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Journal articles on the topic 'Liquid-liquid dispersion'

To see the other types of publications on this topic, follow the link: Liquid-liquid dispersion.

Author: Grafiati

Published: 4 June 2021

Last updated: 7 February 2022

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1

Pennemann, H., S. Hardt, V. Hessel, P. Löb, and F. Weise. "Micromixer Based Liquid/Liquid Dispersion." Chemical Engineering & Technology 28, no. 4 (April 2005): 501–8. http://dx.doi.org/10.1002/ceat.200407144.

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2

Nadiv, Corinne, and Raphael Semiat. "Batch Settling of Liquid-Liquid Dispersion." Industrial & Engineering Chemistry Research 34, no. 7 (July 1995): 2427–35. http://dx.doi.org/10.1021/ie00046a026.

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3

LI, Ming-Jie, Hong-Yi ZHANG, Xiao-Zhe LIU, Chun-Yan CUI, and Zhi-Hong SHI. "Progress of Extraction Solvent Dispersion Strategies for Dispersive Liquid-liquid Microextraction." Chinese Journal of Analytical Chemistry 43, no. 8 (August 2015): 1231–40. http://dx.doi.org/10.1016/s1872-2040(15)60851-9.

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4

Zhong, Qixin, and Minfeng Jin. "Zein nanoparticles produced by liquid–liquid dispersion." Food Hydrocolloids 23, no. 8 (December 2009): 2380–87. http://dx.doi.org/10.1016/j.foodhyd.2009.06.015.

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5

Jeelani, S. A. K., and S. Hartland. "Effect of Dispersion Properties on the Separation of Batch Liquid−Liquid Dispersions." Industrial & Engineering Chemistry Research 37, no. 2 (February 1998): 547–54. http://dx.doi.org/10.1021/ie970545a.

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6

Theron, Félicie, Nathalie Le Sauze, and Alain Ricard. "Turbulent Liquid−Liquid Dispersion in Sulzer SMX Mixer." Industrial & Engineering Chemistry Research 49, no. 2 (January 20, 2010): 623–32. http://dx.doi.org/10.1021/ie900090d.

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7

Skelland, A. H. P., and George G. Ramsay. "Minimum agitator speeds for complete liquid-liquid dispersion." Industrial & Engineering Chemistry Research 26, no. 1 (January 1987): 77–81. http://dx.doi.org/10.1021/ie00061a014.

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8

Kato, Satoru, Eiichi Nakayama, and Junjiro Kawasaki. "Types of dispersion in agitated liquid-liquid systems." Canadian Journal of Chemical Engineering 69, no. 1 (February 1991): 222–27. http://dx.doi.org/10.1002/cjce.5450690126.

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9

Habchi, Charbel, Thierry Lemenand, Dominique Della Valle, and Hassan Peerhossaini. "Liquid/liquid dispersion in a chaotic advection flow." International Journal of Multiphase Flow 35, no. 6 (June 2009): 485–97. http://dx.doi.org/10.1016/j.ijmultiphaseflow.2009.02.019.

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10

Machunsky, Stefanie, and Urs Alexander Peuker. "Liquid-Liquid Interfacial Transport of Nanoparticles." Physical Separation in Science and Engineering 2007 (January 8, 2007): 1–7. http://dx.doi.org/10.1155/2007/34832.

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The study presents the transfer of nanoparticles from the aqueous phase to the second nonmiscible nonaqueous liquid phase. The transfer is based on the sedimentation of the dispersed particles through a liquid-liquid interface. First, the colloidal aqueous dispersion is destabilised to flocculate the particles. The agglomeration is reversible and the flocs are large enough to sediment in a centrifugal field. The aqueous dispersion is laminated above the receiving organic liquid phase. When the particles start to penetrate into the liquid-liquid interface, the particle surface is covered with the stabilising surfactant. The sorption of the surfactant onto the surface of the primary particles leads to the disintegration of the flocs. This phase transfer process allows for a very low surfactant concentration within the receiving organic liquid, which is important for further application, that is, synthesis for polymer-nanocomposite materials. Furthermore, the phase transfer of the nanoparticles shows a high efficiency up to 100% yield. The particle size within the organosol corresponds to the primary particle size of the nanoparticles.

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11

Kolikov, Kiril Hristov, Dimo Donchev Hristozov, Radka Paskova Koleva, and Georgi Aleksandrov Krustev. "Model of Close Packing for Determination of the Major Characteristics of the Liquid Dispersions Components." Scientific World Journal 2014 (2014): 1–10. http://dx.doi.org/10.1155/2014/615236.

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We introduce a close packing model of the particles from the disperse phase of a liquid dispersion. With this model, we find the sediment volumes, the emergent, and the bound dispersion medium. We formulate a new approach for determining the equivalent radii of the particles from the sediment and the emergent (different from the Stokes method). We also describe an easy manner to apply algebraic method for determining the average volumetric mass densities of the ultimate sediment and emergent, as well as the free dispersion medium (without using any pycnometers or densitometers). The masses of the different components and the density of the dispersion phase in the investigated liquid dispersion are also determined by means of the established densities. We introduce for the first time a dimensionless scale for numeric characterization and therefore an index for predicting the sedimentation stability of liquid dispersions in case of straight and/or reverse sedimentation. We also find the quantity of the pure substance (without pouring out or drying) in the dispersion phase of the liquid dispersions.

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12

Goshika, Bharath Kumar, and Subrata Kumar Majumder. "Entrainment and holdup of gas-liquid-liquid dispersion in a downflow gas-liquid-liquid contactor." Chemical Engineering and Processing - Process Intensification 125 (March 2018): 112–23. http://dx.doi.org/10.1016/j.cep.2018.01.011.

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13

Fasano, Antonio, and Roberto Gianni. "Phase change of a two-component liquid–liquid dispersion." Nonlinear Analysis: Real World Applications 1, no. 4 (December 2000): 435–48. http://dx.doi.org/10.1016/s0362-546x(99)00103-0.

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14

Han, Shejiao, Jian Zhou, Yong Jin, Kai Chee Loh, and Zhanwen Wang. "Liquid dispersion in gas-liquid-solid circulating fluidized beds." Chemical Engineering Journal 70, no. 1 (May 1998): 9–14. http://dx.doi.org/10.1016/s1385-8947(98)00067-9.

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15

Sato, Masayuki, Norihisa Morita, Ikuyo Kuroiwa, Takayuki Ohshima, and Kuniko Urashima. "Dielectric liquid-in-liquid dispersion by applying pulsed voltage." IEEE Transactions on Dielectrics and Electrical Insulation 16, no. 2 (April 2009): 391–95. http://dx.doi.org/10.1109/tdei.2009.4815169.

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16

Legrand, J., P. Morançais, and G. Carnelle. "Liquid-Liquid Dispersion in an SMX-Sulzer Static Mixer." Chemical Engineering Research and Design 79, no. 8 (November 2001): 949–56. http://dx.doi.org/10.1205/02638760152721497.

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17

Das, Mainak D., Andrew N. Hrymak, and Malcolm H. I. Baird. "Laminar liquid–liquid dispersion in the SMX static mixer." Chemical Engineering Science 101 (September 2013): 329–44. http://dx.doi.org/10.1016/j.ces.2013.06.047.

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18

Saberian-Broudjenni, Mohamad, Gabriel Wild, and Sang Done Kim. "Liquid axial dispersion in gas—liquid—solid fluidized beds." Chemical Engineering Journal 40, no. 2 (March 1989): 83–92. http://dx.doi.org/10.1016/0300-9467(89)80049-8.

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19

Hawranek, J. P., W. Wrzeszcz, A. S. Muszyński, and M. Pajdowska. "Infrared dispersion of liquid triethylamine." Journal of Non-Crystalline Solids 305, no. 1-3 (July 2002): 62–70. http://dx.doi.org/10.1016/s0022-3093(02)01122-5.

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20

Hawranek, J. P., W. Wrzeszcz, and M. Pajdowska. "Infrared dispersion of liquid tripropylamine." Vibrational Spectroscopy 30, no. 1 (September 2002): 7–15. http://dx.doi.org/10.1016/s0924-2031(02)00033-4.

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21

Czarnecki, M. A., and J. P. Hawranek. "IR Dispersion of Liquid CD3CN." Zeitschrift für Physikalische Chemie 150, no. 1 (January 1986): 97–103. http://dx.doi.org/10.1524/zpch.1986.150.1.097.

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22

Fernández, V. I., A. Iucci, and C. M. Naón. "Luttinger liquid with asymmetric dispersion." European Physical Journal B 30, no. 1 (November 2002): 53–56. http://dx.doi.org/10.1140/epjb/e2002-00357-8.

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23

Cho, Y. J., P. S. Song, C. G. Lee, Y. Kang, S. D. Kim, and L. T. Fan. "Liquid Radial Dispersion in Liquid-solid Circulating Fluidized Beds with Viscous Liquid Medium." Chemical Engineering Communications 192, no. 3 (January 2005): 257–71. http://dx.doi.org/10.1080/00986440590473470.

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24

Hebrard, G., D. Bastoul, M. Roustan, M. P. Comte, and C. Beck. "Characterization of axial liquid dispersion in gas–liquid and gas–liquid–solid reactors." Chemical Engineering Journal 72, no. 2 (February 1999): 109–16. http://dx.doi.org/10.1016/s1385-8947(98)00151-x.

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25

Sovilj, Milan. "Hydrodynamics of gas-agitated liquid-liquid extraction columns." Acta Periodica Technologica, no. 43 (2012): 199–216. http://dx.doi.org/10.2298/apt1243199s.

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Although the non-agitated extraction columns (spray column, packed column, perforated plate column, sieve plate column, etc) can handle high flow rates and are simple and cheap, there have been relatively few applications of these columns because they suffer from serious backmixing of the continuous phase. It was shown that the backmixing is reduced when the spray column is operated with dense packing of drops. Another way of increasing the efficiency of a non-agitated extraction column is to introduce an inert gas (air, nitrogen, oxygen) as a mixing agent in the two-phase liquid-liquid (L-L) system. This method of energy introduction increases the turbulence within the new three-phase gas-liquid-liquid (G-L-L) system, which causes an improved dispersion of droplets, and, consequently, a higher dispersed phase holdup and therefore a great mass transfer area. The present study reports the hydrodynamics in the non-agitated extraction columns, as well as the axial dispersion for the two- and three-phase systems.

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26

Mukanov, Ruslan Vladimirovich, Vladimir Yakovlevich Svintsov, and Evgeniya Mikhaylovna Derbasova. "STUDY OF ELECTROSTATIC DISPERSION." Vestnik MGSU, no. 5 (May 2016): 130–39. http://dx.doi.org/10.22227/1997-0935.2016.5.130-139.

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The article deals with the problems of studying the process of dispersing liquid fuel and water-fuel emulsions, in particular the characteristics of the dispersed spray in high-potential electrostatic fields. The paper deals with the development of a research method for disperse characteristics of liquid fuels, in particular, the changes in the diameter of the spray particles of liquid fuels and water-fuel emulsions based on them, depending on the intensity of high-grade electrostatic field. These studies are relevant in the creation of new devices based on new dispersion, which are not currently used for fuel atomization and combustion devices, in particular based on the electrostatic dispersion. The currently available methods for assessing dispersion are based on the evaluation of the particle diameter, which are formed by dispersing (particle breakage) of the liquid fuel. The views expressed in the course of the study suggest that the dependence of the particle diameter from the electrostatic field can be estimated not only in case of the destruction of the particles (dispersion), but also in case of the formation (growth) of drops during the expiration of the capillary. In order to confirm the provisions the authors developed the installation and technique to study the changes in the dispersion in dependence with the voltage value of high potential electrostatic field. The results of experimental studies are presented and experimental graphics are built for F5 bunker fuel and water-oil emulsions with different concentrations based on it. On the basis of the experimental data processed by correlation analysis method the authors obtained the mathematical model of diameter changes of the particles under the influence of an electrostatic field, which corresponds to the theory of electrostatic dispersion. The developed technique greatly simplifies the determination of the disperse characteristics of liquid fuel in case of electro-static dispersion.

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27

Sovilj, Milan N., Branislava G. Nikolovski, and Momčilo Đ. Spasojević. "Hydrodynamics in spray and packed liquid-liquid extraction columns: A review." Macedonian Journal of Chemistry and Chemical Engineering 38, no. 2 (December 30, 2019): 267. http://dx.doi.org/10.20450/mjcce.2019.1519.

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This work provides a review of hydrodynamic characteristics such as the slip velocity, the dispersed-phase holdup, mean drop size, and axial dispersion of non-mechanically agitated liquid-liquid (L-L) extractors, with special reference to spray and packed bed columns. The complexity and importance of hydrodynamic behavior in designing and scaling up L-L extractors was a driving force to analyze, compare and discuss some important experimental findings available in the literature. The effects of phase velocities and the dispersed-phase holdup on the slip velocity, the mean drop size and the axial dispersion coefficient were studied and presented. Empirical correlations for slip velocity, the Sauter mean drop diameter and the axial dispersion coefficient, which were taken from the literature, were commented in terms of their applicability.

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28

Magiera, Robert, and Eckhart Blass. "Separation of liquid-liquid dispersion by flow through fibre beds." Filtration & Separation 34, no. 4 (May 1997): 369–76. http://dx.doi.org/10.1016/s0015-1882(97)90566-8.

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29

Nieves-Remacha, María José, Amol A. Kulkarni, and Klavs F. Jensen. "Hydrodynamics of Liquid–Liquid Dispersion in an Advanced-Flow Reactor." Industrial & Engineering Chemistry Research 51, no. 50 (December 4, 2012): 16251–62. http://dx.doi.org/10.1021/ie301821k.

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30

Zheng, Ying. "Axial liquid dispersion in a liquid-solid circulating fluidized bed." Canadian Journal of Chemical Engineering 79, no. 4 (August 2001): 564–69. http://dx.doi.org/10.1002/cjce.5450790414.

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31

Schmidt, J., R. Nassar, and A. Lübbert. "Local dispersion in the liquid phase of gas-liquid reactors." Chemical Engineering Science 47, no. 13-14 (September 1992): 3363–70. http://dx.doi.org/10.1016/0009-2509(92)85046-e.

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32

Oliynik, V. N. "Thermal Dispersion and Dissipation of a Sound in Concentrated Dispersion Liquid and Liquid-Gas Media." International Journal of Fluid Mechanics Research 30, no. 4 (2003): 443–61. http://dx.doi.org/10.1615/interjfluidmechres.v30.i4.70.

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33

Htet, Kyaw Myo, M. P. Glotova, and A. L. Galinovsky. "Innovative Research of Ultra-Jet Dispersion and Suspension Technologies for Processing and Modifying Liquids." Advanced Materials & Technologies, no. 3(19) (2020): 068–75. http://dx.doi.org/10.17277/amt.2020.03.pp.068-075.

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Currently used dispersion methods are not able to provide sufficient dispersion of nanomodifiers in liquids. This circumstance significantly reduces the effectiveness of the subsequent use of liquid-phase nanomodifiers which are widely used in the production of a variety of composite polymer and ceramic structures. The article discusses a new method of dispersing and suspending liquids using ultra-jet technology. The results of experimental testing confirming the effectiveness of ultra-jet technologies for producing liquid suspensions with nanomodifiers are presented. Two different types of powder were chosen as liquid modifiers: boehmite and carbon nanotubes. Moreover, special technological equipment was developed to conduct the experiment. The results of the analysis of the obtained liquid suspensions containing nanomodifiers allow us to recommend this dispersion technology for use on an industrial scale.

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34

Skelland, A. H. P., and Jeffrey S. Kanel. "Simulation of mass transfer in a batch agitated liquid-liquid dispersion." Industrial & Engineering Chemistry Research 31, no. 3 (March 1992): 908–20. http://dx.doi.org/10.1021/ie00003a037.

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35

Tan, J., Y. C. Lu, J. H. Xu, and G. S. Luo. "Modeling investigation of mass transfer of gas–liquid–liquid dispersion systems." Separation and Purification Technology 108 (April 2013): 111–18. http://dx.doi.org/10.1016/j.seppur.2013.01.010.

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36

Brujes, Luis, Jack Legrand, and Gerard Carnelle. "Characterization of Liquid-Liquid Dispersion in Batch and Continuous Toroiedal Minimixer." JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 36, no. 1 (2003): 1–6. http://dx.doi.org/10.1252/jcej.36.1.

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37

Kim, Sang D., Myung J. Lee, and Joo H. Han. "Axial dispersion characteristics of three (liquid-liquid-solid) phase fluidized beds." Canadian Journal of Chemical Engineering 67, no. 2 (April 1989): 276–82. http://dx.doi.org/10.1002/cjce.5450670214.

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38

Vikhansky, Alexander. "CFD modelling of turbulent liquid–liquid dispersion in a static mixer." Chemical Engineering and Processing - Process Intensification 149 (March 2020): 107840. http://dx.doi.org/10.1016/j.cep.2020.107840.

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39

Brás, Luís M. R., Elsa F. Gomes, Margarida M. M. Ribeiro, and M. M. L. Guimarães. "Drop Distribution Determination in a Liquid-Liquid Dispersion by Image Processing." International Journal of Chemical Engineering 2009 (2009): 1–6. http://dx.doi.org/10.1155/2009/746439.

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This paper presents the implementation of an algorithm for automatic identification of drops with different sizes in monochromatic digitized frames of a liquid-liquid chemical process. These image frames were obtained at our Laboratory, using a nonintrusive process, with a digital video camera, a microscope, and an illumination setup from a dispersion of toluene in water within a transparent mixing vessel. In this implementation, we propose a two-phase approach, using a Hough transform that automatically identifies drops in images of the chemical process. This work is a promising starting point for the possibility of performing an automatic drop classification with good results. Our algorithm for the analysis and interpretation of digitized images will be used for the calculation of particle size and shape distributions for modelling liquid-liquid systems.

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40

Yasunishi, Akira, Miki Fukuma, and Katsuhiko Muroyama. "Radial liquid dispersion in liquid-solid and three-phase fluidized beds." KAGAKU KOGAKU RONBUNSHU 13, no. 2 (1987): 208–15. http://dx.doi.org/10.1252/kakoronbunshu.13.208.

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41

Takeda, Kazuhiro, Kunimitsu Nakashima, Yoshifumi Tsuge, and Hisayoshi Matsuyama. "A Theoretical Model of Phase Inversion of Liquid-Liquid Dispersion Systems." KAGAKU KOGAKU RONBUNSHU 27, no. 3 (2001): 352–58. http://dx.doi.org/10.1252/kakoronbunshu.27.352.

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42

Zhao, W. Q., B. Y. Pu, and S. Hartland. "Measurement of drop size distribution in liquid/liquid dispersion by encapsulation." Chemical Engineering Science 48, no. 2 (January 1993): 219–27. http://dx.doi.org/10.1016/0009-2509(93)80010-n.

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43

Wang, Xueying, Kai Wang, Antoine Riaud, Xi Wang, and Guangsheng Luo. "Experimental study of liquid/liquid second-dispersion process in constrictive microchannels." Chemical Engineering Journal 254 (October 2014): 443–51. http://dx.doi.org/10.1016/j.cej.2014.05.135.

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44

Korchinsky, W. J. "A dispersion-entrainment model for liquid-liquid extraction column performance prediction." Chemical Engineering Science 43, no. 2 (1988): 349–54. http://dx.doi.org/10.1016/0009-2509(88)85047-4.

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45

Grandjean, B. P. A., P. J. Carreau, and J. Paris. "Comments on “Liquid axial dispersion in gas-liquid-solid fluidized beds." Chemical Engineering Journal 44, no. 1 (June 1990): 51–52. http://dx.doi.org/10.1016/0300-9467(90)80053-f.

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46

Wild, G., S. D. Kim, and M. Saberian-Broudjenni. "Comments on “Liquid axial dispersion in gas-liquid-solid fluidized beds." Chemical Engineering Journal 44, no. 1 (June 1990): 52. http://dx.doi.org/10.1016/0300-9467(90)80054-g.

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47

Mohan, S., V. Agarwala, and S. Ray. "Liquid-liquid dispersion for fabrication of AlPb metal-metal composites." Materials Science and Engineering: A 144, no. 1-2 (October 1991): 215–19. http://dx.doi.org/10.1016/0921-5093(91)90227-e.

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48

Hawranek, J. P., J. Z. Flejszar-Olszewska, and A. S. Muszyński. "Infrared dispersion of liquid sym-collidine." Journal of Molecular Structure 416, no. 1-3 (October 1997): 269–76. http://dx.doi.org/10.1016/s0022-2860(97)00054-9.

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49

Hawranek, J. P., A. S. Muszyński, and J. Z. Flejszar-Olszewska. "Infra-red dispersion of liquid trioctylamine." Journal of Molecular Structure 436-437 (December 1997): 605–12. http://dx.doi.org/10.1016/s0022-2860(97)00206-8.

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50

LIU Zhao-nan, 刘肇楠, 李抄 LI Chao, 夏明亮 XIA Ming-liang, 李大禹 LI Da-yu, and 宣丽 XUAN Li. "Dispersion of Liquid Crystal Wavefront Correctors." ACTA PHOTONICA SINICA 39, no. 6 (2010): 1014–20. http://dx.doi.org/10.3788/gzxb20103906.1014.

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