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Search DetailsKURIMOTO RyoGraduate School of Engineering / Department of Mechanical EngineeringAssistant Professor
Research activity information
■ Award- Aug. 2023 日本混相流学会, 日本混相流学会学会賞 論文賞, 鉛直管におけるフラッディング状態での管内流動特性
- Aug. 2018 日本混相流学会, 日本混相流学会学会賞 奨励賞, マイクロチャネル内気液二相スラグ流に関する研究Japan society
- Apr. 2012 KOBE UNIVERSITY, OUTSTANDING STUDENT AWARDOthers
- Mar. 2011 神戸大学機械クラブ, 機械クラブ国際活動奨励賞Others
- Mar. 2011 日本機械学会, 日本機械学会三浦賞Others
- Abstract Interface tracking simulations of gas–liquid Taylor flow in horizontal square microchannels were carried out to understand the relation between the pressure drop in the bubble part and the curvatures at the nose and tail of a bubble. Numerical conditions ranged for 0.00159 ≤ CaT ≤ 0.0989, 0.0817 ≤ WeT ≤ 25.4, and 8.33 ≤ ReT ≤ 791, where CaT, WeT, and ReT are the capillary, Weber, and Reynolds numbers based on the total volumetric flux. The dimensionless pressure drop in the bubble part increased with increasing the capillary number and the Weber number. The curvature at the nose of a bubble increased and that at the tail of a bubble decreased as the capillary number increased. The variation of the curvature at the tail of a bubble was more remarkable than that at the nose of a bubble due to the increase in the Weber number, which was the main cause of large pressure drop in the bubble part at the same capillary number. The relation between the bubble velocity and the total volumetric flux was also discussed. The distribution parameter of the drift-flux model without inertial effects showed a simple relation with the capillary number. A correlation of the distribution parameter, which is expressed in terms of the capillary number and the Weber number, was developed and was confirmed to give good predictions of the bubble velocity.Springer Science and Business Media LLC, Jul. 2024, Microfluidics and Nanofluidics, 28, 58[Refereed]Scientific journal
- Elsevier BV, Jul. 2024, Chemical Engineering Science, 299, 120557[Refereed]Scientific journal
- Elsevier BV, Apr. 2024, Chemical Engineering Research and Design, 204, 343 - 353[Refereed]Scientific journal
- Corresponding, Begell House, 2024, Multiphase Science and Technology, 36(2) (2), 55 - 73[Refereed]Scientific journal
- Elsevier BV, Dec. 2023, Chemical Engineering Research and Design, 200, 776 - 785[Refereed]Scientific journal
- The Japanese Society for Multiphase Flow, Nov. 2023, JAPANESE JOURNAL OF MULTIPHASE FLOW, 37(4) (4), 401 - 411[Refereed]Scientific journal
- Nov. 2023, 12th International Symposium on Measurement Techniques for Multiphase FlowDrag coefficients of particle-covered bubbles produced using a microchannel[Refereed]
- Nov. 2023, 12th International Symposium on Measurement Techniques for Multiphase FlowMeasurements of surfactant amount at the gas-liquid interface in comtaminated Taylor flows in a microchannel[Refereed]
- Corresponding, Nov. 2023, 12th International Symposium on Measurement Techniques for Multiphase FlowEffects of surfactant on bubbly flow in narrow rectangular column[Refereed]
- The Japanese Society for Multiphase Flow, Oct. 2023, JAPANESE JOURNAL OF MULTIPHASE FLOW, 37(4) (4), 392 - 400[Refereed]Scientific journal
- Corresponding, Elsevier BV, Oct. 2023, Nuclear Engineering and Design, 412, 112476 - 112476[Refereed]Scientific journal
- Informa UK Limited, Mar. 2023, Heat Transfer Engineering, 45(4-5) (4-5), 323 - 336[Refereed]Scientific journal
- Corresponding, The Japanese Society for Multiphase Flow, Jan. 2023, JAPANESE JOURNAL OF MULTIPHASE FLOW, 37(1) (1), 128 - 137[Refereed]Scientific journal
- Begell House, 2023, Multiphase Science and Technology, 35(2) (2), 29 - 41[Refereed]Scientific journal
- The Japanese Society for Multiphase Flow, Dec. 2022, JAPANESE JOURNAL OF MULTIPHASE FLOW, 36(4) (4), 440 - 451[Refereed]Scientific journal
- Corresponding, Nov. 2022, 2022 ANS Winter Meeting and Technology ExpoEffects of upper and lower pipe ends on interfacial and wall friction factors under counter-current flow limitation in a vertical pipe[Refereed]
- Corresponding, Nov. 2022, 2022 ANS Winter Meeting and Technology ExpoEffects of liquid viscosity on friction factors of gas-liquid swirling annular flows in a vertical pipe[Refereed]
- Oct. 2022, 12th Japan-Korea Symposium on Nuclear Thermal Hydraulics and SafetyMeasurements of void fractions in spherical particle beds under pool conditions[Refereed]
- Oct. 2022, 12th Japan-Korea Symposium on Nuclear Thermal Hydraulics and SafetyFlow chracteristics in a vertical pipe with sharp-edged top and vottom ends under flooding conditions[Refereed]
- Corresponding, Elsevier BV, Oct. 2022, Nuclear Engineering and Design, 399, 112001 - 112001[Refereed]Scientific journal
- Elsevier BV, Jul. 2022, Experimental Thermal and Fluid Science, 139, 110735 - 110735[Refereed]Scientific journal
- Elsevier BV, May 2022, 12th Japan-U.S. Seminar on Two-Phase Flow Dynamics 2022Effects of swirl intensity on interfacial and wall friction factors of annular flows in a vertical pipe[Refereed]International conference proceedings
- Begell House, 2022, Multiphase Science and Technology, 34(4) (4), 41 - 55[Refereed]Scientific journal
- Corresponding, Begell House, 2022, Multiphase Science and Technology, 34(4) (4), 1 - 13[Refereed]Scientific journal
- Begell House, 2022, Multiphase Science and Technology, 34(2) (2), 67 - 82[Refereed]Scientific journal
- Begell House, 2022, Multiphase Science and Technology, 34(1) (1), 53 - 66[Refereed]Scientific journal
- Begell House, 2021, Multiphase Science and Technology, 33(4) (4), 1 - 13[Refereed]Scientific journal
- Begell House, 2021, Multiphase Science and Technology, 33(3) (3), 53 - 66[Refereed]Scientific journal
- The Japanese Society for Multiphase Flow, 2021, Japanese Journal of Multiphase Flow, 35(3) (3), 463 - 472[Refereed]Scientific journal
- Begell House, 2021, Multiphase Science and Technology, 33(2) (2), 87 - 101[Refereed]Scientific journal
- Elsevier BV, 2021, Chemical Engineering Science, 245, 116852 - 116852[Refereed]Scientific journal
- The Japanese Society for Multiphase Flow, 2021, Japanese Journal of Multiphase Flow, 35(1) (1), 85 - 92[Refereed]Scientific journal
- Elsevier BV, 2021, Nuclear Engineering and Design, 373, 111020 - 111020[Refereed]Scientific journal
- Wiley, 2021, Chemie Ingenieur Technik, 93(1-2) (1-2), 247 - 259[Refereed]Scientific journal
- Lead, Begell House, 2020, Multiphase Science and Technology, 32(3) (3), 221 - 236[Refereed]Scientific journal
- Springer Science and Business Media LLC, Jan. 2020, Microfluidics and Nanofluidics, 24(1) (1), 5[Refereed]Scientific journal
- Nov. 2019, 12th Pacific Symposium on Flow Visualization and Image Processing, 5 pages, EnglishA study on the reduction of wave resistance using wave interference by trimaran[Refereed]International conference proceedings
- May 2019, 10th International Conference on Multiphase Flow, 2pages, EnglishEffects of surfactant on bubble breakup at T-junction and characteristics of Taylor flow of mini- and micro-channels[Refereed]International conference proceedings
- May 2019, 10th International Conference on Multiphase Flow, 2pages, EnglishPressure drop of gas-liquid Taylor flow in square microchannels[Refereed]International conference proceedings
- Begell House, 2019, Multiphase Science and Technology, 31(3) (3), 273 - 286[Refereed]Scientific journal
- Study Group of Aero Aqua Bio-mechanics, 2019, Journal of Aero Aqua Bio-mechanisms, 8(1) (1), 13 - 19[Refereed]Scientific journal
- Springer Science and Business Media LLC, 2019, Flow, Turbulence and Combustion, 102(2) (2), 435 - 455[Refereed]Scientific journal
- Oct. 2018, 13th International Symposium on Advanced Science and Technology in Experimental Mechanics, 6 pages, EnglishExperimental study on gas-liquid Taylor flow in rectangular microchannels[Refereed]International conference proceedings
- Oct. 2018, 13th International Symposium on Advanced Science and Technology in Experimental Mechanics, 6 pages, EnglishA Study on the Wing Performance and the Passive Separation Control of Two Tandem Arranged NACA0012 Wing using Leading Edge Protuberance in Low Reynolds Number[Refereed]International conference proceedings
- Sep. 2018, 実験力学, 18(3) (3), 214 - 221, Japanese[Refereed]Scientific journal
- Study Group of Aero Aqua Bio-mechanics, Sep. 2018, 7th International Symposium on Aero-aqua Bio-Mechanisms, English[Refereed]International conference proceedings
- Elsevier BV, 2018, International Journal of Heat and Fluid Flow, 74, 28 - 35[Refereed]Scientific journal
- Dec. 2017, 実験力学, 17(4) (4), 298 - 303, Japanese[Refereed]Scientific journal
- Dec. 2017, 10th International Symposium on Measurement Techniques for Multiphase Flow, ISMTMF-R001-102, 2 pages, EnglishVoid fraction and pressure drop measurement of gas-liquid slug flow in square microchannels[Refereed]International conference proceedings
- The void fraction and pressure drop of gas-liquid slug flow in a circular microchannel were measured using a high-speed video camera and image processing method. Water and two types of glycerol water solutions were used as the liquid phase, and N-2 gas was used as the gas phase. Four microchannels with different diameters (200, 320, 500, and 700 mu m) were used. The measured data were compared with the existing and newly developed models. The following conclusions were obtained: (1) the pressure drop was predicted using the model proposed by Warnier et al. (2010) with the liquid film thickness model proposed by Han and Shikazono (2009) within +/- 20%, (2) a distribution parameter model developed in this study can predict the distribution parameter within +/- 10% and is more reliable than the other models. (C) 2017 Elsevier Inc. Alt rights reserved.ELSEVIER SCIENCE INC, Nov. 2017, EXPERIMENTAL THERMAL AND FLUID SCIENCE, 88, 124 - 133, English[Refereed]Scientific journal
- Oct. 2017, The 6th International Conference on Jets, Wakes and Separated Flows 6pages, EnglishTHE EFFECT OF THE REYNOLDS NUMBER ON THE PERFORMANCE OF THE NACA0012 WING WITH THE LEADING EDGE PROTUBERANCE AT LOW REYNOLDS NUMBERS[Refereed]International conference proceedings
- Nov. 2016, 11th International Symposium on Advanced Science and Technology in Experimental Mechanics, 5 pages, EnglishVelocity and shape of single bubble in horizontal cylindrical channel[Refereed]International conference proceedings
- The effects of surfactant on quasi-static bubble growth from an orifice of 2.0 mm in diameter were investigated by using a high-speed video camera and an image processing method. Triton X-100 was used for surfactant and its concentrations were set at 0.0, 0.1, 0.3, 0.5 and 1.0 mol/m(3). To obtain further knowledge of the bubble growth in the clean and contaminated systems, the flow fields around the bubbles were measured by using particle image velocimetry (PIV). The conclusions obtained are as follows: (1) the increase rate of the bubble aspect ratio in the contaminated system almost agrees with that in the clean system before reaching a specific bubble volume, and becomes larger after that, (2) as the surfactant concentration increases, the smallest contact angle increases and the bubble volume at the smallest contact angle decreases; furthermore, the bubble volume at the branch point of the contact angle between the clean and contaminated systems nearly agrees with that at the branch point of the aspect ratio, (3) the surfactant does not affect the flow fields around the growing bubbles in the experiment. (c) 2016 Elsevier B.V. All rights reserved.ELSEVIER SCIENCE SA, Jun. 2016, CHEMICAL ENGINEERING AND PROCESSING, 104, 154 - 159, English[Refereed]Scientific journal
- Effects of microbubbles on germination and growth in deep flow technique of spinach (Spinacia oleracea) were investigated. In the germination experiment, four experiment plots; (1) underwater germination with microbubble water plot (MB plot), (2) underwater germination with aerated water plot (Aeration plot), (3) underwater germination with water plot (Water plot), (4) germination on wet cotton plot (Control plot), were used. Two hundred individuals were germinated for each plot. Germination rate of MB plot after 7 days was about twice as high as that of Aeration plot and Control plot. In the growth experiment, three experiment plots; (1) tenth solution concentration water with microbubble plot (MB plot), (2) tenth solution concentration water plot (Aeration plot), (3) full solution concentration water plot (Control plot), were used. Twelve individuals were grown for each plot. Leaves weight of MB plot was as much as that of Control plot. In contrast, plant physiological disorders appeared in all plants of Aeration plot. Multi-element determination revealed that K concentration of Aeration plot was lower than that of the others plots. These results indicate that microbubbles contribute to the plants absorbing the nutrient from roots.The Japanese Society for Experimental Mechanics, Mar. 2016, Journal of the Japanese Society for Experimental Mechanics, 16(1) (1), 77 - 83, Japanese[Refereed]Scientific journal
- Oct. 2015, 7th European-Japanese Two-Phase Flow Group Meeting, 12 pages, EnglishEFFECT OF EXTERNAL ELECTRIC FIELD ON SPREADING OF A LIQUID DROPLET AT LOW CAPILLARY NUMBER REGIME: EXPERIMENTAL EVIDENCES AND NUMERICAL SIMULATION[Refereed]International conference proceedings
- Aug. 2014, Proc. of the 15th International Heat Transfer Conference, IHTC-15, IHTC15-08960, 11pages, EnglishBubble growth in microgravity under the action of electric forces: experiments and numerical simulation[Refereed]International conference proceedings
- Japan Society of Mechanical Engineers, 2014, Transactions of the JSME (in Japanese), 80(817) (817), FE0259 - FE0259[Refereed]Scientific journal
- In the present paper, a study of bubble dynamics in adiabatic conditions (i.e. with no heat and mass transfer) is carried out in order to understand the fundamental physics ruling the evolution of their interface, and open the way to the comprehension of more complex heat and mass transfer issues involving them. An external electric field is applied to the system to investigate the potentiality of this technique to enhance phase separation and heat transfer. A new numerical method for EHD action on a growing bubble has been developed combining VOF and level-set methods. To experimentally validate it, well-defined and simple boundary conditions have been selected: all the forms of heat and mass transfer have been excluded from the system, and an axisymmetric electric field configuration has been chosen in order to adopt a 2-D simulation. In the experimental apparatus a steady bubble stemming from an orifice in a still fluid (FC-72) has been produced, and a dc potential up to 20. kV was applied to a ring-shaped electrode coaxial with the orifice. In this way, in a first instance, all the dynamical effects have been eliminated, and a clear location of the three phase contact line, which is pinned to the orifice, has been defined. The bubble profile obtained from the experiment has been digitized and compared successfully with the outcomes of the numerical method. Furthermore, the study of the local curvature of the interface allowed the development of a new theory of the local electrical stress to be included in the capillary equation, which compares well with experimental data. Finally, the validated numerical method has been used to predict the bubble shape in the absence of gravity, in preparation of microgravity experiments. © 2013 Elsevier Inc.Sep. 2013, Experimental Thermal and Fluid Science, 49, 160 - 168, English[Refereed]Scientific journal
- Terminal velocities and shapes of drops rising through vertical pipes in clean and fully-contaminated systems are measured by using a high-speed video camera and an image processing method. Silicon oils and glycerol water solutions are used for the dispersed and continuous phases, respectively. Triton X-100 is used for surfactant. Clean and contaminated drops take either spherical, spheroidal or deformed spheroidal shapes when the diameter ratio λ is less than a critical value, λC, whereas they take bullet shapes for λ> λC (Taylor drops). The applicability of available drag and Froude number correlations is examined through comparisons with the measured data. Effects of surfactant on the shape and terminal velocity of a Taylor drop are also discussed based on the experimental data and interface tracking simulations. The conclusions obtained are as follows: (1) drag and Froude number correlations proposed so far give reasonable estimations of the terminal velocities of clean drops at any λ, (2) the terminal velocities of contaminated drops are well evaluated by making the viscosity ratio μ* infinity in the drag correlation for clean drops in the viscous force dominant regime, (3) the effects of surfactant on the shape and terminal velocity of a Taylor drop become significant as the Eötvös number, EoD, decreases and μ* increases, and (4) the reduction in surface tension due to the addition of surfactant would be the cause of the increase in the terminal velocity and elongation of a contaminated Taylor drop. © 2012 Elsevier Ltd.Mar. 2013, International Journal of Multiphase Flow, 49, 8 - 23, English[Refereed]Scientific journal
- Jun. 2012, 2012 Japan-U.S. seminar on Two-Phase flow Dynamics, 10pages, EnglishEffects of Surfactant on the Motion of Bubbles in Linear Shear FlowsInternational conference proceedings
- A scaling analysis based on the field equations for two phases and the jump conditions at the interface is carried out to deduce a balance of forces acting on a Taylor drop rising through stagnant liquid in a vertical pipe. The force balance is utilized to deduce a functional form of an empirical correlation of terminal velocity of the Taylor drop. Undetermined coefficients in the correlation are evaluated by making use of available correlations for two limiting cases, i.e. extremely high and low Reynolds number Taylor bubbles in large pipes. Terminal velocity data obtained by interface tracking simulations are also used to determine the coefficients. The proposed correlation expresses the Froude number Fr as a function of the drop Reynolds number Re-D, the Eotvos number Eo(D) and the viscosity ratio mu*. Comparisons between the correlation, simulations and experimental data confirm that the proposed correlation is applicable to Taylor drops under various conditions, i.e., 0.002 < Re-D < 4960, 4.8 < Eo(D) < 228, 0 <= mu* <= 70, 1 < N < 14700, -12 < log M < 4, and d/D < 1.6, where N is the inverse viscosity number, M the Morton number, d the sphere-volume equivalent drop diameter and D the pipe diameter. (C) 2010 Elsevier Ltd. All rights reserved.PERGAMON-ELSEVIER SCIENCE LTD, Apr. 2011, INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 37(3) (3), 241 - 251, English[Refereed]Scientific journal
- An interface tracking method for predicting motions of bubbles contaminated with soluble surfactants is presented. A level set method is utilized to track the interface. Transportations of surfactants in the bulk liquid and those at the interface are taken into account. The amount of adsorption and desorption is evaluated by using the Frumkin & Levich model. Simulations of bubbles contaminated with soluble surfactants are carried out, i.e., single air bubbles rising through stagnant water, Taylor bubbles in a vertical pipe filled with water, and a wobbling bubble in a vertical duct. As a result, the following conclusions are obtained: (1) the increase in drag coefficients of spherical bubbles due to the presence of surfactant, i.e. Marangoni effect, is well predicted, (2) surfactants mainly accumulate at the rear edge of a Taylor bubble and the Marangoni effect is very small in the nose region at high Eötvös and low Morton numbers, and therefore, the effects of surfactant on the bubble rising velocity are small in low viscosity systems, and (3) the surfactant concentration is low in the top region of a wobbling bubble, whereas it is high in the bottom region. The peak concentration appears at the side edge of the bubble and the location of the peak concentration moves with the bubble and wake movements. Copyright © 2011 by ASME.2011, ASME-JSME-KSME 2011 Joint Fluids Engineering Conference, AJK 2011, 1(D) (D), 1641 - 1650, English[Refereed]International conference proceedings
- May 2010, Proc. of International Conference on Multiphase Flow ICMF2010, 11pages, EnglishTerminal velocity of a single drop in a vertical pipe in clean and fully-contaminated systems[Refereed]International conference proceedings
- May 2010, Proc. of International Conference on Multiphase Flow ICMF2010, 13pages, EnglishTerminal velocity of a Taylor drop in a vertical pipe[Refereed]International conference proceedings
- An empirical correlation of the terminal velocity of a Taylor bubble in a vertical pipe is proposed. A fundamental functional form, Fr = f (Re D, EoD), of the correlation is deduced by carrying out a dimensional analysis based on the local instantaneous field equations and the jump conditions. Here Fr is the Froude number, ReD the bubble Reynolds number, and EoD the Eötvös number. In the two limiting cases, (EoD →∞ and ReD →∞) and (EoD →∞ and ReD → 0), the deduced functional form approaches those of the well-known Fr models. Coefficients appearing in the correlation are determined by making use of the limiting cases and available experimental data. Comparisons between the proposed Fr correlation and the experimental data show that the correlation gives a good estimation of terminal velocities of Taylor bubbles for a wide range of fluid properties and pipe diameters, i.e., 10-7 < ReD < 104, 4 < EoD < 3 × 103, 10-2 < N < 105, and -11 < log M < 10, where N is the inverse viscosity number and M the Morton number. © 2010 by Begell House, Inc.2010, Multiphase Science and Technology, 22(3) (3), 197 - 210, English[Refereed]Scientific journal
- Interface tracking simulations of single drops rising through a vertical pipe are carried out using three coordinate systems, i.e. cylindrical, general curvilinear and Cartesian coordinates, to investigate the effects of coordinate system and spatial resolution on the accuracy of predictions. Experiments of single drops in a vertical pipe are also conducted to obtain experimental data for comparisons with simulations. The drop shape observed are spheroidal and deformed spheroidal at low values of the diameter ratio, Λ, of the sphere-volume equivalent diameter of a drop to the pipe diameter, whereas they take bullet-shapes at large Λ. The conclusions obtained are as follows: (1) the effects of coordinate system on drop shape are small at low Λ. At large Λ, the effects are also small for drops in a low viscosity system, whereas non-physical shape distortion takes place when the Cartesian coordinates are used with low spatial resolution for drops in a high viscosity system, and (2) the drop terminal velocity and the velocity profile in the liquid film between a bullet-shaped drop and a pipe wall are well predicted using all the coordinate systems tested even at low spatial resolution.SAGE Publications, 2010, The Journal of Computational Multiphase Flows, 2(1) (1), 47 - 57, English[Refereed]Scientific journal
- Sep. 2009, 5th European Two-Phase Flow Group Meeting , 6pages, EnglishDimensional Analysis of Terminal Velocity of a Taylor Bubble in a Vertical PipeInternational conference proceedings
- 日本混相流学会, Mar. 2014, 混相流, 27(5) (5), 102 - 105, JapaneseFluid Engineering Laboratory, Department of Mechanical Systems Engineering, School of Engineering, The University of Shiga Prefecture
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024堆積層内気液二相流の流動特性に関する研究
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024鉛直円管内旋回環状流内体積率及び圧力損失の一次元三流体モデルによる予測
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024フラッディング状態での鉛直管内流動特性に対する管径の影響
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024停滞水条件における3×3ロッドバンドル内での界面摩擦
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024気泡塔内非均質気泡流におけるドリフトフラックスパラメータの検討
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024気泡塔内ボイド率に及ぼす初期液位依存性に関する研究
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024Experimental analysis of bubble terminal velocity in fiber bundle
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024平板間静止液中を上昇する単一気泡の形状及び抗力係数
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024鉛直円管内テイラー気泡の液膜厚さに加振が及ぼす影響に関する研究
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024平板間静止液中単一気泡の形状及び上昇速度に関する研究
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024鉛直細円柱群内の気泡の上昇運動に関する研究
- 日本混相流学会 混相流シンポジウム2024, Sep. 2024微細流路内テイラー気泡の形状に及ぼす界面活性剤の影響
- 第67回理論応用力学講演会, Sep. 2024正方形マイクロチャネル内テイラー流の圧力損失と気泡速度に関する研究
- IUTAM Symposium on Dynamics and Interface Phenomena of Bubbles and Droplets at Multiple Scales, Dec. 2023Surface Coverage of Bubbles with Surfactant or Particles[Invited]
- 日本混相流学会 混相流シンポジウム2023, Aug. 2023鉛直管におけるフラッディング状態での管内流動特性[Invited]
- 日本混相流学会 混相流シンポジウム2023, Aug. 2023鉛直管でのフラッディング状態における気液界面摩擦係数
- 日本混相流学会 混相流シンポジウム2023, Aug. 2023停滞水条件における3x3ロッドバンドル内での流動特性
- 日本混相流学会 混相流シンポジウム2023, Aug. 2023微細流路を用いた粒子付着気泡の生成と抗力係数の評価
- 日本混相流学会 混相流シンポジウム2023, Aug. 2023微細流路内汚染系テイラー流における気泡への界面活性剤吸着量に関する研究
- 日本混相流学会 混相流シンポジウム2023, Aug. 2023U字管内気液二相流のボイド率に及ぼすベンド曲率の影響
- 日本混相流学会 混相流シンポジウム2023, Aug. 2023鉛直円管内旋回環状流の界面及び壁面摩擦係数に及ぼす管径の影響に関する研究
- ASME-JSME-KSME Joint Fluids Engineering Conference AJKFED 2023, Jul. 2023Effects of fine particles and surfactant on bubbly flows in narrow rectangular column
- 11th International Conference on Multiphase Flow, Apr. 2023Bubbly flows in a column with submerged hollow fiber membranes
- 日本機械学会関西支部第98期定時総会講演会, Mar. 2023中空糸膜を有する塔内気泡流に関する研究
- 日本原子力学会熱流動部会 第4回若手研究者勉強会, Nov. 2022鉛直円管内気液二相対向流の界面及び壁面摩擦係数に及ぼす管端形状の影響
- 日本原子力学会熱流動部会 第4回若手研究者勉強会, Nov. 2022鉛直円管内旋回環状流の摩擦係数に及ぼす液相動粘度の影響
- European-American-Japanese Two-Phase Flow Group Meeting, Oct. 2022Bubbly flows in a column with submerged hollow fiber membranes
- 4th International Symposium on Multiscale Multiphase Process Engineering, Sep. 2022Bubbly flows in a vertical pipe with horizontal oscillation
- 4th International Symposium on Multiscale Multiphase Process Engineering, Sep. 2022Pressure drop of single bubble in Taylor flow through square microchannels
- 日本原子力学会2022年秋の大会, Sep. 2022上下端シャープエッジ鉛直管におけるフラッディング状態での流動特性
- 日本混相流学会混相流シンポジウム2022, Aug. 2022正方形流路内テイラー流における気泡の圧力損失に関する研究
- 日本混相流学会混相流シンポジウム2022, Aug. 2022鉛直円管内気液二相対向流の界面及び壁面摩擦係数に及ぼす管端形状の影響
- 日本混相流学会混相流シンポジウム2022, Aug. 2022鉛直円管内旋回環状流の界面及び壁面摩擦係数に及ぼす旋回強度及び液相粘度の影響
- 日本混相流学会混相流シンポジウム2022, Aug. 2022狭平板間静止液中単一気泡の分裂に関する研究
- 第8回複雑熱流体工学研究センターシンポジア, Nov. 2021マイクロチャネル内気液二相流の実験的・数値的研究
- 日本原子力学会2021年秋の大会, Sep. 2021鉛直管上端フラッディングでの流動特性に対する上部タンク水位の影響
- 日本混相流学会混相流シンポジウム2021, Aug. 2021気泡流による中空糸膜の汚れ除去と揺動に関する研究
- 日本混相流学会混相流シンポジウム2021, Aug. 2021Lベンド通過後の鉛直細管内環状流の液膜厚さ推移に関する研究
- 日本混相流学会混相流シンポジウム2021, Aug. 2021気泡塔内平均及び局所ボイド率の初期液位依存性に関する研究
- 日本混相流学会混相流シンポジウム2021, Aug. 2021振動を伴う鉛直円管内の気液二相流動特性に関する研究
- 日本混相流学会混相流シンポジウム2021, Aug. 2021堆積層内における気液二相流に関する研究
- 日本混相流学会混相流シンポジウム2021, Aug. 2021鉛直円管内気液二相流の界面および壁面摩擦係数に及ぼす旋回強度の影響
- 日本混相流学会混相流シンポジウム2021, Aug. 2021垂直U字管内気液二相流のボイド率に関する研究
- 日本混相流学会混相流シンポジウム2021, Aug. 2021鉛直サーペンタイン管内気液二相流のボイド率及び液膜厚さ
- 日本混相流学会混相流シンポジウム2020, Aug. 2020Study on effects of acceleration of a vertical pipe on two-phase flows in the pipe
- 日本混相流学会混相流シンポジウム2020, Aug. 2020Study on chemisorption from single bubbles rising through alkaline solutions in a vertical pipe
- 日本混相流学会混相流シンポジウム2020, Aug. 2020Effects of liquid viscosity on interfacial and wall friction factors of gas-liquid two-phase swirling flows in a vertical pipe
- 日本混相流学会混相流シンポジウム2020, Aug. 2020Study on annular flows in circular pipe with L-shaped bend
- 日本機械学会関西支部第95期定時総会講演会, Mar. 2020, Japanese, Domestic conference狭平行平板間を上昇する気泡の運動に関する研究Poster presentation
- 11th International Symposium on Measurement Techniques for Multiphase Flow, Nov. 2019Numerical simulation of air-water two-phase flow in pipes with branch junction
- 日本機械学会2019年度年次大会, Sep. 2019, Japanese, Domestic conference低Re数領域における直列配置されたNACA0012翼周りの流れと翼性能に関する研究Oral presentation
- 日本機械学会2019年度年次大会, Sep. 2019, Japanese, Domestic conferenceエアーノズルで発生する流体騒音の低減に関する研究Oral presentation
- 日本混相流学会混相流シンポジウム2019, Aug. 2019, Japanese, Domestic conference正方形マイクロチャネル内気液二相スラグ流の圧力損失Oral presentation
- 日本機械学会第96期流体工学部門講演会, Nov. 2018, Japanese, Domestic conference進行波を利用したポンプの性能評価に関する研究Oral presentation
- 日本機械学会第96期流体工学部門講演会, Nov. 2018, Japanese, Domestic conference前縁波形状翼を用いた翼性能の改善に関する研究(前縁波形状翼の有効範囲の検討)Oral presentation
- 混相流シンポジウム2018, Aug. 2018, Japanese, Domestic conference矩形マイクロチャネル内気液二相テイラー流に関する研究Oral presentation
- 混相流シンポジウム2018, Aug. 2018, Japanese, Domestic conferenceゼータ電位の異なるマイクロバブルがコマツナの生育に与える影響(生育実験と元素分析)Oral presentation
- 8th European-Japanese Two-Phase Flow Group Meeting, Apr. 2018Pressure drop and void fraction of gas-liquid Taylor flow in square microchannels
- 日本機械学会関西支部第93期定時総会講演会, Mar. 2018, Japanese, Domestic conference振動平板ポンプの開発および性能評価に関する研究Poster presentation
- 日本機械学会関西支部第93期定時総会講演会, Mar. 2018, Japanese, Domestic conference前縁波形状翼を用いた翼性能の改善に関する研究(翼キャンバーの影響)Poster presentation
- 2017年度日本機械学会年次大会, Sep. 2017, Japanese, Domestic conference低レイノルズ数領域で用いる前縁波形状翼の最適な形状に関する研究Oral presentation
- 園芸学会平成29年度秋季大会, Sep. 2017, Japanese, Domestic conferencepHが異なる低濃度培養液でのマイクロバブル処理が水耕コマツナの生育に及ぼす影響Oral presentation
- 混相流シンポジウム2017, Aug. 2017, Japanese, Domestic conference清浄及び汚染系におけるマイクロチャネル内気液二相スラグ流に関する研究Oral presentation
- 混相流シンポジウム2017, Aug. 2017, Japanese, Domestic conferenceマイクロバブルのゼータ電位がコマツナの生育に及ぼす影響Oral presentation
- 53rd European Two-Phase Flow Group Meeting, May 2017Bubble growth from an orifice under the action of electric forces
- 日本機械学会関西支部第92期定時総会講演会, Mar. 2017, Japanese, Domestic conferenceマイクロバブル水洗浄に関する基礎研究Oral presentation
- 日本機械学会関西支部第92期定時総会講演会, Mar. 2017, Japanese, Domestic conferenceマイクロチューブ内気液二相スラグ流に関する研究Oral presentation
- 日本機械学会関西支部第92期定時総会講演会, Mar. 2017, Japanese, Domestic conference低レイノルズ数領域における前縁波形状翼を用いた翼性能の向上に関する研究Poster presentation
- 日本機械学会関西支部第92期定時総会講演会, Mar. 2017, Japanese, Domestic conference水平管内を流れる気泡に関する研究Poster presentation
- 日本機械学会関西支部第92期定時総会講演会, Mar. 2017, Japanese, Domestic conferenceマイクロバブルがサラダナの生育に与える影響Poster presentation
- 日本機械学会関西支部第92期定時総会講演会, Mar. 2017, Japanese, Domestic conference水平加熱平板からの自然対流に及ぼす電場の影響Poster presentation
- 日本機械学会2016年度年次大会, Sep. 2016, Japanese, Domestic conferenceエアバキュームクリーナーのエジェクター部形状が性能におよぼす影響Oral presentation
- 日本機械学会関西支部第91期定時総会講演会, Mar. 2016, Japanese, Domestic conferenceマイクロチューブ内気液二相スラグ流に関する研究(管内径と粘度による影響)Oral presentation
- 混相流シンポジウム2015, Aug. 2015, Japanese, Domestic conferenceマイクロバブルがホウレンソウの発芽および生育に与える影響Oral presentation
- 混相流シンポジウム2015, Aug. 2015, Japanese, Domestic conferenceマイクロバブルの白濁に関する研究Oral presentation
- 混相流シンポジウム2015, Aug. 2015, Japanese, Domestic conferenceマイクロバブルの発生方法の違いおよび界面活性剤の有無によるゼータ電位への影響Oral presentation
- 混相流シンポジウム2015, Aug. 2015, Japanese, Domestic conference固体表面上を拡大する液滴に及ぼす外部電場の影響Oral presentation
- 日本機械学会関西支部第90期定時総会講演会, Mar. 2015, Japanese, Domestic conferenceマイクロチューブ内気液二相スラグ流に関する研究(高粘度流体を用いた場合)Poster presentation
- 日本機械学会流体工学部門講演会, Oct. 2014, Japanese, Domestic conference低レイノルズ数領域で用いる水中グライダーの最適な翼形状に関する研究(最適な翼前縁形状の調査)Oral presentation
- 混相流シンポジウム2014, Jul. 2014, Japanese, Domestic conference非一様電場におけるオリフィスからの気泡成長Oral presentation
- 混相流シンポジウム2014, Jul. 2014, Japanese, Domestic conferenceマイクロチューブ内気液二相スラグ流の摩擦損失(ユニット・セル・モデルの適用)Oral presentation
- 混相流シンポジウム2014, Jul. 2014, Japanese, Domestic conferenceマイクロバブルがトマトの生育に与える影響Oral presentation
- 日本機械学会流体工学部門講演会, Nov. 2013, Japanese, Domestic conferenceマイクロバブルによる鉛直管内流の摩擦抵抗低減効果Oral presentation
- 6th Japanese-European Two-Phase Flow Group Meeting, Sep. 2012Bubble growth under the action of electric forces: Experiments and numerical simulation
- 50th European Two-Phase Flow Group Meeting, May 2012Numerical simulation of bubble growth under the action of electric forces
- 日本混相流学会年会講演会2011, Aug. 2011, Japanese, Domestic conference可溶性界面活性剤の吸脱着を伴う気泡の界面追跡計算Oral presentation
- 日本混相流学会年会講演会2010, Jul. 2010, Japanese, Domestic conference鉛直円管内テイラー液滴の終端上昇速度相関式Oral presentation
- 日本混相流学会年会講演会2009, Aug. 2009, Japanese, Domestic conference鉛直円管内単一大液滴の終端上昇速度に関する研究Oral presentation
■ Research Themes
- 日本学術振興会, 科学研究費助成事業 基盤研究(C), 基盤研究(C), 神戸大学, 01 Apr. 2023 - 31 Mar. 2026密な鉛直物体群内外における気泡流構造の解明と数値予測技術の開発
- 公益財団法人 JKA, 2022年度 機械振興補助事業 研究補助 複数年研究, 神戸大学, 2022 - 2023微細粒子及び界面活性剤分散液中気泡流の流動解明と数値予測技術の開発補助事業
- Japan Society for the Promotion of Science, Grants-in-Aid for Scientific Research Grant-in-Aid for Early-Career Scientists, Grant-in-Aid for Early-Career Scientists, Kobe University, Apr. 2020 - Mar. 2022Development of numerical method for interaction of flexible structures and bubbly flowNumerical simulation would be useful for design and development of membrane bioreactors (MBR) in the view of visualization and prediction of flow in MBR plants. Experimental data on a relation between motion of membraned and bubbly flow are lacking, although motion of membranes should be implemented in the numerical simulation. We carried out experiments to observe bubbly flow, measure removal rate of a sludge and evaluate motion of membranes in an experimental setup with hollow fiber membranes. Liquid property affects bubble break-up at a lower tie plate and membranes. Liquid property affects the number of bubbles and those diameter in bubbly flows, since frequency of bubble break-up occurring at lower tie plate and membranes varies. This variation of the structure of bubbly flows affects removal rate attached to sludge.
- 公益財団法人 前川報恩会, 2019年度学術研究助成, 神戸大学, 2020ベンドを有する円管内における気液二相環状流の液膜推移に関する研究
- 公益財団法人 JKA, 2019年度 機械振興補助事業 研究補助 若手研究, 滋賀県立大学, 2019鉛直平行平板流路内気泡の非定常後流の解明補助事業
- 公益財団法人 関西エネルギー・リサイクル科学研究振興財団, 平成28年度研究助成, 滋賀県立大学, 2017微細流路混相反応器開発のための微細流路内固気液三相流の流動特性に関する研究