentation of bubbles in the cloud are ignored.
� Viscosity of bubbly mixture is ignored in the cloud.
� Th t t f th li id i th l d i t t
� The temperature of the liquid in the cloud is constant.
� Each bubble oscillates maintaining spherical symmetry.
Assumptions for each bubble Assumptions for each bubble
� Each bubble oscillates maintaining spherical symmetry.
� The pressure and temperature inside the bubble are uniform except for the thin boundary layer near the bubble wall.
� Temperature at the bubble wall is equal to that of liquid
� Temperature at the bubble wall is equal to that of liquid.
� Mass of non-condensable gas inside a bubble is constant.
� Gases inside a bubble obey the van der Waals gas law.
� Coalescence and fragmentation of mist inside a bubble are ignored.
Governing equations 1 Governing equations 1
The motion of the bubble cloud interface
3 2 1
1 1 1 4
2 3
c c c c c
c c c w l
l c
R R R R d R
R R R p p
c c c c dt � R
� �
� �
� � � � � � � � � � � �� � � �
� � � � � �
� � � � � �� �
� � � �
�� �
The mass and momentum conservation equations
� �
2�
2� � �
1 1
1 0
l
r l lu
� � � �
� � � � � �
� 2�
� � �
l l�
t r r �
� �
� �
2�
2� �
2�
1 1
1 0
l l
l l
u p
r u
t r r r
� � � �
� � � � � �� �
� � �
The conservation equation of the number density of bubbles
�
2�
1 0
n r nu
� � � �
The governing equations for each bubble (The motion of the bubble wall,
� �
2 r nub 0
t�r r �
� �
g g q ( ,
The energy conservation equation, The nucleation rate equation of the mist
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Governing equations 2 Governing equations 2
The motion of the bubble wall (Fujikawa & Akamatsu equation)
3 2 4 4
1 2 1
2 3 3
l l
R m m R
RR R
c �c �c c
� � � �
� � � � �
� � � �
� � � �
� � � �
�� �
( j q )
, ,
1 2 0
2
l r R l r R
l l l l l l
p p Rp
mR R m m m
c c R c
� � � � � �
�� � �
� � � �
� � � � �� � � �� � �
� � � �
� �
�� � � � �
� �
� �
2
2 4
vi gi l l
l R
m m
p p p � �� �� � � �R �
� � � � � � ��� ��
� �
, 2 4
l r R v g
b l
l vi gi
p p p R
R R �
� � �
� � � �� ��
The energy conservation equation in gas phase with mist
� �
2 2g g g v v v
vg g vv v vl c
g v
p M d p M d C M C M C M dT
dt dt dt
dM T dM dM dM
� �
� �
� � � �
� � �
0
c v c c
v l
r R
dM T dM dM dM
L S h h
dt � r dt dt dt
�
� � �
� � � � � �� � ��� � �
The nucleation rate equation of mist q
Frequency response of a bubble cloud Frequency response of a bubble cloud
Maximum pressure inside the bubbles in the cloud Maximum pressure inside the bubbles in the cloud
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Natural modes (
Natural modes (�� pp = 10 kPa) = 10 kPa)
ff = 200 kHz = 200 kHz ff = 600 kHz = 600 kHz Water pressure inside the bubble cloud
Water pressure inside the bubble cloud Natural mode shapes
Natural mode shapes
Linearized analysis of a spherical bubble Linearized analysis of a spherical bubble cloud (d’Agostino & Brennen, 1989) cloud (d’Agostino & Brennen, 1989)
Natural mode shapes Natural mode shapes
( g , )
( g , )
•• Continuity equation Continuity equation
•• Momentum equation Momentum equation R l i h
R l i h Pl Pl t t ti ti
•• Rayleigh Rayleigh--Plesset equation Plesset equation
Frequency response of a bubble cloud Frequency response of a bubble cloud
Maximum pressure inside the bubbles in the cloud Maximum pressure inside the bubbles in the cloud
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Pressure wave in the bubble cloud Pressure wave in the bubble cloud
��pp = 75 kPa, 190 kHz = 75 kPa, 190 kHz
��pp = 10 kPa, 200 kHz = 10 kPa, 200 kHz
Collapse of the cloud
Collapse of the cloud ((�� pp = 125 kPa, 160 kHz) = 125 kPa, 160 kHz)
a]sure [MPapress
/R [ ]
time, t/ T [-]
r/ Rc0 [-]
Water pressure inside the bubble cloud Water pressure inside the bubble cloud
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⋡ᰴ
• 䈲䈛䉄䈮
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• න৻᳇ᵃ䈱േ
• ᳇ᵃ䉪䊤䉡䊄䈱േ
• ᵹᯏ᪾䈱䉨䊞䊎䊁䊷䉲䊢䊮䉣䊨䊷䉳䊢䊮 ᵹᯏ᪾ 䉨䊞 䊁
• 䈍䉒䉍䈮 䈍䉒䉍䈮
䉪䊤䉡䊄䉨䊞䊎䊁䊷䉲䊢䊮䈱᷵
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⠢䉨䊞䊎䊁䊷䉲䊢䊮䈱ᤨ㑆⊒ዷ
Cavity Velocity(|u|) Pressure
6 . 0 deg,
6 �
�
� �
�
⢛ ᥊
䊘䊮䊒䈱↢↥䉮䉴䊃ૐᷫ � ዊဳൻ
㜞ㅦ䋨㜞࿁ォ䋩ൻ
䉨䊞䊎䊁䊷䉲䊢䊮䉣䊨䊷䉳䊢䊮 䉨䊞䊎䊁 䉲䊢䊮䉣䊨 䉳䊢䊮
䉣䊨䊷䉳䊢䊮੍᷹䋺 ᓥ᧪䈲ታ㛎⊛䈭ᚻᴺ䈏ਥᵹ
CFD
䈱ലᵴ↪�
⹜㛎䈱⋭ജൻ䈮䉋䉎㐿⊒ᦼ㑆⍴❗䉨䊞䊎䊁䊷䉲䊢
䊮 䉨䊞䊎
䉨䊞䊎䊁䊷䉲䊢䊮㐳䈘 䊁
䉣䊨䊷䉳䊢䊮੍᷹ᴺ䈱৻䋺
นⷞൻ⸘᷹
䊁䊷 䉲䊢䊮㐳䈘
䉣䊨 䉳 䊮ㅦᐲ䉕੍᷹
㪚㪝㪛੍᷹
ታ㛎ᑼ
䉣䊨䊷䉳䊢䊮
䉣䊨䊷䉳䊢䊮ㅦᐲ䉕੍᷹
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᳇ᵃ䊝䊂䊦⸃ᨆ䉮䊷䊄
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䊶᳇ᵃᢙኒᐲಽᏓ
᳇ᵃ䈱⚦േ
᳇ᵃ䊝䊂䊦⸃ᨆ 䊄
᳇ᵃ䈱፣უ 䋨ᶖṌ䋩
䊶᳇ᵃ䈱⚦േ
䋨᳇ᵃ䈱ਗㅴ䊶Ⓧㆇേ䋩
᳇ᵃ 䉴䊌䉟䉪⁁䈱 ⴣ᠄⊒↢
㆙ᔃ䊘䊮䊒
㆙ᔃ䊘䊮䊒
ⴣ᠄⊒↢
䉨䊞䊎䊁䊷䉲䊢䊮ᒝ䈘 䉨䊞 䊁 䉲䊢䊮ᒝ䈘 䉣䊨䊷䉳䊢䊮⊒↢⟎䊶㊂
䋨ታ㛎䌄䌂䋩
䉳䊢䊮⊒↢⟎ ㊂
⸘▚ᚻᴺ
(1) ቯ ( )
ᶧ⋧䋺
᳓ (
㕖❗ᕈ)
᳇⋧䋺᳇ᵃ (
❗ᕈ)
䊶᳇ᵃ䈲ᒻ䈪ว䉇ಽⵚ䈭䈚
᳇ᵃౝ䈲⫳᳇䈍䉋䈶ਇಝ❗䉧䉴 䊶᳇ᵃౝ䈲⫳᳇䈍䉋䈶ਇಝ❗䉧䉴
䋨╬᷷⤘ᒛ䊶ᢿᾲ❗䋩
䊶᳇⋧䈱ኒᐲ䉇ㆇേ㊂䈲ᶧ⋧䈮 Ყ䈼䈩ᓸዊ
( ) ᡰ㈩ᣇ⒟ᑼ (2) ᡰ㈩ᣇ⒟ᑼ
䊶ᶧ⋧Ⓧ₸䈱ሽᑼ 䊶᳇ᵃᵹ䈱ㆇേ㊂ሽᑼ 䊶᳇ᵃᵹ䈱ㆇേ㊂ሽᑼ 䊶᳇ᵃᢙኒᐲ䈱ሽᑼ
䊶ജᣇ⒟ᑼ䋨Ⓧ₸䈱᜔᧤᧦ઙ䈎䉌ዉ䇯ᡆૃ❗ᕈᴺ䈱⠨䈋ᣇ䈮ၮ䈨䈒䋩
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ᡰ㈩ᣇ⒟ᑼ -1
G H F E G F E t
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t
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ᡰ㈩ᣇ⒟ᑼ -2
R l i h Pl t ᑼ
᳇ᵃ䈱Ⓧㆇേ
̪Ꮢ⽼䉮䊷䊄╬䈪䈲Ꮐㄝ╙䋱㗄䉕⋭⇛䈚䇮◲ᤃᑼ䉕⸃䈒
䋨᳇ᵃേ ⇛䉕⸃䈒䋩䉅 䈏䈅䉎Rayleigh-Plesset ᑼ
) )(
4 ( ) 1
2 (
3
22 2
Gi Li Gi Li L
B G
G
G
p p u u u u
D Dr r
r D � � � � � � --- (2)
䋨᳇ᵃേ䈱⇛䉕⸃䈒䋩䉅䈱䈏䈅䉎䇯
) )(
4 ( )
2 (
2 Li Gi Li Gi
L
G
Dt Dt �
D Dr p T
p
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p p
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v G
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䊗䉟䊄₸ ᳇ᵃ䈱ਗㅴㆇേ
᳇ᵃౝജ
䊗䉟䊄₸
G G
G
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f
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pi Di Li CiAi
F F F F
--- (4) F --- (5)
3
F
Ai: ઃടᘠᕈജ
F
pi: ࿐ᵹ䈱ടㅦ䈮䉋䉎ജ
᛫ജ䈍 䈶឴ജ
᳇ᵃᢙኒᐲ
F
Di, F
Li: ᛫ജ䈍䉋䈶឴ജ F
Ci: 䉮䊥䉥䊥ജ
㻞㻥
This document is provided by JAXA.
㪀㩷⸃ᨆ㗔ၞ䈫Ⴚ⇇᧦ઙ
ญႺ⇇
㫑
ๆㄟ
ญႺ⇇
䊶ᵹㅦ䇮᳇ᵃᓘ䇮᳇ᵃᢙኒᐲ╬䈱৻᭽ᵹ
⋥▤ᵹ ญႺ⇇
〝 ฯ
ᚸᒻᄢᵹ〝
Ⴚ⇇
䊶ജ৻ቯ 䉲䊠䊤䉡䊄
ᚸᒻᄢᵹ〝
䊶䉲䊠䊤䉡䊄䈅䉍 䊶⠀ᩮᨎᢙ䋶ᨎ
㪛㪔㩷㪊㪇㪉㩷㫄㫄 㪈㪏㪇㩷㫄㫄 㪧㪪
䊶⸃ᨆᩰሶᢙ ⚂ 㪉㪉㪇㪃㪇㪇㪇
㪪㪪
㪉㪌㪇㩷㫄㫄 䊶ೋᦼ᧦ઙ
䊗䉟䊄₸ 㪑㩷㪇㪅㪇㪇㪈㩷㩿㪔㩷㪇㪅㪈䋦㪀
᳇ᵃᓘ 㪑㩷㪈㪅㪇㬍㪈㪇㪄㪌㫄 㩿 㪈㪇 㪀
㩿㪔㩷㪈㪇㩷㱘㫄㪀
ᱜ㕙䋨㪧㪪䋩䈫⽶㕙䋨㪪㪪䋩
䈱㑆䈱㪈⠢㑆
⸃ᨆ⚿ᨐ䈍䉋䈶⠨ኤ 䋱
4 1 䉨䊞䊎䊁䊷䉲䊢䊮ᕈ⢻
⸃ᨆ⚿ᨐ䈲䇮䊘䊮䊒䈱৻⥸⊛䈭 䉨䊞䊎䊁 䉲䊢䊮ᕈ⢻䈫4.1 䉨䊞䊎䊁䊷䉲䊢䊮ᕈ⢻
ㇱಽ⽶⩄᧦ઙ
( Q/Q
d= 0.6)
䉨䊞䊎䊁䊷䉲䊢䊮ᕈ⢻䈫 ቯᕈ⊛䈮৻⥌
)
1.4 1.6
1.2 1.4
0 0.2 0.4 0.6 0.8 1
NPSH’R cal= 0.068
0 8 1.0 1.2
�
0.8Case 1 1
Ȁ
0.4 0.6
�
0.80.4 0.6
Exp.
NPSH’R exp= 0.094
Ȁ
� = H / ( U
t2/ 2g )
NPSH’ = NPSH / ( U
t2/ 2g)
0.0 0.2
0.0 0.2 0.4 0.6 0.8 1.0
0
p 0.2
Cal.
0.0 0.2 0.4 0.6 0.8 1.0
NPSH'
㻟㻜
This document is provided by JAXA.
⸃ᨆ⚿ᨐ䈍䉋䈶⠨ኤ 䋲 䊗䉟䊄₸䈫᳇ᵃᢙኒᐲ
䉨䊞䊎䊁䊷䉲䊢䊮㗔ၞ ᳇ᵃᩭ䈱㓸Ⓧ
䉨䊞䊎䊁 䉲䊢䊮㗔ၞ ᳇ᵃᩭ䈱㓸Ⓧ
㩿㫄㩷㩷㪀㪄㪊
ォᣇะ ࿁ォᣇะ
࿁ォᣇะ ࿁ォᣇะ
䊗䉟䊄₸ ᳇ᵃᢙኒᐲ
⸃ᨆ⚿ᨐ䈍䉋䈶⠨ኤ 䋳
㪇㪅㪈㪋 㪇㪅㪈㪍
㪇 㪇
㪇 㪇 㪇 㪇 㪇 㪈 㪈 㪈 㪈 㪈 㪈
䊗䉟䊄₸
L.E. T.E.
㪇㪅㪇㪏 㪇㪅㪈㪇 㪇㪅㪈㪉 㪇㪅㪈㪋
㫉㪸㪺㫋㫀㫆㫅㪃㩷㪽㪞
㪇 㪇
䊗䉟䊄₸ 㪇
s s =0 L.E.
㪇㪅㪇㪉 㪇㪅㪇㪋 㪇㪅㪇㪍
㪭㫆㫀㪻㩷㪝㫉
㪇 㪇 㪇
s =1
࿁ォᣇะ 㪇㪅㪇㪇㪇㪅㪇 㪇㪅㪈 㪇㪅㪉 㪇㪅㪊 㪇㪅㪋 㪇㪅㪌 㪇㪅㪍 㪇㪅㪎 㪇㪅㪏 㪇㪅㪐 㪈㪅㪇 㪛㫀㫊㫋㪸㫅㪺㪼㪃㩷㫊
㪇
㪈㪉 㪇
㫅㪞㪈㪋㪅㪇
㪈㪉 㪈㪋
㪇 㪇 㪇 㪇 㪇 㪈 㪈 㪈 㪈 㪈 㪈
᳇ᵃᢙኒᐲ
T.E.
㪍 㪇 㪏㪅㪇 㪈㪇㪅㪇 㪈㪉㪅㪇
㪹㪼㫉㩷㪛㪼㫀㫅㫊㫀㫋㫐㪃㩷 㪍
㪏 㪈㪇
᳇ᵃᢙኒᐲ
⠀ᩮ⽶㕙䈮ᴪ䈦䈢
⠀ᩮ೨✼䈎䉌䈱〒㔌㫊
㪇 㪇 㪉㪅㪇 㪋㪅㪇 㪍㪅㪇
㪙㫌㪹㪹㫃㪼㩷㪥㫌㫄㪹
㪇 㪉 㪋 㪍
G G
G
r n
f � 4 �
3 㪇㪅㪇㪇㪅㪇 㪇㪅㪈 㪇㪅㪉 㪇㪅㪊 㪇㪅㪋 㪇㪅㪌 㪇㪅㪍 㪇㪅㪎 㪇㪅㪏 㪇㪅㪐 㪈㪅㪇 㪛㫀㫊㫋㪸㫅㪺㪼㪃㩷㫊
G 㪇 G
f
G3
䊗䉟䊄₸ ᳇ᵃᢙኒᐲ
㻟㻝
This document is provided by JAXA.