Journal articles: 'Interfacial area'

1

Ishii, Mamoru. "INTERFACIAL AREA MODELLING." Multiphase Science and Technology 3, no. 1-4 (1987): 31–61. http://dx.doi.org/10.1615/multscientechn.v3.i1-4.20.

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2

Millies, Marco, and Dieter Mewes. "Interfacial area density in bubbly flow." Chemical Engineering and Processing: Process Intensification 38, no. 4-6 (September 1999): 307–19. http://dx.doi.org/10.1016/s0255-2701(99)00022-7.

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3

Kataoka, Isao, and Akimi Serizawa. "Interfacial area concentration in bubbly flow." Nuclear Engineering and Design 120, no. 2-3 (June 1990): 163–80. http://dx.doi.org/10.1016/0029-5493(90)90370-d.

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4

Yarbro, Stephen L., and Richard L. Long. "Using a New Interfacial Area Transport Equation to Predict Interfacial Area in Co-current Jet Mixers." Canadian Journal of Chemical Engineering 80, no. 4 (May 19, 2008): 1–10. http://dx.doi.org/10.1002/cjce.5450800416.

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5

Tamhankar, Y., B. King, J. Whiteley, K. McCarley, T. Cai, M. Resetarits, and C. Aichele. "Interfacial area measurements and surface area quantification for spray absorption." Separation and Purification Technology 156 (December 2015): 311–20. http://dx.doi.org/10.1016/j.seppur.2015.10.017.

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6

Godinez-Brizuela, Omar E., Nikolaos K. Karadimitriou, Vahid Joekar-Niasar, Craig A. Shore, and Mart Oostrom. "Role of corner interfacial area in uniqueness of capillary pressure-saturation- interfacial area relation under transient conditions." Advances in Water Resources 107 (September 2017): 10–21. http://dx.doi.org/10.1016/j.advwatres.2017.06.007.

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7

Li, Muzi, Yuanzheng Zhai, and Li Wan. "Measurement of NAPL–water interfacial areas and mass transfer rates in two-dimensional flow cell." Water Science and Technology 74, no. 9 (August 19, 2016): 2145–51. http://dx.doi.org/10.2166/wst.2016.397.

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The nonaqueous-phase liquid (NAPL)–water interfacial area and the mass transfer rate across the NAPL and water interface are often key factors in in situ groundwater pollution treatment. In this study, the NAPL–water interfacial area and residual NAPL saturation were measured using interfacial and partitioning tracer tests in a two-dimensional flow cell. The results were compared with previous column and field experiment results. In addition, the mass transfer rates at various NAPL–water interfacial areas were investigated. Fe2+-activated persulfate was used for in situ chemical oxidation remediation to remove NAPL gradually. The results showed that the reduction of NAPL–water interfacial areas as well as NAPL saturation by chemical oxidation caused a linear decrease in the interphase mass transfer rates (R2 = 0.97), revealing the relationship between mass transfer rates and interfacial areas in a two-dimensional system. The NAPL oxidation rates decreased with the reduction of interfacial areas, owing to the control of NAPL mass transfer into the aqueous phase.

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8

Machnicki, Catherine E., Fanfan Fu, Lin Jing, Po-Yen Chen, and Ian Y. Wong. "Mechanochemical engineering of 2D materials for multiscale biointerfaces." Journal of Materials Chemistry B 7, no. 41 (2019): 6293–309. http://dx.doi.org/10.1039/c9tb01006h.

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Atomically thin nanomaterials that are wrinkled or crumpled represent a unique paradigm for interfacing with biological systems due to their mechanical flexibility, exceptional interfacial area, and ease of chemical functionalization.

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9

Ishii, M., S. S. Paranjape, S. Kim, and X. Sun. "Interfacial structures and interfacial area transport in downward two-phase bubbly flow." International Journal of Multiphase Flow 30, no. 7-8 (July 2004): 779–801. http://dx.doi.org/10.1016/j.ijmultiphaseflow.2004.04.009.

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10

Bartel, Michael D., Mamoru Ishii, Takuyki Masukawa, Ye Mi, and Rong Situ. "Interfacial area measurements in subcooled flow boiling." Nuclear Engineering and Design 210, no. 1-3 (December 2001): 135–55. http://dx.doi.org/10.1016/s0029-5493(01)00415-0.

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11

Hibiki, Takashi, and Mamoru Ishii. "Interfacial area concentration of bubbly flow systems." Chemical Engineering Science 57, no. 18 (September 2002): 3967–77. http://dx.doi.org/10.1016/s0009-2509(02)00263-4.

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12

LONG, R. L., and P. REIMUS. "INTERFACIAL AREA PRODUCTION AT A TEE JUNCTION." Chemical Engineering Communications 111, no. 1 (January 1992): 1–12. http://dx.doi.org/10.1080/00986449208935977.

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13

Liu, Chenhan, Zhiyong Wei, Jian Wang, Kedong Bi, Juekuan Yang, and Yunfei Chen. "The contact area dependent interfacial thermal conductance." AIP Advances 5, no. 12 (December 2015): 127111. http://dx.doi.org/10.1063/1.4937775.

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14

KATAOKA, Isao. "Development of Research on Interfacial Area Transport." Journal of Nuclear Science and Technology 47, no. 1 (January 2010): 1–19. http://dx.doi.org/10.1080/18811248.2010.9711923.

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15

Revankar, S. T., and M. Ishii. "Local interfacial area measurement in bubbly flow." International Journal of Heat and Mass Transfer 35, no. 4 (April 1992): 913–25. http://dx.doi.org/10.1016/0017-9310(92)90257-s.

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16

Aprahamian, Edward, Frederick F. Cantwell, and Henry Freiser. "Measurement of interfacial adsorption and interfacial area in vigorously stirred solvent extraction systems." Langmuir 1, no. 1 (January 1985): 79–82. http://dx.doi.org/10.1021/la00061a012.

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17

Dave, A. J., A. Manera, M. Beyer, D. Lucas, and H. M. Prasser. "Uncertainty analysis of an interfacial area reconstruction algorithm and its application to two group interfacial area transport equation validation." Nuclear Engineering and Design 310 (December 2016): 620–37. http://dx.doi.org/10.1016/j.nucengdes.2016.10.038.

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18

Watanabe, T., and K. Ebihara. "Numerical Simulation of Droplet Flows and Evaluation of Interfacial Area." Journal of Fluids Engineering 124, no. 3 (August 19, 2002): 576–83. http://dx.doi.org/10.1115/1.1490128.

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Droplet flows with coalescence and breakup are simulated numerically using the lattice Boltzmann method. It is shown that the rising velocities are in good agreement with those obtained by the force balance and the empirical correlation. The breakup of droplets after coalescence is simulated well in terms of the critical Weber number. A numerical method to evaluate the interfacial area and the volume fraction in two-phase flows is proposed. It is shown that the interfacial area corresponds to the shape, the number and the size of droplets, and the proposed method is effective for numerical evaluation of interfacial area even if the interface changes dynamically.

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19

Hibiki, Takashi, Tatsuya Hazuku, Tomoji Takamasa, and Mamoru Ishii. "Interfacial-Area Transport Equation at Reduced-Gravity Conditions." AIAA Journal 47, no. 5 (May 2009): 1123–31. http://dx.doi.org/10.2514/1.38208.

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20

Hibiki, Takashi, Mamoru Ishii, and Zheng Xiao. "Axial interfacial area transport of vertical bubbly flows." International Journal of Heat and Mass Transfer 44, no. 10 (May 2001): 1869–88. http://dx.doi.org/10.1016/s0017-9310(00)00232-5.

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21

Hibiki, Takashi, and Mamoru Ishii. "Interfacial Area Transport Equations for Gas-Liquid Flow." Journal of Computational Multiphase Flows 1, no. 1 (January 2009): 1–22. http://dx.doi.org/10.1260/175748209787387089.

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22

Hibiki, Takashi, Tae Ho Lee, Jae Young Lee, and Mamoru Ishii. "Interfacial area concentration in boiling bubbly flow systems." Chemical Engineering Science 61, no. 24 (December 2006): 7979–90. http://dx.doi.org/10.1016/j.ces.2006.09.009.

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23

Maceiras, R., E. Álvarez, and M. A. Cancela. "Experimental interfacial area measurements in a bubble column." Chemical Engineering Journal 163, no. 3 (October 2010): 331–36. http://dx.doi.org/10.1016/j.cej.2010.08.011.

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24

Skoczylas, A., and W. Majewski. "Effective interfacial area in mechanical thin-layer apparatus." Chemical Engineering Journal 46, no. 2 (June 1991): 69–78. http://dx.doi.org/10.1016/0300-9467(91)80025-r.

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25

Hazuku, Tatsuya, Tomoji Takamasa, Takashi Hibiki, and Mamoru Ishii. "Interfacial area concentration in annular two-phase flow." International Journal of Heat and Mass Transfer 50, no. 15-16 (July 2007): 2986–95. http://dx.doi.org/10.1016/j.ijheatmasstransfer.2007.01.017.

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26

Hazuku, Tatsuya, Yutaka Fukuhara, Tomoji Takamasa, and Takashi Hibiki. "ICONE19-44014 APPLICABILITY OF INTERFACIAL AREA TRANSPORT EQUATION TO BUBBLY TWO-PHASE FLOWS UNDER MICROGRAVIT." Proceedings of the International Conference on Nuclear Engineering (ICONE) 2011.19 (2011): _ICONE1944. http://dx.doi.org/10.1299/jsmeicone.2011.19._icone1944_8.

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27

Hibiki, T., S. Hogsett, and M. Ishii. "Local measurement of interfacial area, interfacial velocity and liquid turbulence in two-phase flow." Nuclear Engineering and Design 184, no. 2-3 (August 1998): 287–304. http://dx.doi.org/10.1016/s0029-5493(98)00203-9.

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28

Wang, Guanyi, Zhuoran Dang, Peng Ju, Xiaohong Yang, Mamoru Ishii, Andrew Ireland, Stephen Bajorek, and Matthew Bernard. "Experimental study on interfacial structure and interfacial area transport in downward two-phase flow." International Journal of Heat and Mass Transfer 106 (March 2017): 1303–17. http://dx.doi.org/10.1016/j.ijheatmasstransfer.2016.10.112.

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29

Jiang, Bingyan, Yang Zou, Guomeng Wei, and Wangqing Wu. "Evolution of Interfacial Friction Angle and Contact Area of Polymer Pellets during the Initial Stage of Ultrasonic Plasticization." Polymers 11, no. 12 (December 14, 2019): 2103. http://dx.doi.org/10.3390/polym11122103.

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Interfacial friction heating is one of the leading heat generation mechanisms during the initial stage of ultrasonic plasticization of polymer pellets, which has a significant influence on the subsequent viscoelastic heating according to our previous study. The interfacial friction angle and contact area of polymer pellets are critical boundary conditions for the analysis of interfacial frictional heating of polymer pellets. However, the duration of the interfacial friction heating is extremely short in ultrasonic plasticization, and the polymer pellets are randomly distributed in the cylindrical barrel, resulting in the characterization of the distribution of the interfacial friction angle and contact area to be a challenge. In this work, the interfacial friction angle of the polymer pellets in the partially plasticized samples of polymethyl methacrylate (PMMA), polypropylene (PP), and nylon66 (PA66) were characterized by a super-high magnification lens zoom 3D microscope. The influence of trigger pressure, plasticizing pressure, ultrasonic amplitude, and vibration time on the interfacial friction angle and the contact area of the polymer pellets were studied by a single factor experiment. The results show that the compaction degree of the plasticized samples could be enhanced by increasing the level of the process parameters. With the increasing parameter level, the proportion of interfacial friction angle in the range of 0–10° and 80–90° increased, while the proportion in the range of 30–60° decreased accordingly. The proportion of the contact area of the polymer pellets was increased up to 50% of the interfacial friction area which includes the upper, lower, and side area of the cylindrical plasticized sample.

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30

Pelipenko, Jan, Julijana Kristl, Romana Rošic, Saša Baumgartner, and Petra Kocbek. "Interfacial rheology: An overview of measuring techniques and its role in dispersions and electrospinning." Acta Pharmaceutica 62, no. 2 (June 1, 2012): 123–40. http://dx.doi.org/10.2478/v10007-012-0018-x.

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Interfacial rheology: An overview of measuring techniques and its role in dispersions and electrospinning Interfacial rheological properties have yet to be thoroughly explored. Only recently, methods have been introduced that provide sufficient sensitivity to reliably determine viscoelastic interfacial properties. In general, interfacial rheology describes the relationship between the deformation of an interface and the stresses exerted on it. Due to the variety in deformations of the interfacial layer (shear and expansions or compressions), the field of interfacial rheology is divided into the subcategories of shear and dilatational rheology. While shear rheology is primarily linked to the long-term stability of dispersions, dilatational rheology provides information regarding short-term stability. Interfacial rheological characteristics become relevant in systems with large interfacial areas, such as emulsions and foams, and in processes that lead to a large increase in the interfacial area, such as electrospinning of nanofibers.

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31

Almoslh, Adel, Falah Alobaid, Christian Heinze, and Bernd Epple. "Influence of Pressure on Gas/Liquid Interfacial Area in a Tray Column." Applied Sciences 10, no. 13 (July 3, 2020): 4617. http://dx.doi.org/10.3390/app10134617.

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The influence of pressure on the gas/liquid interfacial area is investigated in the pressure range of 0.2–0.3 MPa by using a tray column test rig. A simulated waste gas, which consisted of 30% CO2 and 70% air, was used in this study. Distilled water was employed as an absorbent. The temperature of the inlet water was 19 °C. The inlet volumetric flow rate of water was 0.17 m3/h. Two series of experiments were performed; the first series was performed at inlet gas flow rate 15 Nm3/h, whereas the second series was at 20 Nm3/h of inlet gas flow rate. The results showed that the gas/liquid interfacial area decreases when the total pressure is increased. The effect of pressure on the gas/liquid interfacial area at high inlet volumetric gas flow rates is more significant than at low inlet volumetric gas flow rates. The authors studied the effect of decreasing the interfacial area on the performance of a tray column for CO2 capture.

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32

Shen, Xiuzhong, and Takashi Hibiki. "ICONE23-1795 TWO-GROUP INTERFACIAL AREA CONCENTRATION CORRELATIONS OF TWO-PHASE FLOWS IN LARGE DIAMETER PIPES." Proceedings of the International Conference on Nuclear Engineering (ICONE) 2015.23 (2015): _ICONE23–1—_ICONE23–1. http://dx.doi.org/10.1299/jsmeicone.2015.23._icone23-1_384.

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33

Wang, Jian Giang, Ke Dong Bi, and Yun Fei Chen. "Molecular Dynamic Simulations of Contact Thermal Resistance between Two Individual Silicon Nanowires." Key Engineering Materials 483 (June 2011): 663–67. http://dx.doi.org/10.4028/www.scientific.net/kem.483.663.

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Contact thermal resistance between two individual silicon nanowires is investigated by nonequilibrium molecular dynamic simulations as a function of temperature, overlap, bonding strength and spacing between them. The results indicate that contact thermal resistance per unit area increases with temperature increasing. The increasing overlap leads to the increase of the contact areas, which enhances the per unit area contact thermal resistance. With a weakened interfacial van der Waals bonding strength, the contact thermal resistance per unit area increases significantly. Additionally, a method to verify the effect of the bonding strength is used by changing the interfacial spacing, and a reasonable result is observed.

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34

Hibiki, Takashi, and Mamoru Ishii. "Interfacial area concentration in steady fully-developed bubbly flow." International Journal of Heat and Mass Transfer 44, no. 18 (September 2001): 3443–61. http://dx.doi.org/10.1016/s0017-9310(00)00365-3.

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35

Ishii, M., S. Kim, and J. Uhle. "Interfacial area transport equation: model development and benchmark experiments." International Journal of Heat and Mass Transfer 45, no. 15 (July 2002): 3111–23. http://dx.doi.org/10.1016/s0017-9310(02)00041-8.

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36

Takamasa, T., T. Iguchi, T. Hazuku, T. Hibiki, and M. Ishii. "Interfacial area transport of bubbly flow under microgravity environment." International Journal of Multiphase Flow 29, no. 2 (February 2003): 291–304. http://dx.doi.org/10.1016/s0301-9322(02)00129-5.

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37

Ende, David J., Roger E. Eckert, and Lyle F. Albright. "Interfacial Area of Dispersions of Sulfuric Acid and Hydrocarbons." Industrial & Engineering Chemistry Research 34, no. 12 (December 1995): 4343–50. http://dx.doi.org/10.1021/ie00039a026.

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38

Noh, Tae-Geun, Yongsug Tak, Jae-Do Nam, and Hyoukryeol Choi. "Electrochemical characterization of polymer actuator with large interfacial area." Electrochimica Acta 47, no. 13-14 (May 2002): 2341–46. http://dx.doi.org/10.1016/s0013-4686(02)00089-0.

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39

Quadros, Paulo A., and Cristina M. S. G. Baptista. "Effective interfacial area in agitated liquid–liquid continuous reactors." Chemical Engineering Science 58, no. 17 (September 2003): 3935–45. http://dx.doi.org/10.1016/s0009-2509(03)00302-6.

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40

Wu, Q., S. Kim, M. Ishii, and S. G. Beus. "One-group interfacial area transport in vertical bubbly flow." International Journal of Heat and Mass Transfer 41, no. 8-9 (April 1998): 1103–12. http://dx.doi.org/10.1016/s0017-9310(97)00167-1.

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41

Potůček, František. "The specific interfacial area in an airlift tower reactor." Collection of Czechoslovak Chemical Communications 55, no. 4 (1990): 981–86. http://dx.doi.org/10.1135/cccc19900981.

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This study deals with the oxygen transfer in the gas-liquid dispersion systems. The sulfite oxidation method was used to determine the specific interfacial area in the airlift tower reactor with and without motionless mixers. The experimental results obtained were described by the correlation equations and compared with those already published in the literature.

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42

Ishii, Mamoru. "LOCAL MEASUREMENT OF INTERFACIAL AREA IN TWO-PHASE FLOW." Annual Review of Heat Transfer 6, no. 6 (1995): 271–321. http://dx.doi.org/10.1615/annualrevheattransfer.v6.70.

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43

Wang, Jun, Yixin Leng, Hui Shao, Weiming Li, and Chunxiang Huang. "Prediction of gas-liquid interfacial area in valve trays." AIChE Journal 62, no. 3 (October 22, 2015): 905–15. http://dx.doi.org/10.1002/aic.15065.

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44

Patel, Snehal A., James G. Daly, and Dragomir B. Bukur. "Holdup and interfacial area measurements using dynamic gas disengagement." AIChE Journal 35, no. 6 (June 1989): 931–42. http://dx.doi.org/10.1002/aic.690350606.

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45

Bandyopadhyay, Amitava, and Manindra Nath Biswas. "Determination of interfacial area in a tapered bubble column." Journal of Chemical Technology & Biotechnology 86, no. 9 (April 26, 2011): 1211–25. http://dx.doi.org/10.1002/jctb.2635.

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46

Yang, C., B. N. J. Persson, J. Israelachvili, and K. Rosenberg. "Contact mechanics with adhesion: Interfacial separation and contact area." EPL (Europhysics Letters) 84, no. 4 (November 2008): 46004. http://dx.doi.org/10.1209/0295-5075/84/46004.

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47

Liu, Hang, Jianyong Lai, Yi Li, Haojie Huang, Liangming Pan, and Wenxiong Zhou. "INTERFACIAL AREA CORRELATION FOR ANNULAR FLOW IN VERTICAL PIPES." Proceedings of the International Conference on Nuclear Engineering (ICONE) 2019.27 (2019): 1987. http://dx.doi.org/10.1299/jsmeicone.2019.27.1987.

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48

Tan, M. J., and M. Ishii. "A method for measurement of local specific interfacial area." International Journal of Multiphase Flow 16, no. 2 (March 1990): 353–58. http://dx.doi.org/10.1016/0301-9322(90)90064-p.

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49

Delhaye, J. M., and P. Bricard. "Interfacial area in bubbly flow: experimental data and correlations." Nuclear Engineering and Design 151, no. 1 (November 1994): 65–77. http://dx.doi.org/10.1016/0029-5493(94)90034-5.

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50

Dłuska, E., S. Wroński, and T. Ryszczuk. "Interfacial area in gas–liquid Couette–Taylor flow reactor." Experimental Thermal and Fluid Science 28, no. 5 (April 2004): 467–72. http://dx.doi.org/10.1016/j.expthermflusci.2003.06.003.

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Journal articles on the topic 'Interfacial area'

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