Готові списки джерел за темами / Transport/ mass transfer

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Добірка наукової літератури з теми "Transport/ mass transfer"

Автор: Grafiati
Опубліковано: 14 вересня 2024

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Статті в журналах з теми "Transport/ mass transfer"

1

Moore, J. A., and C. R. Ethier. "Oxygen Mass Transfer Calculations in Large Arteries." Journal of Biomechanical Engineering 119, no. 4 (November 1, 1997): 469–75. http://dx.doi.org/10.1115/1.2798295.

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The purpose of this study was to model the transport of oxygen in large arteries, including the physiologically important effects of oxygen transport by hemoglobin, coupling of transport between oxygen in the blood and in wall tissue, and metabolic consumption of oxygen by the wall. Numerical calculations were carried out in an 89 percent area reduction axisymmetric stenosis model for several wall thicknesses. The effects of different boundary conditions, different schemes for linearizing the oxyhemoglobin saturation curve, and different Schmidt numbers were all examined by comparing results against a reference solution obtained from solving the full nonlinear governing equations with physiologic values of Schmidt number. Our results showed that for parameters typical of oxygen mass transfer in the large arteries, oxygen transport was primarily determined by wall-side effects, specifically oxygen consumption by wall tissue and wall-side mass transfer resistance. Hemodynamic factors played a secondary role, producing maximum local variations in intimal oxygen tension on the order of only 5–6 mmHg. For purposes of modeling blood-side oxygen transport only, accurate results were obtained through use of a computationally efficient linearized form of the convection-diffusion equation, so long as blood-side oxygen tensions remained in the physiologic range for large arteries. Neglect of oxygen binding by hemoglobin led to large errors, while arbitrary reduction of the Schmidt number led to more modest errors. We conclude that further studies of oxygen transport in large arteries must couple blood-side oxygen mass transport to transport in the wall, and accurately model local oxygen consumption within the wall.
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2

Speetjens, M. F. M., and A. A. Van Steenhoven. "Heat and Mass Transfer Made Visible." Defect and Diffusion Forum 312-315 (April 2011): 713–18. http://dx.doi.org/10.4028/www.scientific.net/ddf.312-315.713.

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Heat and mass transfer in fluid flows traditionally is examined in terms of temperature and concentration fields and heat/mass-transfer coefficients at fluid-solid interfaces. However, heat/mass transfer may alternatively be considered as the transport of a passive scalar by the total advective-diffusive flux in a way analogous to the transport of fluid by the flow field. This Lagrangian approach facilitates heat/mass-transfer visualisation in a similar manner as flow visualisation and has great potential for transport problems in which insight into (interaction between) the scalar fluxes throughout the entire configuration is essential. This ansatz furthermore admits investigation of heat and mass transfer by well-established geometrical methods from laminar-mixing studies, which offers promising new research capabilities. The Lagrangian approach is introduced and demonstrated by way of representative examples.
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3

Ndiaye, L., Mb Ndiaye, A. Sy, and D. Seck. "Pollution Transfer as Optimal Mass Transport Problem." Journal of Mathematics Research 8, no. 6 (November 25, 2016): 58. http://dx.doi.org/10.5539/jmr.v8n6p58.

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In this paper, we use mass transportation theory to study pollution transfer in porous media. We show the existence of a $L^2-$regular vector field defined by a $W^{1, 1}-$ optimal transport map. A sufficient condition for solvability of our model, is given by a (non homogeneous) transport equation with a source defined by a measure. The mathematical framework used, allows us to show in some specifical cases, existence of solution for a nonlinear PDE deriving from the modelling. And we end by numerical simulations.
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4

Mujumdar, A. S. "Transport Phenomena in Heat and Mass Transfer." Drying Technology 11, no. 7 (January 1993): 1917–18. http://dx.doi.org/10.1080/07373939308916939.

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5

Levdansky, Valerij, Olina Šolcová, Karel Friess, and Pavel Izák. "Mass Transfer Through Graphene-Based Membranes." Applied Sciences 10, no. 2 (January 8, 2020): 455. http://dx.doi.org/10.3390/app10020455.

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The problems related to the transport of gases through nanoporous graphene (NG) and graphene oxide (GO) membranes are considered. The influence of surface processes on the transport of gas molecules through the aforementioned membranes is studied theoretically. The obtained regularities allow finding the dependence of the flux of the gas molecules passing through the membrane on the kinetic parameters which describe the interaction of the gas molecules with the graphene sheets. This allows to take into account the influence of external fields (e.g., resonance radiation), affecting the aforementioned kinetic parameters, on the transport of gas molecules through the membranes. The proposed approach makes it possible to explain some experimental results related to mass transfer in the GO membranes. The possibility of the management of mass transfer through the NG and GO membranes using resonance radiation is discussed.
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6

Geary, Denis F., Elizabeth A. Harvey, and J. Williamson Balfe. "Mass Transfer Area Coefficients in Children." Peritoneal Dialysis International: Journal of the International Society for Peritoneal Dialysis 14, no. 1 (January 1994): 30–33. http://dx.doi.org/10.1177/089686089401400106.

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Objective Measurement of mass transfer area coefficients (MTAC) in children of different sizes to determine if solute transport varies with age and to compare with published adult values. Design Mass transfer area coefficients calculated from prospectively collected data in 28 selected patients. Participants All children starting maintenance peritoneal dialysis at the Hospital for Sick Children. Selected patients were also studied if hospitalized for unrelated reasons. Results Mean MTAC values for creatinine and glucose were 4.0 and 4.5 mL/min, respectively, both considerably lower than adult values. When scaled per 70 kg body weight, these results were greater, and when scaled per 1.73 m2 surface area, they were lower than reported adult values. The MTAC/kg body weight was inversely correlated to age. Conclusions Solute transport in children is directly related to age and does not approach adult values until later childhood. However, more rapid transport per unit body weight is observed in children and may reflect an increased effective peritoneal surface area.
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7

Boskovic-Vragolovic, Nevenka, Radmila Garic-Grulovic, and Zeljko Grbavcic. "Wall-to-liquid mass transfer in fluidized beds and vertical transport of inert particles." Journal of the Serbian Chemical Society 72, no. 11 (2007): 1103–13. http://dx.doi.org/10.2298/jsc0711103b.

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Mass transfer coefficients in single phase flow, liquid fluidized beds and vertical hydraulic transport of spherical inert particles were studied experimentally using 40 mm and 25.4 mm diameter columns. The mass transfer data were obtained by studying the transfer of benzoic acid from a tube segment to water using the dissolution method. In all runs, the mass transfer rates were determined in the presence of spherical glass particles 1.2, 1.94 and 2.98 mm in diameter. The influence of different parameters, such as liquid velocity, particles size and voids on mass transfer in fluidized beds and hydraulic transport are presented. The data for mass transfer in all the investigated systems are shown using the Sherwood number (Sh) and mass transfer factor - Colburn factor (jD) - as a function of Reynolds number (Re) for the particles and for the column. The data for mass transfer in particulate fluidized beds and for vertical hydraulic transport of spherical particles were correlated by treating the flowing fluid-particle mixture as a pseudo fluid by introducing a modified mixture Reynolds number (Rem). A new correlation for the mass transfer factor in fluidized beds and in vertical hydraulic transport is proposed.
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8

Wäsche, S., H. Horn, and D. C. Hempel. "Mass transfer phenomena in biofilm systems." Water Science and Technology 41, no. 4-5 (February 1, 2000): 357–60. http://dx.doi.org/10.2166/wst.2000.0466.

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Mathematical models allow the simulation of microorganism growth and substrate transport in biofilm systems. Nevertheless there is still a lack of knowledge about the mass transfer of substrate in the boundary layer between biofilm and bulkphase. Several biofilms were cultivated under different substrate and hydrodynamic conditions in a biofilm tube reactor. Oxygen concentration profiles were measured with oxygen microelectrodes in the biofilm and in the boundary layer. The thickness of the concentration layer was found to depend on surface structure which depends on the substrate loading and the hydrodynamic conditions during the growth phase of the biofilm. Biofilm density and maximum substrate flux were also influenced by growth conditions. An empirical function for the concentration layer thickness was formulated for biofilms grown under different conditions to describe transport phenomena in the boundary layer.
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9

Shu, Zhixin, Sunil Hadap, Eli Shechtman, Kalyan Sunkavalli, Sylvain Paris, and Dimitris Samaras. "Portrait Lighting Transfer Using a Mass Transport Approach." ACM Transactions on Graphics 36, no. 4 (July 20, 2017): 1. http://dx.doi.org/10.1145/3072959.3095816.

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10

Shu, Zhixin, Sunil Hadap, Eli Shechtman, Kalyan Sunkavalli, Sylvain Paris, and Dimitris Samaras. "Portrait lighting transfer using a mass transport approach." ACM Transactions on Graphics 36, no. 4 (July 20, 2017): 1. http://dx.doi.org/10.1145/3072959.3126847.

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Дисертації з теми "Transport/ mass transfer"

1

Binder, Thomas, Christian Chmelik, Jörg Kärger, and Douglas M. Ruthven. "Mass-transfer of binary mixtures in DDR single crystals." Universitätsbibliothek Leipzig, 2015. http://nbn-resolving.de/urn:nbn:de:bsz:15-qucosa-182920.

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2

Weber, Sofie Aimee. "Contaminant transport and mass transfer to runoff including infiltration." Thesis, The University of Arizona, 1997. http://etd.library.arizona.edu/etd/GetFileServlet?file=file:///data1/pdf/etd/azu_etd_hy0151_sip1_w.pdf&type=application/pdf.

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3

Binder, Thomas, Christian Chmelik, Jörg Kärger, and Douglas M. Ruthven. "Mass-transfer of binary mixtures in DDR single crystals." Diffusion fundamentals 20 (2013) 44, S. 1-2, 2013. https://ul.qucosa.de/id/qucosa%3A13614.

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4

Heinke, Lars, and Jörg Kärger. "Mass transfer in one-dimensional nanoporous crystals with different surface permeabilities." Universitätsbibliothek Leipzig, 2016. http://nbn-resolving.de/urn:nbn:de:bsz:15-qucosa-192770.

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The use of optical techniques, such as interference microscopy and IR micro-imaging, has enabled the direct observation of transient concentration profiles. In a one-dimensional crystal, surface permeabilities on opposing crystal faces are usually equal, so that mass transfer occurs symmetrically and the fluxes through both crystal faces are identical. If the surface permeabilities on opposing crystal faces are different from each other, mass transfer is not symmetrical anymore. We are going to show that the fraction of molecular uptake (or release) through a given host face is inversely proportional to the time constant of uptake/release via this crystal face. This finding permits a straightforward estimate of the influence of asymmetry on overall uptake.
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5

Inzoli, Isabella, Jean Marc Simon, and Signe Kjelstrup. "Surface resistance to heat and mass transfer in a silicalite membrane." Universitätsbibliothek Leipzig, 2016. http://nbn-resolving.de/urn:nbn:de:bsz:15-qucosa-193396.

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6

Remi, Julien Cousin Saint, Alexander Lauerer, Gino Baron, Christian Chmelik, Joeri Denayer, and Jörg Kärger. "The effect of crystal diversity of nanoporous materials on mass transfer studies." Universitätsbibliothek Leipzig, 2016. http://nbn-resolving.de/urn:nbn:de:bsz:15-qucosa-198073.

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7

Heinke, Lars. "Significance of concentration-dependent intracrystalline diffusion and surface permeation for overall mass transfer." Universitätsbibliothek Leipzig, 2016. http://nbn-resolving.de/urn:nbn:de:bsz:15-qucosa-194507.

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The intracrystalline concentration profiles evolving during molecular uptake and release by nanoporous materials as accessible by interference microscopy contain a lot of hidden information. For concentration-independent transport parameter, the influence of surface resistances to overall mass transfer can be calculated by correlating the actual surface concentration with the overall uptake. By using a numerical solution of Fick’s 2nd law and considering a large variety of concentration dependencies of the transport diffusivity and the surface permeability, we show that the factor by which the transport process is retarded by the surface resistance may reasonably well be estimated by the type of correlation between the actual boundary concentration and the total uptake at a given time. In this way, a novel technique of uptake analysis which may analytically be shown to hold for constant diffusivities and surface permeabilities, is shown to be quite generally applicable.
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8

Heinke, Lars, and Jörg Kärger. "Mass transfer in one-dimensional nanoporous crystals with different surface permeabilities." Diffusion fundamentals 9 (2008) 2, S. 1-6, 2008. https://ul.qucosa.de/id/qucosa%3A14139.

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The use of optical techniques, such as interference microscopy and IR micro-imaging, has enabled the direct observation of transient concentration profiles. In a one-dimensional crystal, surface permeabilities on opposing crystal faces are usually equal, so that mass transfer occurs symmetrically and the fluxes through both crystal faces are identical. If the surface permeabilities on opposing crystal faces are different from each other, mass transfer is not symmetrical anymore. We are going to show that the fraction of molecular uptake (or release) through a given host face is inversely proportional to the time constant of uptake/release via this crystal face. This finding permits a straightforward estimate of the influence of asymmetry on overall uptake.
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9

Snyder, Kevin P. "Multiphase flow and mass transport through porous media." Thesis, Virginia Tech, 1993. http://hdl.handle.net/10919/40658.

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10

Simoni, Stefano Federico. "Factors affecting bacterial transport and substrate mass transfer in model aquifers /." [S.l.] : [s.n.], 1999. http://e-collection.ethbib.ethz.ch/show?type=diss&nr=13232.

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Книги з теми "Transport/ mass transfer"

1

Acosta, Jose Luis. Porous media: Heat & mass transfer, transport & mechanics. Hauppauge: Nova Science Publishers, 2009.

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2

Murch, G. E., and Andreas Öchsner. Recent advances in mass transport in materials. Durnten-Zurich: Trans Tech Publications, 2012.

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3

1928-, Greenkorn Robert Albert, ed. Momentum, heat, and mass transfer fundamentals. New York: Marcel Dekker, 1999.

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4

International Conference on Transport in Nonstoichiometric Compounds (3rd 1984 Pennsylvania State University). Transport in nonstoichiometric compounds. New York: Plenum Press, 1985.

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5

Murch, G. E., Irina Belova, and Andreas Öchsner. Recent advances in mass transport in engineering materials. Durnten-Zurich, Switzerland: TTP, Trans Tech Publications Ltd, 2013.

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6

Moosavi, Ali. Transport properties of multi-phase composite materials. Lappeenranta, Finland: Lappeenranta University of Technology, 2003.

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7

Brenner, Howard. Macrotransport processes. Boston: Butterworth-Heinemann, 1993.

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8

International Conference on Ion and Mass Transport in Cement-Based Materials (1999 Toronto, Ont.). Ion and mass transport in cement-based materials. Westerville, Ohio: American Ceramic Society, 2001.

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9

R, Holton James, Rosenlof Karen H, and United States. National Aeronautics and Space Administration., eds. Seasonal variation of mass transport across the tropopause. [Washington, DC: National Aeronautics and Space Administration, 1996.

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10

Tsonopoulos, Constantine. Thermodynamic and transport properties of coal liquids. New York: Wiley, 1986.

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Частини книг з теми "Transport/ mass transfer"

1

Dutta, Sujay Kumar. "Mass Transfer." In Fundamental of Transport Phenomena and Metallurgical Process Modeling, 183–219. Singapore: Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-19-2156-8_4.

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2

Poirier, D. R., and G. H. Geiger. "Interphase Mass Transfer." In Transport Phenomena in Materials Processing, 547–69. Cham: Springer International Publishing, 2016. http://dx.doi.org/10.1007/978-3-319-48090-9_15.

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3

Mehling, Harald, and Luisa F. Cabeza. "Applications in transport and storage containers." In Heat and Mass Transfer, 191–203. Berlin, Heidelberg: Springer Berlin Heidelberg, 2008. http://dx.doi.org/10.1007/978-3-540-68557-9_7.

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4

Ghiaasiaan, S. Mostafa. "Thermophysical and transport fundamentals." In Convective Heat and Mass Transfer, 1–42. Second edition. | Boca Raton : Taylor & Francis, CRC Press, 2018. | Series: Heat transfer: CRC Press, 2018. http://dx.doi.org/10.1201/9781351112758-1.

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Poirier, E. J., and D. R. Poirier. "Interphase Mass Transfer." In Solutions Manual To accompany Transport Phenomena in Materials Processing, 240–52. Cham: Springer International Publishing, 2016. http://dx.doi.org/10.1007/978-3-319-65130-9_12.

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6

Poirier, E. J., and D. R. Poirier. "Interphase Mass Transfer." In Solutions Manual To accompany Transport Phenomena in Materials Processing, 294–304. Cham: Springer International Publishing, 2016. http://dx.doi.org/10.1007/978-3-319-65130-9_15.

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7

Iguchi, Manabu, and Olusegun J. Ilegbusi. "Diffusion and Mass Transfer." In Basic Transport Phenomena in Materials Engineering, 135–47. Tokyo: Springer Japan, 2013. http://dx.doi.org/10.1007/978-4-431-54020-5_8.

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8

Leeuwen, Herman P. van, and Josep Galceran. "Biointerfaces and Mass Transfer." In Physicochemical Kinetics and Transport at Biointerfaces, 113–46. Chichester, UK: John Wiley & Sons, Ltd, 2004. http://dx.doi.org/10.1002/0470094044.ch3.

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Nagnibeda, Ekaterina, and Elena Kustova. "Algorithms for the Calculation of Transport Coefficients." In Heat and Mass Transfer, 111–69. Berlin, Heidelberg: Springer Berlin Heidelberg, 2009. http://dx.doi.org/10.1007/978-3-642-01390-4_6.

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Nagnibeda, Ekaterina, and Elena Kustova. "Multi-Temperature Models in Transport and Relaxation Theory." In Heat and Mass Transfer, 55–95. Berlin, Heidelberg: Springer Berlin Heidelberg, 2009. http://dx.doi.org/10.1007/978-3-642-01390-4_4.

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Тези доповідей конференцій з теми "Transport/ mass transfer"

1

Page, R. H. "Jet Impingement: Transport Phenomena." In Heat and Mass Transfer Australasia. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/978-1-56700-099-3.630.

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2

Shiomi, Junichiro, Carl Fredrik Carlborg, and Shigeo Maruyama. "Heat and Mass Transport in Carbon Nantubes." In 2010 14th International Heat Transfer Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/ihtc14-23115.

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We have investigated heat and mass transport in single-walled carbon nanotubes (SWNTs) using molecular dynamics methods. Particular attention was paid on the non-equilibrium dynamics at the interface between SWNT and other materials, which strongly manifests in nanoscale. In the first part, we have investigated the heat transport through the interface between SWNTs and surrounding argon matrices in liquid and solid phases. By analyzing the energy relaxation from SWNT to the matrices using non-stationary molecular dynamics simulations, elastic and inelastic thermal energy transports across the interface were separately quantified. The result reveals that the elastic interaction transports energy much faster than the inelastic one, but carries much smaller energy due to slow intra-SWNT phonon relaxation. In the second part, we have investigated a possibility to utilize nonequilibrium thermal interface to transport water through an SWNT. By applying the longitudinal temperature gradient to the SWNT, it is demonstrated that the water cluster is efficiently driven at average acceleration proportional to the temperature gradient. However, the transport simulations with a junction of two different SWNTs suggest that an angstrom diameter difference may result in a significant drag for small diameter SWNTs.
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Mayinger, Franz. "Transport Phenomena in Highly Turbulent Flames." In Heat and Mass Transfer Australasia. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/978-1-56700-099-3.240.

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4

Hisajima, Daisuke, Sirajul K. Choudhury, Akira Nishiguchi, Tomihisa Oouchi, and Seiichiro Sakaguchi. "HEAT AND MASS TRANSFER IN FALLING FILMS." In International Symposium on Imaging in Transport Processes. Connecticut: Begellhouse, 1992. http://dx.doi.org/10.1615/ichmt.1992.intsympimgtranspproc.170.

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5

Renz, Rudolf, and Dieter Mewes. "Flow, Heat and Mass Transfer VisualizationOBSERVATION OF HEAT AND MASS TRANSFER IN LIQUIDS BY MEANS OF OPTICAL TOMOGRAPHY." In International Symposium on Imaging in Transport Processes. Connecticut: Begellhouse, 1992. http://dx.doi.org/10.1615/ichmt.1992.intsympimgtranspproc.70.

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6

Ramos, J. I. "MASS TRANSFER IN ANNULAR LIQUID JETS." In International Symposium on Liquid-Liquid Two Phase Flow and Transport Phenomena. Connecticut: Begellhouse, 1997. http://dx.doi.org/10.1615/ichmt.1997.intsymliqtwophaseflowtranspphen.390.

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7

Mungekar, Hemant, Bruno Geoffrion, Bikram Kapoor, Naren Dubey, Mak Salimian, Michael Cox, and Paddy Krishnaraj. "Heat and Mass Transport in HDP-CVD Chamber." In ASME 2003 Heat Transfer Summer Conference. ASMEDC, 2003. http://dx.doi.org/10.1115/ht2003-47030.

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HDP-CVD reactors are used for Shallow Trench Isolation (STI), Inter Metal Dielectric (IMD) and Inter Layer Dielectric (ILD) applications for logic and memory device fabrication. As device dimension shrinks, the trend has been to use lower pressure and higher plasma density for gap-fill with higher aspect ratio (AR). Higher AR gapfill in addition to higher throughput is achieved by running multiple wafers between a chamber clean, present a unique set of challenges for heat and mass-transfer in an HDP-CVD reactor. This paper describes some of the new state-of-the-art hardware innovations specifically developed to meet these challenges. In particular, heat transfer to plasma facing materials, fluid mechanics, and transport of sub-micron sized particles in the plasma environment of an HDP-CVD reactor are explored.
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Maděra, J., P. Tesárek, and R. Černý. "Coupled heat and moisture transport in a building envelope on cast gypsum basis." In HEAT AND MASS TRANSFER 2006. Southampton, UK: WIT Press, 2006. http://dx.doi.org/10.2495/ht060151.

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Tsuruta, Takaharu, and Gyoko Nagayama. "A MOLECULAR DYNAMICS APPROACH TO INTERPHASE MASS TRANSFER BETWEEN LIQUID AND VAPOR." In Heat Transfer and Transport Phenomena in Microscale. Connecticut: Begellhouse, 2023. http://dx.doi.org/10.1615/1-56700-150-5.630.

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10

Shiomi, Junichiro, Yuan Lin, Carl Fredrik Carlborg, Gustav Amberg, and Shigeo Maruyama. "Low Dimensional Heat and Mass Transport in Carbon Nanotubes." In ASME 2009 Second International Conference on Micro/Nanoscale Heat and Mass Transfer. ASMEDC, 2009. http://dx.doi.org/10.1115/mnhmt2009-18541.

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Анотація:
This report covers various issues related to heat and mass transport in carbon nanotubes. Heat and mass transport under quasi-one-dimensional confinement has been investigated using molecular dynamics simulations. It is shown that the quasi-ballistic heat conduction manifests in the length and diameter dependences of carbon nanotube thermal conductance. Such quasi-ballistic nature of carbon nanotube heat conduction also influences the thermal boundary conductance between carbon nanotubes and the surrounding materials. The quasi-one-dimensional structure also influences the mass transport of water through carbon nanotubes. The confinement gives rise to strongly directional dynamic properties of water. Here, it is demonstrated that the confined water can be efficiently transported by using the temperature gradient. Furthermore, the simulations reveal the diameter-dependent anisotropic dielectric properties, which could be used to identify intrusion of water into carbon nanotubes.
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Звіти організацій з теми "Transport/ mass transfer"

1

Chambre, P. L., T. H. Pigford, W. W. L. Lee, J. Ahn, S. Kajiwara, C. L. Kim, H. Kimura, H. Lung, W. J. Williams, and S. J. Zavoshy. Mass transfer and transport in a geologic environment. Office of Scientific and Technical Information (OSTI), April 1985. http://dx.doi.org/10.2172/5161610.

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2

Ahn, Joonhong. Mass transfer and transport of radionuclides in fractured porous rock. Office of Scientific and Technical Information (OSTI), April 1988. http://dx.doi.org/10.2172/7132953.

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3

HAGGERTY, ROY, SEAN W. FLEMING, and SEAN A. MCKENNA. STAMMT-R Solute Transport and Multirate Mass Transfer in Radial Coordinates. Office of Scientific and Technical Information (OSTI), July 2000. http://dx.doi.org/10.2172/759366.

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4

Viswanathan, H. S. Modification of the finite element heat and mass transfer code (FEHM) to model multicomponent reactive transport. Office of Scientific and Technical Information (OSTI), August 1996. http://dx.doi.org/10.2172/279704.

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5

Viswanathan, H. S. Modification of the finite element heat and mass transfer code (FEHMN) to model multicomponent reactive transport. Office of Scientific and Technical Information (OSTI), December 1995. http://dx.doi.org/10.2172/541823.

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6

Koretsky, Carla M., and Philippe Van Cappellen. Quantitative Mass Transfer in Coastal Sediments During Early Diagenesis: Effects of Biological Transport, Mineralogy and Fabric. Fort Belvoir, VA: Defense Technical Information Center, September 2001. http://dx.doi.org/10.21236/ada626821.

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7

Miller, R. M. ,. Brusseau, M. L. Influence of biosurfactants on mass transfer, biodegradation, and transport of mixed wastes in multiphase systems: Final report. Office of Scientific and Technical Information (OSTI), January 1997. http://dx.doi.org/10.2172/488754.

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8

Furukawa, Yoko. Quantitative Chemical Mass Transfer in Coastal Sediments During Early Diagenesis: Effects of Biological Transport, Mineralogy, and Fabric. Fort Belvoir, VA: Defense Technical Information Center, September 1999. http://dx.doi.org/10.21236/ada636798.

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9

Lavoie, Dawn, Yoko Furukawa, Phillippe VanCappellan, and Barbara Ransom. Quantitative Chemical Mass Transfer in Coastal Sediments During Earky Diagenesis: Effects of Biological Transport, Mineralogy, and Fabric. Fort Belvoir, VA: Defense Technical Information Center, September 1997. http://dx.doi.org/10.21236/ada621036.

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10

Ransom, Barbara, and Miriam Kastner. Quantitative Chemical Mass Transfer in Coastal Sediments During Early Diagenesis: Effects of Biological Transport, Mineralogy, and Fabric. Fort Belvoir, VA: Defense Technical Information Center, September 1997. http://dx.doi.org/10.21236/ada626810.

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