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Journal articles on the topic 'Mass transfer'

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Published: 4 June 2021
Last updated: 14 September 2024

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1

Gekas, Vassilis. "Mass transfer modeling." Journal of Food Engineering 49, no. 2-3 (August 2001): 97–102. http://dx.doi.org/10.1016/s0260-8774(00)00223-5.

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2

Wesselingh, J. A. "Multicomponent Mass Transfer." Chemical Engineering Journal and the Biochemical Engineering Journal 60, no. 1-3 (December 1995): 177–79. http://dx.doi.org/10.1016/0923-0467(96)80015-7.

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3

Garofalo, Paolo S. "Mass transfer during gold precipitation within a vertically extensive vein network (Sigma deposit - Abitibi greenstone belt - Canada). Part II. Mass transfer calculations." European Journal of Mineralogy 16, no. 5 (October 18, 2004): 761–76. http://dx.doi.org/10.1127/0935-1221/2004/0016-0761.

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4

Nakhman, A. D., and Yu V. Rodionov. "Generalized Solution of the Heat and Mass Transfer Problem." Advanced Materials & Technologies, no. 4 (2017): 056–63. http://dx.doi.org/10.17277/amt.2017.04.pp.056-063.

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5

Hosovkyi, Roman, Diana Kindzera, and Volodymyr Atamanyuk. "Diffusive Mass Transfer during Drying of Grinded Sunflower Stalks." Chemistry & Chemical Technology 10, no. 4 (September 15, 2016): 459–63. http://dx.doi.org/10.23939/chcht10.04.459.

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Diffusive mass transfer has been studied during drying of grinded sunflower stalks to produce fuel briquettes. Theoretical aspects of diffusive processes during filtration drying have been analyzed. The process of diffusive mass transfer during drying of grinded sunflower stalks particles of prismatic shape has been mathematically described. The temperature effect on effective diffusion coefficient has been examined.
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6

Wogelius, Roy A., Peter M. Morris, Michael A. Kertesz, Emmanuelle Chardon, Alexander I. R. Stark, Michele Warren, and James R. Brydie. "Mineral surface reactivity and mass transfer in environmental mineralogy." European Journal of Mineralogy 19, no. 3 (July 2, 2007): 297–307. http://dx.doi.org/10.1127/0935-1221/2007/0019-1727.

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7

Coulson, J. M., J. F. Richardson, J. R. Backhurst, and J. H. Harker. "Fluid flow, heat transfer and mass transfer." Filtration & Separation 33, no. 2 (February 1996): 102. http://dx.doi.org/10.1016/s0015-1882(96)90353-5.

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8

Wu, Kinwah. "Mass Transfer in Low Mass Close Binaries." International Astronomical Union Colloquium 163 (1997): 283–88. http://dx.doi.org/10.1017/s0252921100042755.

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AbstractThe mass transfer process in low mass close binaries is reviewed. The driving mechanisms and the stability properties are discussed by means of general, simple formulations. A model in terms of mass transfer instabilities is suggested to explain the outbursts of GRO J1655–40 in 1994.
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9

Kobayashi, Takeshi. "Immobilization and mass transfer." Japan journal of water pollution research 9, no. 11 (1986): 696–98. http://dx.doi.org/10.2965/jswe1978.9.696.

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10

COLLINS II, G. W., J. C. BROWN, and J. P. CASSINELLI. "Dynamical mass-transfer paradox." Nature 347, no. 6292 (October 1990): 433. http://dx.doi.org/10.1038/347433a0.

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11

Sardeing, R., J. Aubin, and C. Xuereb. "Gas–Liquid Mass Transfer." Chemical Engineering Research and Design 82, no. 12 (December 2004): 1589–96. http://dx.doi.org/10.1205/cerd.82.12.1589.58030.

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12

Sardeing, R., J. Aubin, M. Poux, and C. Xuereb. "Gas–Liquid Mass Transfer." Chemical Engineering Research and Design 82, no. 9 (September 2004): 1161–68. http://dx.doi.org/10.1205/cerd.82.9.1161.44158.

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13

Chesnokov, V. M. "Mass Transfer in Liquids." Theoretical Foundations of Chemical Engineering 39, no. 4 (July 2005): 419–24. http://dx.doi.org/10.1007/s11236-005-0097-1.

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14

Yang, Yuqi, Matthew D. Biviano, Jixiang Guo, Joseph D. Berry, and Raymond R. Dagastine. "Mass transfer between microbubbles." Journal of Colloid and Interface Science 571 (July 2020): 253–59. http://dx.doi.org/10.1016/j.jcis.2020.02.120.

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15

Sucharov, Lance. "Heat and mass transfer." Advances in Water Resources 14, no. 1 (February 1991): 50. http://dx.doi.org/10.1016/0309-1708(91)90031-i.

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16

Fitt, V., J. R. Ockendon, and M. Shillor. "Counter-current mass transfer." International Journal of Heat and Mass Transfer 28, no. 4 (April 1985): 753–59. http://dx.doi.org/10.1016/0017-9310(85)90225-x.

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17

Vieil, E., K. Meerholz, T. Matencio, and J. Heinze. "Mass transfer and convolution." Journal of Electroanalytical Chemistry 368, no. 1-2 (April 1994): 183–91. http://dx.doi.org/10.1016/0022-0728(93)03110-b.

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18

Hansel, Armin. "Proton Transfer Mass Spectrometer." Europhysics News 35, no. 6 (November 2004): 197–99. http://dx.doi.org/10.1051/epn:2004606.

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19

Quitzsch, K. "Heat and Mass Transfer." Zeitschrift für Physikalische Chemie 212, Part_2 (January 1999): 236–38. http://dx.doi.org/10.1524/zpch.1999.212.part_2.236.

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20

Weatherley, Laurence R. "Electrically enhanced mass transfer." Heat Recovery Systems and CHP 13, no. 6 (November 1993): 515–37. http://dx.doi.org/10.1016/0890-4332(93)90004-f.

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21

Brites, Ana Maria, and Maria Norberta de Pinho. "Mass transfer in ultrafiltration." Journal of Membrane Science 61 (January 1991): 49–63. http://dx.doi.org/10.1016/0376-7388(91)80005-q.

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22

Ivanova, Natalia, Surjakanta Kundu, and Ali Pourmand. "Unified Rapid Mass Transfer." Astrophysical Journal 971, no. 1 (August 1, 2024): 64. http://dx.doi.org/10.3847/1538-4357/ad583e.

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Abstract We present a method to obtain rapid mass-loss rates in binary systems, specifically at the onset of mass transfer (MT) episodes. The method unifies atmospheric (underflow) and L 1 stream (overflow) mass rates in a single continuous procedure. The method uses averaged 3D properties of the binaries, such as effective binary potential and effective binary acceleration, to both evolve the donor and obtain properties of the matter at the L 1 plane. In the case of underflow, we obtain atmospheric stratification. Our method can be used for binaries with an extensive range of mass ratios, 0.01 ≤ q ≤ 100, and can also be applied to hot donors. The considered examples show that the MT rates obtained with this revised formalism always differ from the optically thin and optically thick MT rates widely used during the computations of binary evolution.
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23

S. K. Abbouda, P. A. Seib, D. S. Chung, and A. Song. "Heat and Mass Transfer in Stored Milo. Part II. Mass Transfer Model." Transactions of the ASAE 35, no. 5 (1992): 1575–80. http://dx.doi.org/10.13031/2013.28770.

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24

Kunze, Anna-Katharina, Philip Lutze, Manuela Kopatschek, Jan F. Maćkowiak, Jerzy Maćkowiak, Marcus Grünewald, and Andrzej Górak. "Mass transfer measurements in absorption and desorption: Determination of mass transfer parameters." Chemical Engineering Research and Design 104 (December 2015): 440–52. http://dx.doi.org/10.1016/j.cherd.2015.08.025.

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25

Rhim, Jung A., and Jeong Hyo Yoon. "Mass transfer characteristics and overall mass transfer coefficient in the ozone contactor." Korean Journal of Chemical Engineering 22, no. 2 (March 2005): 201–7. http://dx.doi.org/10.1007/bf02701485.

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26

Iliuta, Ion, Maria C. Iliuta, and Fernand C. Thyrion. "Gas-liquid mass transfer in trickle-bed reactors: Gas-side mass transfer." Chemical Engineering & Technology 20, no. 9 (December 1997): 589–95. http://dx.doi.org/10.1002/ceat.270200904.

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27

Barna, Iryna, Yaroslav Gumnytskyi, and Volodymyr Atamanyuk. "Intradiffusion Mass Transfer during Drying of Slag Gravel Raw Granule." Chemistry & Chemical Technology 7, no. 4 (December 15, 2013): 461–65. http://dx.doi.org/10.23939/chcht07.04.461.

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28

Dyachok, Vasyl, Serhiy Huhlych, Yuri Yatchyshyn, Yulia Zaporochets, and Viktoriia Katysheva. "About the Problem of Biological Processes Complicated by Mass Transfer." Chemistry & Chemical Technology 11, no. 1 (March 15, 2017): 111–16. http://dx.doi.org/10.23939/chcht11.01.111.

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29

Gichan, O. I. "Dynamic instabilities on a charged boundary: influence of mass transfer." Reports of the National Academy of Sciences of Ukraine, no. 10 (November 16, 2016): 47–53. http://dx.doi.org/10.15407/dopovidi2016.10.047.

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30

Durand, Cyril, Emilien Oliot, Didier Marquer, and Jean-Pierre Sizun. "Chemical mass transfer in shear zones and metacarbonate xenoliths: a comparison of four mass balance approaches." European Journal of Mineralogy 27, no. 6 (December 14, 2015): 731–54. http://dx.doi.org/10.1127/ejm/2015/0027-2475.

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31

Pongayi Ponnusamy Selvi and Rajoo Baskar, Pongayi Ponnusamy Selvi and Rajoo Baskar. "Mass Transfer Enhancement for CO2 Absorption in Structured Packed Absorption Column." Journal of the chemical society of pakistan 41, no. 5 (2019): 820. http://dx.doi.org/10.52568/000803/jcsp/41.05.2019.

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The acidic gas, Carbon dioxide (CO2) absorption in aqueous ammonia solvent was carried as an example for industrial gaseous treatment. The packed column was provided with a novel structured BX-DX packing material. The overall mass transfer coefficient was calculated from the absorption efficiency of the various runs. Due to the high solubility of CO2, mass transfer was shown to be mainly controlled by gas side transfer rates. The effects of different operating parameters on KGav including CO2 partial pressure, total gas flow rates, volume flow rate of aqueous ammonia solution, aqueous ammonia concentration, and reaction temperature were investigated. For a particular system and operating conditions structured packing provides higher mass transfer coefficient than that of commercial random packing.
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32

Selim, A. M., and M. M. Elsayed. "Interfacial mass transfer and mass transfer coefficient in aqua ammonia packed bed absorber." International Journal of Refrigeration 22, no. 4 (June 1999): 263–74. http://dx.doi.org/10.1016/s0140-7007(98)00073-5.

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33

Cheremisinoff, N. P. "Handbook of heat and mass transfer, Vol. 2: Mass transfer and reactor design." Chemical Engineering Science 42, no. 10 (1987): 2494. http://dx.doi.org/10.1016/0009-2509(87)80132-x.

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34

Horvath, E., E. Nagy, C. Boyadjiev, and J. Gyenis. "Interphase mass transfer between liquid-liquid counter-current flows. II. Mass transfer kinetics." Journal of Engineering Physics and Thermophysics 80, no. 4 (July 2007): 728–33. http://dx.doi.org/10.1007/s10891-007-0099-4.

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35

Lisovsky, A. F. "Some features of mass transfer in composite materials." Science of Sintering 50, no. 4 (2018): 395–400. http://dx.doi.org/10.2298/sos1804395l.

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The paper deals with the process of mass transfer in a two-phase system which consists of a mobile phase (a liquid or a gas) and dispersed particles forming a spacial structure, i.e. a skeleton. It is shown that in systems like this the process of the mobile phase transfers is greatly affected by forces generated at both interfaces and particle boundaries. These forces are responsible for new regularities of the mass transfer in dispersed systems, in particular, a spontaneous increase in an intensive variable is a possibility.
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36

Matkivska, Iryna, Yaroslav Gumnytskyi, and Volodymyr Atamanyuk. "Kinetics of Diffusion Mass Transfer during Filtration Drying of Grain Materials." Chemistry & Chemical Technology 8, no. 3 (September 1, 2014): 359–63. http://dx.doi.org/10.23939/chcht08.03.359.

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37

Jansen, T. G. T., P. A. Lovell, J. Meuldijk, and A. M. van Herk. "Mass Transfer in Miniemulsion Polymerisation." Macromolecular Symposia 333, no. 1 (November 2013): 24–34. http://dx.doi.org/10.1002/masy.201300050.

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38

Simal, Susana, J. A. Cárcel, J. Bon, Á. Castell-Palou, and Carmen Rosselló. "Mass Transfer Modelling in an Acoustic-Assisted Osmotic Process." Defect and Diffusion Forum 258-260 (October 2006): 600–609. http://dx.doi.org/10.4028/www.scientific.net/ddf.258-260.600.

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Ultrasounds are mechanical waves that produce different effects when travelling through a medium, some related to mass transfer (i.e. microstirring at the interface, the so called "sponge effect" and cavitations). Thus, ultrasound appears to be a way to reduce both the internal and external resistances in osmotic food drying processes. In this study, the influence of the ultrasounds on water and solute transports during osmotic processes of drying is evaluated. Two different systems have been studied, apple slabs immersed in 30ºBrix sucrose solution, and pork loin slabs in sodium chloride saturated brine. The mathematical modelling of the mass transfers has been carried out by assuming diffusional mechanism and considering the mutual effect between the two mass transfers, the water losses and solute gains. The mass transfer curves in the osmotic process of apple drying in sucrose solution were satisfactorily simulated by using a diffusional model considering independent mass fluxes. Nevertheless, this model did not allow for the accurate simulation of the water losses in the system constituted by pork-loin in saline solution. When the mass fluxes were considered mutually affected, the simulation was accurate for both cases water and solute transfer.
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39

KOYAMA, Kazuya, Takamasa OGINO, Yasuhiro FUKUNAKA, and Zenjiro ASAKI. "Mass Transfer in Powder Injection." Shigen-to-Sozai 110, no. 1 (1994): 23–29. http://dx.doi.org/10.2473/shigentosozai.110.23.

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40

Xue-Zheng, Hu, Liu Jun-Kang, Yu Xue-Jun, and Liu Song-Qin. "Interfacial Instability and Mass Transfer." Acta Physico-Chimica Sinica 14, no. 11 (1998): 1053–56. http://dx.doi.org/10.3866/pku.whxb19981118.

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41

., Sonia. "Topic heat and mass transfer." International Journal of Applied Research 7, no. 12 (December 1, 2021): 109–17. http://dx.doi.org/10.22271/allresearch.2021.v7.i12b.9621.

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42

Kawai, Yosuke. "Proton Transfer Reaction Mass Spectrometry." Journal of the Mass Spectrometry Society of Japan 70, no. 1 (March 1, 2022): 70–71. http://dx.doi.org/10.5702/massspec.s22-12.

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43

Jacobi, Dipl Biotechnol Anna, Dipl Ing Dragomira Ivanova, and Prof Dr Ing Clemens Posten. "Photobioreactors: Hydrodynamics and mass transfer." IFAC Proceedings Volumes 43, no. 6 (2010): 162–67. http://dx.doi.org/10.3182/20100707-3-be-2012.0033.

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44

Kärnä, Aki, Mika Järvinen, and Timo Fabritius. "Supersonic Lance Mass Transfer Modelling." Materials Science Forum 762 (July 2013): 686–90. http://dx.doi.org/10.4028/www.scientific.net/msf.762.686.

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Numerical models of steelmaking processes are essential tools for process development and optimisation. A usable model is detailed enough to provide reliable results and not to slow to run. In order to make a fast and accurate model of a single process, all model parameters must be known well. This can be achieved by first simulating detailed models from which the parameters are obtained.In many converter processes oxygen is delivered into melt by supersonic top lance blowing. When such process is modeled, a model describing mass transfer from the lance into melt surface is needed.This paper describes numerical modeling of mass transfer by supersonic lances. Lance flow CFD models are used to determine mass transfer coefficients for typical lance applications. Models are validated with supersonic nozzle data and wall impinging jet mass transfer data from literature. The results are later used in fast process simulation models.
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45

Nishiki, Tadaaki. "Mass Transfer in Reverse Micelles." membrane 25, no. 1 (2000): 11–16. http://dx.doi.org/10.5360/membrane.25.11.

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46

Fukuda, Makoto. "Mass Transfer in a Dialyzer." MEMBRANE 37, no. 1 (2012): 10–16. http://dx.doi.org/10.5360/membrane.37.10.

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47

Zaki, M. M., Y. A. EL‐Taweel, A. A. Zatout, M. Z. El‐Abd, and G. H. Sadahmed. "Mass Transfer at Oscillating Grids." Journal of The Electrochemical Society 138, no. 2 (February 1, 1991): 430–34. http://dx.doi.org/10.1149/1.2085604.

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48

Pavlovskii, K., and N. Ivanova. "Mass transfer from giant donors." Monthly Notices of the Royal Astronomical Society 449, no. 4 (April 14, 2015): 4415–27. http://dx.doi.org/10.1093/mnras/stv619.

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49

Saito, Noritsuna, Hitoshi Kosuge, and Koichi Asano. "Mass Transfer in Heterogeneous Distillation." JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 31, no. 5 (1998): 758–64. http://dx.doi.org/10.1252/jcej.31.758.

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50

Krishna, R., and J. M. van Baten. "Mass transfer in bubble columns." Catalysis Today 79-80 (April 2003): 67–75. http://dx.doi.org/10.1016/s0920-5861(03)00046-4.

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