Log in

Relevant bibliographies by topics / Reaction-transport model / Journal articles

To see the other types of publications on this topic, follow the link: Reaction-transport model.

Journal articles on the topic 'Reaction-transport model'

Author: Grafiati

Published: 4 June 2021

Last updated: 1 February 2022

Create a spot-on reference in APA, MLA, Chicago, Harvard, and other styles

Select a source type:

Consult the top 50 journal articles for your research on the topic 'Reaction-transport model.'

Next to every source in the list of references, there is an 'Add to bibliography' button. Press on it, and we will generate automatically the bibliographic reference to the chosen work in the citation style you need: APA, MLA, Harvard, Chicago, Vancouver, etc.

You can also download the full text of the academic publication as pdf and read online its abstract whenever available in the metadata.

Browse journal articles on a wide variety of disciplines and organise your bibliography correctly.

1

Karapiperis, T., and B. Blankleider. "Cellular automation model of reaction-transport porcesses." Physica D: Nonlinear Phenomena 78, no. 1-2 (November 1994): 30–64. http://dx.doi.org/10.1016/0167-2789(94)00093-x.

Full text

APA, Harvard, Vancouver, ISO, and other styles

2

Lao, Liangfeng, Matthew Ellis, and Panagiotis D. Christofides. "Economic Model Predictive Control of Transport-Reaction Processes." Industrial & Engineering Chemistry Research 53, no. 18 (June 24, 2013): 7382–96. http://dx.doi.org/10.1021/ie401016a.

Full text

APA, Harvard, Vancouver, ISO, and other styles

3

Mihopoulos, Theodoros G., Vijay Gupta, and Klavs F. Jensen. "A reaction-transport model for AlGaN MOVPE growth." Journal of Crystal Growth 195, no. 1-4 (December 1998): 733–39. http://dx.doi.org/10.1016/s0022-0248(98)00649-6.

Full text

APA, Harvard, Vancouver, ISO, and other styles

4

Xu, Qingqing, and Stevan Dubljevic. "Linear model predictive control for transport-reaction processes." AIChE Journal 63, no. 7 (January 25, 2017): 2644–59. http://dx.doi.org/10.1002/aic.15592.

Full text

APA, Harvard, Vancouver, ISO, and other styles

5

Bendersky, Eugene, and Panagiotis D. Christofides. "Optimization of transport-reaction processes using nonlinear model reduction." Chemical Engineering Science 55, no. 19 (October 2000): 4349–66. http://dx.doi.org/10.1016/s0009-2509(00)00037-3.

Full text

APA, Harvard, Vancouver, ISO, and other styles

6

Bressloff, P. C. "Multi-spike solutions of a hybrid reaction–transport model." Proceedings of the Royal Society A: Mathematical, Physical and Engineering Sciences 477, no. 2247 (March 2021): 20200829. http://dx.doi.org/10.1098/rspa.2020.0829.

Full text

Abstract:

Simulations of classical pattern-forming reaction–diffusion systems indicate that they often operate in the strongly nonlinear regime, with the final steady state consisting of a spatially repeating pattern of localized spikes. In activator–inhibitor systems such as the two-component Gierer–Meinhardt (GM) model, one can consider the singular limit D a ≪ D h , where D a and D h are the diffusivities of the activator and inhibitor, respectively. Asymptotic analysis can then be used to analyse the existence and linear stability of multi-spike solutions. In this paper, we analyse multi-spike solutions in a hybrid reaction–transport model, consisting of a slowly diffusing activator and an actively transported inhibitor that switches at a rate α between right-moving and left-moving velocity states. Such a model was recently introduced to account for the formation and homeostatic regulation of synaptic puncta during larval development in Caenorhabditis elegans . We exploit the fact that the hybrid model can be mapped onto the classical GM model in the fast switching limit α → ∞, which establishes the existence of multi-spike solutions. Linearization about the multi-spike solution yields a non-local eigenvalue problem that is used to investigate stability of the multi-spike solution by combining analytical results for α → ∞ with a graphical construction for finite α .

APA, Harvard, Vancouver, ISO, and other styles

7

Rugonyi, Sandra, Erik Tucker, Ulla Marzec, Andras Gruber, and Stephen Hanson. "Transport-Reaction Model of Mural Thrombogenesis: Comparisons of Mathematical Model Predictions and Results from Baboon Models." Annals of Biomedical Engineering 38, no. 8 (March 30, 2010): 2660–75. http://dx.doi.org/10.1007/s10439-010-0016-4.

Full text

APA, Harvard, Vancouver, ISO, and other styles

8

Janacova, Dagmar, Karel Kolomaznik, Pavel Mokrejs, Vladimir Vasek, Jiri Krenek, and Ondrej Liska. "The balance model for heat transport from hydrolytic reaction mixture." MATEC Web of Conferences 125 (2017): 02060. http://dx.doi.org/10.1051/matecconf/201712502060.

Full text

APA, Harvard, Vancouver, ISO, and other styles

9

MOMII, Kazuro, Tomohisa YANO, Kenji JINNO, Takushi YOKOYAMA, Ryuichi ITOI, and Yoshinari HIROSHIRO. "Solute Transport Model in Groundwater Including Multicomponent Chemical Reaction Processes." PROCEEDINGS OF HYDRAULIC ENGINEERING 35 (1991): 641–46. http://dx.doi.org/10.2208/prohe.35.641.

Full text

APA, Harvard, Vancouver, ISO, and other styles

10

Houssa, M., M. Aoulaiche, S. De Gendt, G. Groeseneken, M. M. Heyns, and A. Stesmans. "Reaction-dispersive proton transport model for negative bias temperature instabilities." Applied Physics Letters 86, no. 9 (February 28, 2005): 093506. http://dx.doi.org/10.1063/1.1871357.

Full text

APA, Harvard, Vancouver, ISO, and other styles

11

Lin, Yenhan, Joungmo Cho, Jeffrey M. Davis, and George W. Huber. "Reaction-transport model for the pyrolysis of shrinking cellulose particles." Chemical Engineering Science 74 (May 2012): 160–71. http://dx.doi.org/10.1016/j.ces.2012.02.016.

Full text

APA, Harvard, Vancouver, ISO, and other styles

12

Zubov, Alexandr, Lucie Pechackova, Libor Seda, Marek Bobak, and Juraj Kosek. "Transport and reaction in reconstructed porous polypropylene particles: Model validation." Chemical Engineering Science 65, no. 7 (April 2010): 2361–72. http://dx.doi.org/10.1016/j.ces.2009.09.082.

Full text

APA, Harvard, Vancouver, ISO, and other styles

13

Hwang, Seungtaik, Jörg Kärger, and Erich Miersemann. "Diffusion and reaction in pore hierarchies by the two-region model." Adsorption 27, no. 5 (March 19, 2021): 761–76. http://dx.doi.org/10.1007/s10450-021-00307-x.

Full text

Abstract:

AbstractThe two-region (“Kärger”) model of diffusion in complex pore spaces is exploited for quantitating mass transfer in hierarchically organized nanoporous materials, consisting of a continuous microporous bulk phase permeated by a network of transport pores. With the implications that the diffusivity in the transport pores significantly exceeds the diffusivity in the micropores and that the relative population of the transport pores is far below that of the micropores, overall transport depends on only three independent parameters. Depending on their interrelation, enhancement of the overall mass transfer is found to be ensured by two fundamentally different mechanisms. They are referred to as the limiting cases of fast and slow exchange, with the respective time constants of molecular uptake being controlled by different parameters. Complemented with reaction terms, the two-region model may equally successfully be applied to the quantitation of the combined effect of diffusion and reaction in terms of the effectiveness factor. Generalization of the classical Thiele concept is shown to provide an excellent estimate of the effectiveness factor of a chemical reaction in hierarchically porous materials, solely based on the intrinsic reaction rate and the time constant of molecular uptake relevant to the given conditions.

APA, Harvard, Vancouver, ISO, and other styles

14

Tawfik, Ashraf M., and Mohamed Mokhtar Hefny. "Subdiffusive Reaction Model of Molecular Species in Liquid Layers: Fractional Reaction-Telegraph Approach." Fractal and Fractional 5, no. 2 (June 3, 2021): 51. http://dx.doi.org/10.3390/fractalfract5020051.

Full text

Abstract:

In recent years, different experimental works with molecular simulation techniques have been developed to study the transport of plasma-generated reactive species in liquid layers. Here, we improve the classical transport model that describes the molecular species movement in liquid layers via considering the fractional reaction–telegraph equation. We have considered the fractional equation to describe a non-Brownian motion of molecular species in a liquid layer, which have different diffusivities. The analytical solution of the fractional reaction–telegraph equation, which is defined in terms of the Caputo fractional derivative, is obtained by using the Laplace–Fourier technique. The profiles of species density with the mean square displacement are discussed in each case for different values of the time-fractional order and relaxation time.

APA, Harvard, Vancouver, ISO, and other styles

15

Steinboeck, Andreas, Martin Guay, and Andreas Kugi. "Real-Time Nonlinear Model Predictive Control of a Transport–Reaction System." Industrial & Engineering Chemistry Research 55, no. 28 (July 12, 2016): 7730–41. http://dx.doi.org/10.1021/acs.iecr.6b00592.

Full text

APA, Harvard, Vancouver, ISO, and other styles

16

Li, Zhen, Alireza Yazdani, Alexandre Tartakovsky, and George Em Karniadakis. "Transport dissipative particle dynamics model for mesoscopic advection-diffusion-reaction problems." Journal of Chemical Physics 143, no. 1 (July 7, 2015): 014101. http://dx.doi.org/10.1063/1.4923254.

Full text

APA, Harvard, Vancouver, ISO, and other styles

17

Yang, Yaru, Stevan Dubljevic, and Shaoyuan Li. "Economic model predictive control for transport-reaction systems with target profiles." Control Engineering Practice 107 (February 2021): 104684. http://dx.doi.org/10.1016/j.conengprac.2020.104684.

Full text

APA, Harvard, Vancouver, ISO, and other styles

18

CALE, TIMOTHY S., and SHERIF A. MOHAMED. "FUNDAMENTAL MODEL OF TRANSPORT AND REACTION IN A CYLINDRICAL CATALYST PORE." Chemical Engineering Communications 109, no. 1 (October 1991): 89–108. http://dx.doi.org/10.1080/00986449108910975.

Full text

APA, Harvard, Vancouver, ISO, and other styles

19

Bekbauov, B. E. "Acidizing Process in Acid Fracturing." Eurasian Chemico-Technological Journal 11, no. 2 (April 6, 2016): 159. http://dx.doi.org/10.18321/ectj310.

Full text

Abstract:

The theory and numerical implementation of acid-fracturing model that solves the 2D fracture geometry leakoff, acid transport and acid-rock reaction simultaneously will be presented. The mathematical model proovides a penetration distance for acid fracturing. Due to limitation of analytical solution, a finite-difference method was developed for modelling the fracture acidizing process. Example was solved for HCl reaction in limestone and dolomite fractures, and the results are presented in graphical form. The acid-transport model integrates a number of features which were not accounted for an earlier design models: comprehensive study of hydrodynamic process; acidizing controlled by mass transfer, rate of reaction, and leakoff. Coupling with reservoir forecasting models gives the ability to optimize the job.

APA, Harvard, Vancouver, ISO, and other styles

20

Sund, Nicole, Giovanni Porta, Diogo Bolster, and Rishi Parashar. "A Lagrangian Transport Eulerian Reaction Spatial (LATERS) Markov Model for Prediction of Effective Bimolecular Reactive Transport." Water Resources Research 53, no. 11 (November 2017): 9040–58. http://dx.doi.org/10.1002/2017wr020821.

Full text

APA, Harvard, Vancouver, ISO, and other styles

21

KAWAKAMI, Keiji, Keita OCHI, Yusuke WATANABE, and Yoshinari HIROSHIRO. "TWO-DIMENSIONAL TRANSPORT MODEL OF ARSENIC CONSIDERING THE REDOX REACTION IN GROUNDWATER." Journal of Japan Society of Civil Engineers, Ser. B1 (Hydraulic Engineering) 69, no. 4 (2013): I_565—I_570. http://dx.doi.org/10.2208/jscejhe.69.i_565.

Full text

APA, Harvard, Vancouver, ISO, and other styles

22

Vijayendran, Ravi A., Frances S. Ligler, and Deborah E. Leckband. "A Computational Reaction−Diffusion Model for the Analysis of Transport-Limited Kinetics." Analytical Chemistry 71, no. 23 (December 1999): 5405–12. http://dx.doi.org/10.1021/ac990672b.

Full text

APA, Harvard, Vancouver, ISO, and other styles

23

Bielecki, Andrzej, and Piotr Kalita. "Dynamical properties of the reaction–diffusion type model of fast synaptic transport." Journal of Mathematical Analysis and Applications 393, no. 2 (September 2012): 329–40. http://dx.doi.org/10.1016/j.jmaa.2012.04.012.

Full text

APA, Harvard, Vancouver, ISO, and other styles

24

Hossain, Md Akram. "Modeling advective–dispersive transport with reaction: An accurate explicit finite difference model." Applied Mathematics and Computation 102, no. 2-3 (July 1999): 101–8. http://dx.doi.org/10.1016/s0096-3003(98)10036-x.

Full text

APA, Harvard, Vancouver, ISO, and other styles

25

Sutinen, Jari, Reijo Karvinen, and Wm James Frederick. "A Chemical Reaction Engineering and Transport Model of Kraft Char Bed Burning." Industrial & Engineering Chemistry Research 41, no. 6 (March 2002): 1477–83. http://dx.doi.org/10.1021/ie000393a.

Full text

APA, Harvard, Vancouver, ISO, and other styles

26

Chernyavsky, Boris M., and Ulrich G. Wortmann. "REMAP: A reaction transport model for isotope ratio calculations in porous media." Geochemistry, Geophysics, Geosystems 8, no. 2 (February 2007): n/a. http://dx.doi.org/10.1029/2006gc001442.

Full text

APA, Harvard, Vancouver, ISO, and other styles

27

Bullard, Jeffrey W., Edith Enjolras, William L. George, Steven G. Satterfield, and Judith E. Terrill. "A parallel reaction-transport model applied to cement hydration and microstructure development." Modelling and Simulation in Materials Science and Engineering 18, no. 2 (January 18, 2010): 025007. http://dx.doi.org/10.1088/0965-0393/18/2/025007.

Full text

APA, Harvard, Vancouver, ISO, and other styles

28

Li, Jian, Hanlin Gan, Yifeng Xu, Chaoyang Wang, FengLong Gu, and Gang Wang. "Chemical reaction-transport model of diethylzinc hydrolysis in a vertical MOCVD reactor." Applied Thermal Engineering 136 (May 2018): 108–17. http://dx.doi.org/10.1016/j.applthermaleng.2018.02.069.

Full text

APA, Harvard, Vancouver, ISO, and other styles

29

R�hricht, B., J. Parisi, J. Peinke, and O. E. R�ssler. "A simple morphogenetic reaction-diffusion model describing nonlinear transport phenomena in semiconductors." Zeitschrift f�r Physik B Condensed Matter 65, no. 2 (June 1986): 259–66. http://dx.doi.org/10.1007/bf01303850.

Full text

APA, Harvard, Vancouver, ISO, and other styles

30

Makungu, James, Heikki Haario, and William Charles Mahera. "A generalized 1-dimensional particle transport method for convection diffusion reaction model." Afrika Matematika 23, no. 1 (March 8, 2011): 21–39. http://dx.doi.org/10.1007/s13370-011-0007-0.

Full text

APA, Harvard, Vancouver, ISO, and other styles

31

DATTA, R. "Supported liquid-phase catalysis I. A theoretical model for transport and reaction." Journal of Catalysis 95, no. 1 (September 1985): 181–92. http://dx.doi.org/10.1016/0021-9517(85)90018-1.

Full text

APA, Harvard, Vancouver, ISO, and other styles

32

Tebes-Stevens, Caroline L., Felipe Espinoza, and Albert J. Valocchi. "Evaluating the sensitivity of a subsurface multicomponent reactive transport model with respect to transport and reaction parameters." Journal of Contaminant Hydrology 52, no. 1-4 (November 2001): 3–27. http://dx.doi.org/10.1016/s0169-7722(01)00151-6.

Full text

APA, Harvard, Vancouver, ISO, and other styles

33

Jasielec, Jerzy, Jakub Stec, Krzysztof Szyszkiewicz-Warzecha, Artur Łagosz, Jan Deja, Andrzej Lewenstam, and Robert Filipek. "Effective and Apparent Diffusion Coefficients of Chloride Ions and Chloride Binding Kinetics Parameters in Mortars: Non-Stationary Diffusion–Reaction Model and the Inverse Problem." Materials 13, no. 23 (December 3, 2020): 5522. http://dx.doi.org/10.3390/ma13235522.

Full text

Abstract:

A non-equilibrium diffusion–reaction model is proposed to describe chloride transport and binding in cementitious materials. A numerical solution for this non-linear transport with reaction problem is obtained using the finite element method. The effective chloride diffusion coefficients and parameters of the chloride binding are determined using the inverse method based on a diffusion–reaction model and experimentally measured chloride concentrations. The investigations are performed for two significantly different cements: ordinary Portland and blast furnace cements. The results are compared with the classical diffusion model and appropriate apparent diffusion coefficients. The role of chloride binding, with respect to the different binding isotherms applied, in the overall transport of chlorides is discussed, along with the applicability of the two models. The proposed work allows the determination of important parameters that influence the longevity of concrete structures. The developed methodology can be extended to include more ions, electrostatic interactions, and activity coefficients for even more accurate estimation of the longevity.

APA, Harvard, Vancouver, ISO, and other styles

34

Nagy, Endre, and Imre Hegedüs. "Diffusive Plus Convective Mass Transport, Accompanied by Biochemical Reaction, Across Capillary Membrane." Catalysts 10, no. 10 (September 25, 2020): 1115. http://dx.doi.org/10.3390/catal10101115.

Full text

Abstract:

This study theoretically analyzes the mass transport through capillary, asymmetric, biocatalytic membrane reactor, where the diffusive plus convective mass transport is accompanied by biochemical reaction with Michaelis-Menten kinetics. An approach mathematical model was developed that provides the mass transfer properties in closed, explicit mathematical forms. The inlet and outlet mass transfer rates can then put into the differential mass transport expressions of the lumen and the shell fluid phases as boundary values. The approach solution was obtained by dividing the membrane layer into very thin sub-layers with constant transport and reaction kinetic parameters and the obtained second-order differential equation with constant parameters, given for every sublayer, could be solved analytically. Two operating modes are analyzed in this paper, namely, with and without a sweeping phase on the permeating side. These models deviate by the boundary conditions, only, defined them for the outlet membrane surface. The main purpose of this study is to show how the cylindrical space affects the transport process, concentration distribution, mass transfer rates and conversion in presence of a biochemical reaction. It is shown that the capillary transport can significantly be affected by the lumen radius, by the biocatalytic reactor thickness and the convective flow. Decreasing values of the lumen radius reduce the effect of the biochemical/chemical reaction; the increasing reactor thickness also decreases the physical mass transfer rate and, with it, increases the effect of reaction rate. The model can also be applied to reactions with more general kinetic equations with variable parameters.

APA, Harvard, Vancouver, ISO, and other styles

35

Schleiff, Martin, Günther Lefeld, Hermann Matschiner, and Otomar Špalek. "Modelling of mass transport and chemical reaction in a diaphragm." Collection of Czechoslovak Chemical Communications 52, no. 7 (1987): 1692–700. http://dx.doi.org/10.1135/cccc19871692.

Full text

Abstract:

A mathematical model was proposed for the transport of ions in a diaphragm separating an acidic and an alkaline electrolyte. Besides an approximate analytical solution, a more exact numerical one was presented. The model permits the calculation of the position of the neutralization zone in the diaphragm, rates of transport of ions, and potential in the diaphragm. The dependence of the position of the neutralization zone on the composition of both electrolytes and on the current density was calculated for two technically important cases.

APA, Harvard, Vancouver, ISO, and other styles

36

Benzinger, M. S., R. Schießl, and U. Maas. "A Unified Reduced Model for Auto-Ignition and Combustion in Premixed Systems." Eurasian Chemico-Technological Journal 16, no. 2-3 (April 8, 2014): 107. http://dx.doi.org/10.18321/ectj175.

Full text

Abstract:

In this paper, two complementary chemistry model reduction methods for combustion simulations are further developed and combined. A progress variable model (PVM), which follows the idea of trajectory generated manifolds (TGLDM), is tailored for describing auto-ignition in situations where the influence of<br />molecular transport on chemical reaction is weak, like auto-ignition in media with weak scalar gradients. The other model using the reaction diffusion manifold approach (REDIM) is designed for situations where the interaction of chemistry with molecular transport is essential. The formulation of both models is discussed and implementational issues of each single model are given. Also, each model is tested in its respective range of applicability (quasi-homogeneous combustion under steady/unsteady physical boundary conditions for the PVM, combustion in fields with essential scalar gradients for REDIM). The coupling of the two models into a unified model, which covers combustion in both regimes and during the transitions between regimes, is discussed, based on the global quasi-linearization concept (GQL).

APA, Harvard, Vancouver, ISO, and other styles

37

ZHDANOV, VLADIMIR P., and BENGT KASEMO. "KINETICS OF ELECTROCHEMICAL REACTIONS ON MODEL SUPPORTED CATALYSTS: READSORPTION AND MASS TRANSPORT." Surface Review and Letters 15, no. 06 (December 2008): 745–51. http://dx.doi.org/10.1142/s0218625x08011962.

Full text

Abstract:

To bridge the structure gap, electrochemical reactions can be studied in flow cells with nm-sized catalyst particles deposited or fabricated on the cell walls. The understanding of the role of mass transport in such cells is now limited. To clarify the likely effects in this field, we analyze the simplest reaction scheme including intermediate desorption, readsorption, and subsequent reaction and show how the net rate of the formation of intermediate can be influenced by its diffusion in the liquid phase. With certain approximations, we derive analytical results describing reaction and diffusion near catalyst particles and in more remote regions in the simplest 1D case and more complex 2D and 3D situations.

APA, Harvard, Vancouver, ISO, and other styles

38

Charpin, Laurent, and Alain Ehrlacher. "Simplified Model for the Transport of Alkali-Silica Reaction Gel in Concrete Porosity." Journal of Advanced Concrete Technology 12, no. 1 (January 15, 2014): 1–6. http://dx.doi.org/10.3151/jact.12.1.

Full text

APA, Harvard, Vancouver, ISO, and other styles

39

Carroll, Sam R., Heather Z. Brooks, and Paul C. Bressloff. "Bifurcation analysis of pattern formation in a two-dimensional hybrid reaction–transport model." Physica D: Nonlinear Phenomena 402 (January 2020): 132274. http://dx.doi.org/10.1016/j.physd.2019.132274.

Full text

APA, Harvard, Vancouver, ISO, and other styles

40

González-Gutiérrez, Linda V., Hugo Jiménez-Islas, and Eleazar M. Escamilla-Silva. "Dynamic transport and reaction model for azo dye removal in a UAFB reactor." Process Biochemistry 45, no. 1 (January 2010): 30–38. http://dx.doi.org/10.1016/j.procbio.2009.07.018.

Full text

APA, Harvard, Vancouver, ISO, and other styles

41

Peters, Toni, Rebecca Potter, Xiarong Li, Zhi He, Glenn Hoskins, and Michael F. Flessner. "Mouse model of foreign body reaction that alters the submesothelium and transperitoneal transport." American Journal of Physiology-Renal Physiology 300, no. 1 (January 2011): F283—F289. http://dx.doi.org/10.1152/ajprenal.00328.2010.

Full text

Abstract:

To address the hypothesis that sterile intraperitoneal (ip) catheters alone promote a progressive foreign body reaction (FBR), silicone catheters were surgically implanted in C57BL mice. Controls (CON) underwent sham operations. After 1–5 wk (E1–E5 for catheter-bearing mice), catheters were recovered, and the adherent cell layer (ACL) was separated and cultured to demonstrate sterility. Transperitoneal transport experiments were performed to determine the mass transfer coefficients of mannitol (MTCM) and albumin (MTCA) and the osmotic filtration flux ( Josm). After euthanasia, tissue samples were analyzed for submesothelial thickness, angiogenesis, and cytokine immunohistochemistry (IHC). Progressive increases with time were observed in submesothelial thickness (μm: CON, 18.8 ± 12.3; E1, 46.1 ± 20.0; E2, 72.0 ± 17.9; E4, 97.3 ± 20.0; E5, 131.7 ± 10.3; P < 0.003), angiogenesis (no. of vessels/mm of peritoneum: CON, 10.7 ± 9.4; E1, 15.4 ± 15.6; E2, 27.0 ± 14.0; E4, 39.8 ± 15.7; E5, 90.1 ± 8.1; P < 0.0003), MTCA(6.5 ± 1.5 × 10−5cm/min, mean CON; 18.0 ± 1.1 × 10−5cm/min, mean E1–E5, P < 0.0001), Josm(0.0013 ± 0.0001 cm/min, mean CON; 0.0017 ± 0.0001 cm/min, mean E1–E5, P < 0.01). No significant differences were found for MTCM. IHC demonstrated strong staining for all treated animals and correlated with the ACL. This mouse model demonstrates that ip silicone catheters result in progressive FBR, altering the submesothelial anatomy and transperitoneal transport, and will form the basis for mechanistic studies in genetically-altered animals.

APA, Harvard, Vancouver, ISO, and other styles

42

Tuncay, K., and P. Ortoleva. "Salt tectonics as a self-organizing process: A reaction, transport, and mechanics model." Journal of Geophysical Research: Solid Earth 106, B1 (January 10, 2001): 803–17. http://dx.doi.org/10.1029/2000jb900107.

Full text

APA, Harvard, Vancouver, ISO, and other styles

43

Hamlington, K. L., Y. Y. Kwan, H. Fujioka, R. Cortez, and D. P. Gaver III. "Evaluation of Grid-Based and Grid-Free Methods to Model Microchannel Transport-Reaction." SIAM Journal on Scientific Computing 35, no. 4 (January 2013): B846—B867. http://dx.doi.org/10.1137/120880598.

Full text

APA, Harvard, Vancouver, ISO, and other styles

44

Forney, Larry J., J. Michael Brown, Bryan M. Kadlubowski, and Jude T. Sommerfeld. "Simplified Model for Oxygen Transport With Reaction in a Polymer-Electrolyte Fuel Cell." Canadian Journal of Chemical Engineering 83, no. 3 (May 19, 2008): 500–507. http://dx.doi.org/10.1002/cjce.5450830313.

Full text

APA, Harvard, Vancouver, ISO, and other styles

45

Horner, Christoph, Ekkehard Holzbecher, and Gunnar Nützmann. "A coupled transport and reaction model for long column experiments simulating bank filtration." Hydrological Processes 21, no. 8 (2007): 1015–25. http://dx.doi.org/10.1002/hyp.6276.

Full text

APA, Harvard, Vancouver, ISO, and other styles

46

Parkhurst, David L., and Laurin Wissmeier. "PhreeqcRM: A reaction module for transport simulators based on the geochemical model PHREEQC." Advances in Water Resources 83 (September 2015): 176–89. http://dx.doi.org/10.1016/j.advwatres.2015.06.001.

Full text

APA, Harvard, Vancouver, ISO, and other styles

47

Bektursunova, Rimma, and Ivan L'Heureux. "A reaction-transport model of periodic precipitation of pyrite in anoxic marine sediments." Chemical Geology 287, no. 3-4 (August 2011): 158–70. http://dx.doi.org/10.1016/j.chemgeo.2011.06.004.

Full text

APA, Harvard, Vancouver, ISO, and other styles

48

Singh, Raghvendra, Johannes Nitsche, and Stelios T. Andreadis. "An Integrated Reaction-Transport Model for DNA Surface Hybridization: Implications for DNA Microarrays." Annals of Biomedical Engineering 37, no. 1 (October 22, 2008): 255–69. http://dx.doi.org/10.1007/s10439-008-9584-y.

Full text

APA, Harvard, Vancouver, ISO, and other styles

49

Shang, Feng, Hyoungmin Woo, Jonathan B. Burkhardt, and Regan Murray. "Lagrangian Method to Model Advection-Dispersion-Reaction Transport in Drinking Water Pipe Networks." Journal of Water Resources Planning and Management 147, no. 9 (September 2021): 04021057. http://dx.doi.org/10.1061/(asce)wr.1943-5452.0001421.

Full text

APA, Harvard, Vancouver, ISO, and other styles

50

Tsai, Kuochen, Paul A. Gillis, Subrata Sen, and Rodney O. Fox. "A Finite-Mode PDF Model for Turbulent Reacting Flows." Journal of Fluids Engineering 124, no. 1 (April 25, 2001): 102–7. http://dx.doi.org/10.1115/1.1431546.

Full text

Abstract:

The recently proposed multi-environment model, R. O. Fox, 1998, “On the Relationship between Lagrangian Micromixing Models and Computational Fluid Dynamics,” Chem. Eng. Proc., Vol. 37, pp. 521–535. J. Villermaux and J. C. Devillon, 1994, “A Generalized Mixing Model for Initial Contacting of Reactive Fluids,” Chem. Eng. Sci., Vol. 49, p. 5127, provides a new category of modeling techniques that can be employed to resolve the turbulence-chemistry interactions found in reactive flows. By solving the Eulerian transport equations for volume fractions and chemical species simultaneously, the local concentrations of chemical species in each environment can be obtained. Assuming micromixing occurs only in phase space, the well-known IEM (interaction by exchange with the mean) model can be applied to close the micromixing term. This simplification allows the model to use micromixing timescales obtained from more sophisticated models and can be applied to any number of environments. Although the PDF shape doesn’t change under this assumption, the interaction between turbulence and chemistry can be resolved up to the second moments without any ad-hoc assumptions for the mean reaction rates. Furthermore, the PDF shape is found to have minimal effect on mean reaction rates for incompressible turbulent reacting flows. In this formulation, a spurious dissipation term arises in the transport equation of the scalar variances due to the use of Eulerian transport equations. A procedure is proposed to eliminate this spurious term. The model is applied to simulate the experiment of S. Komori, et al., 1993, “Measurements of Mass Flux in a Turbulent Liquid Flow With a Chemical Reaction,” AIChE J., Vol. 39, pp. 1611–1620, for a reactive mixing layer and the experiment of K. Li and H. Toor, 1986, “Turbulent Reactive Mixing With a Series Parallel reaction: Effect of Mixing on Yield,” AIChE J., Vol. 32, pp. 1312–1320, with a two-step parallel/consecutive reaction. The results are found to be in good agreement with the experimental data of Komori et al. and the PDF simulation of K. Tsai and R. Fox, 1994, “PDF Simulation of a Turbulent Series-Parallel Reaction in an Axisymmetric Reactor,” Chem. Eng. Sci., Vol. 49, pp. 5141–5158, for the experiment of Li and Toor. The resulting model is implemented in the commercial CFD code, FLUENT,1 and can be applied with any number of species and reactions.

APA, Harvard, Vancouver, ISO, and other styles

We offer discounts on all premium plans for authors whose works are included in thematic literature selections. Contact us to get a unique promo code!