The DOI matches its Crossref record.
NEW METHOD FOR PREDICTION OF BINARY GAS-PHASE DIFFUSION COEFFICIENTS
Abstract
ADVERTISEMENT RETURN TO ISSUEPREVArticleNEXTNEW METHOD FOR PREDICTION OF BINARY GAS-PHASE DIFFUSION COEFFICIENTSEdward N. Fuller, Paul D. Schettler, and J. Calvin. GiddingsCite this: Ind. Eng. Chem. 1966, 58, 5, 18–27Publication Date (Print):May 1, 1966Publication History Published online1 May 2002Published inissue 1 May 1966https://pubs.acs.org/doi/10.1021/ie50677a007https://doi.org/10.1021/ie50677a007research-articleACS PublicationsRequest reuse permissionsArticle Views12407Altmetric-Citations1654LEARN ABOUT THESE METRICSArticle Views are the COUNTER-compliant sum of full text article downloads since November 2008 (both PDF and HTML) across all institutions and individuals. These metrics are regularly updated to reflect usage leading up to the last few days.Citations are the number of other articles citing this article, calculated by Crossref and updated daily. Find more information about Crossref citation counts.The Altmetric Attention Score is a quantitative measure of the attention that a research article has received online. Clicking on the donut icon will load a page at altmetric.com with additional details about the score and the social media presence for the given article. Find more information on the Altmetric Attention Score and how the score is calculated. Share Add toView InAdd Full Text with ReferenceAdd Description ExportRISCitationCitation and abstractCitation and referencesMore Options Share onFacebookTwitterWechatLinked InRedditEmail Other access options Get e-Alerts
Overview
Integrity signals
Registry
Cites
Statistics
Verification
Claims the paper makes
Claims other papers make about this one
Each is checked against this paper’s own text: does it say what the citing paper says it does?
In the citing paper
“The maximum operating temperature of the membrane, is typically 90 °C and should not be exceeded so as to avoid reduced proton mobility through the membrane, [154] as well as flooding due to increased water crossover from the anode.[145,250]”
From Electrochemical CO 2 Reduction into Chemical Feedstocks: From Mechanistic Electrocatalysis Models to System Design (2019) · cites this paper as [250]
Citations
Cited by
Sorted by citations
Items 601–700 of 1,000
A numerical modeling study on the influence of porosity changes during thermochemical heat storage
Seitz, G., Helmig, R., & Class, H. (2019) · Applied Energy · doi:10.1016/j.apenergy.2019.114152 · Cited by 30
Ozturk, T., & Erbil, H. Y. (2020) · Langmuir · doi:10.1021/acs.langmuir.9b03590 · Cited by 30
Kinetic study of glycerol steam reforming catalyzed by a Ni-promoted metallurgical residue
Desgagnés, A., & Iliuta, M. C. (2021) · Chemical Engineering Journal · doi:10.1016/j.cej.2021.132278 · Cited by 30
Cesário, M. T., de Wit, H. L., TRAMPER, J., et al. (1997) · Biotechnology Progress · doi:10.1021/bp970043s · Cited by 30
A numerical study of fixed bed reactor modelling for steam methane reforming process
Rout, K. R., & Jakobsen, H. A. (2015) · The Canadian Journal of Chemical Engineering · doi:10.1002/cjce.22202 · Cited by 30
Wang, G., Reckhorn, S. B. F., & Grathwohl, P. (2003) · Vadose Zone Journal · doi:10.2113/2.4.692 · Cited by 30
Torri, C., & Fabbri, D. (2009) · Microchemical Journal · doi:10.1016/j.microc.2009.05.010 · Cited by 30
Jeong, A., Shin, D., Baek, S. M., et al. (2018) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2018.06.059 · Cited by 30
Influence of retention on band broadening in turbulent-flow liquid and gas chromatography
Martin, M., & Guiochon, G. A. (1982) · Analytical Chemistry · doi:10.1021/ac00246a019 · Cited by 30
Influence of Sampler Configuration on the Uptake Kinetics of a Passive Air Sampler
Zhang, X., Wong, C., Lei, Y. D., et al. (2011) · Environmental Science & Technology · doi:10.1021/es203292x · Cited by 30
Lahvis, M. A., & Baehr, A. L. (1997) · Antarctica A Keystone in a Changing World · doi:10.3133/ofr97630 · Cited by 30
Hue, V., Cavalié, T., Dobrijevic, M., Hersant, F., & Greathouse, T. K. (2015) · Icarus · doi:10.1016/j.icarus.2015.04.001 · Cited by 30
“The molecular diffusion coefficient we adopt is based on experimental measurements of binary gas diffusion coefficients (Fuller et al., 1966, 1969).”
MethodModeling of adsorption process on monolith adsorbents: A mini-review
Pour, S. E., Mamaghani, A. H., & Hashisho, Z. (2024) · Separation and Purification Technology · doi:10.1016/j.seppur.2024.128846 · Cited by 29
Study on the impact of hydrogen-natural gas mixing on working cycles of underground gas storage
Liao, Y., Wang, Y., Lv, M., et al. (2025) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2025.03.384 · Cited by 29
Measurements of diffusion coefficients by the method of gas chromatography
Huang, T., Yang, F. J. F., Huang, C., et al. (1972) · Journal of Chromatography A · doi:10.1016/s0021-9673(01)91051-9 · Cited by 29
Seasonal and spatial evasion of mercury from the western Mediterranean Sea
Mastromonaco, M. N., Gårdfeldt, K., & Wängberg, I. (2017) · Marine Chemistry · doi:10.1016/j.marchem.2017.02.003 · Cited by 29
Geng, C., Shao, Y., Bian, Z., et al. (2019) · Chemical Engineering Journal · doi:10.1016/j.cej.2019.123977 · Cited by 29
Serincan, M. F., Pasaogullari, U., & Singh, P. (2020) · Journal of Power Sources · doi:10.1016/j.jpowsour.2020.228310 · Cited by 29
On the mechanisms that sustain the inception of attached cavitation
Ram, O., Agarwal, K., & Katz, J. (2020) · Journal of Fluid Mechanics · doi:10.1017/jfm.2020.646 · Cited by 29
AL-bonsrulah, H. A. Z., Alshukri, M. J., Mikhaeel, L. M., et al. (2021) · Energies · doi:10.3390/en14092643 · Cited by 29
“A dynamic simulation model was developed that explains the design and analysis of this system and the monitoring and analysis of system performance for the solar system, and the output constant voltage is evaluated within the AC/DC exchanger and connected with the other components of the system [22].”
MethodEller, J., Sauerborn, T., Becker, B., Buntic, I., Groß, J., & Helmig, R. (2022) · Water Resources Research · doi:10.1029/2021wr030885 · Cited by 32
“Property Model Hydrogen density 𝐴𝐴 𝐴𝐴H2 Ideal gas law Water density 𝐴𝐴 𝐴𝐴H2O IAPWS (Wagner & Kretzschmar, 2008) Hydrogen viscosity 𝐴𝐴 𝐴𝐴H2 Chung (Chung et al., 1988) Water viscosity 𝐴𝐴 𝐴𝐴H2O IAPWS (Cooper & Dooley, 2008) Diffusion coefficient gas phase Fuller (Fuller et al., 1966) Diffusion coefficient liquid phase Ap…”
MethodInfluentialInteractions between a propagating detonation wave and circular water cloud in hydrogen/air mixture
Xu, Y. C., & Zhang, H. (2022) · Combustion and Flame · doi:10.1016/j.combustflame.2022.112369 · Cited by 29
Iron ore reduction by methane partial oxidation in a porous media
Palacios, P., Mario Toledo, T., & Cabrera, M. (2015) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2015.05.058 · Cited by 29
Aerosol speciation and mass prediction from toluene oxidation under high NOx conditions
Kelly, J. L., Michelangeli, D. V., Makar, P. A., et al. (2009) · Atmospheric Environment · doi:10.1016/j.atmosenv.2009.10.035 · Cited by 29
Modeling of the SCR reactor for coal-fired power plants: Impact of NH3 inhibition on Hg0 oxidation
Beretta, A., Usberti, N., Lietti, L., et al. (2014) · Chemical Engineering Journal · doi:10.1016/j.cej.2014.06.114 · Cited by 29
Krishna, R. (2016) · Industrial & Engineering Chemistry Research · doi:10.1021/acs.iecr.6b00762 · Cited by 29
Selective active oxidation in hafnium boride-silicon carbide composites above 2000 °C
Poerschke, D. L., Novak, M. D., Abdul-Jabbar, N. M., et al. (2016) · Journal of the European Ceramic Society · doi:10.1016/j.jeurceramsoc.2016.05.048 · Cited by 29
Modeling of intensified glycerol steam reforming in a heat-exchange integrated microchannel reactor
Delparish, A., & Avci, A. K. (2017) · Catalysis Today · doi:10.1016/j.cattod.2017.03.029 · Cited by 29
Interaction of cylindrically converging diffracted shock with uniform interface
Liang, Y., Ding, J., Zhai, Z., et al. (2017) · Physics of Fluids · doi:10.1063/1.4997071 · Cited by 29
Fougerit, V., Pozzobon, V., Pareau, D., et al. (2018) · Journal of Membrane Science · doi:10.1016/j.memsci.2018.10.042 · Cited by 29
“The empirical Fuller equation is used to estimate binary diffusion coefficients DAB g [59].”
MethodA comprehensive mathematical model for nanofibre formation in centrifugal spinning methods
Noroozi, S., Arne, W., Larson, R. G., & Taghavi, S. M. (2020) · Journal of Fluid Mechanics · doi:10.1017/jfm.2020.196 · Cited by 29
Wang, G., Reckhorn, S. B. F., & Grathwohl, P. (2003) · Vadose Zone Journal · doi:10.2136/vzj2003.6920 · Cited by 29
“The tailing of the diffusive fluxes seals, which improved the mass balance in the experi- † Calculated by the FSG method (Fuller–Schettler–Giddings) for prediction of binary gas-phase diffusion coefficients (Fuller et al., 1966).”
MethodForced convective boiling of binary mixtures in annular flow. Part II: heat and mass transfer
Barbosa, J. R., Jr., & Hewitt, G. F. (2001) · International Journal of Heat and Mass Transfer · doi:10.1016/s0017-9310(00)00210-6 · Cited by 29
Evaluating the Onda Mass Transfer Correlation for the Design of Packed‐Column Air Stripping
Staudinger, J., Knocke, W. R., & Randall, C. W. (1990) · American Water Works Association · doi:10.1002/j.1551-8833.1990.tb06908.x · Cited by 29
Aerosol formation in reacting gases: Theory and application to the anhydrous NH3‐HCL system
Dahlin, R. S., Su, J., & Peters, L. K. (1981) · AIChE Journal · doi:10.1002/aic.690270310 · Cited by 29
Efficiency of silicone-grease-coated denuders for collection of polynuclear aromatic hydrocarbons
Coutant, R. W., Callahan, P. J., Chuang, J. C., et al. (1992) · Atmospheric Environment Part A General Topics · doi:10.1016/0960-1686(92)90020-l · Cited by 29
Papkov, V. S., & Pashchenko, D. (2025) · Fuel · doi:10.1016/j.fuel.2025.134906 · Cited by 28
Heterogeneous uptake of NO2 on soils under variable temperature and relative humidity conditions
Wang, L., Wang, W., & Ge, M. (2012) · Journal of Environmental Sciences · doi:10.1016/s1001-0742(11)61015-2 · Cited by 28
Sohn, S., Nam, J. H., Jeon, D. H., et al. (2010) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2010.08.063 · Cited by 28
Onel, O., Niziolek, A. M., Butcher, H., et al. (2017) · Computers & Chemical Engineering · doi:10.1016/j.compchemeng.2017.01.016 · Cited by 28
Surface effects in a capacitive argon discharge in the intermediate pressure regime
Guðmundsson, J. T., Krek, J., Wen, D., Kawamura, E., & Lieberman, M. A. (2021) · Plasma Sources Science and Technology · doi:10.1088/1361-6595/ac3ba1 · Cited by 28
Bekaert, D. V., Barry, P. H., Broadley, M. W., Byrne, D. J., Marty, B. M., Ramírez, C. J., de Moor, J. M., Rodríguez, A., Hudak, M. R., Subhas, A. V., et al. (2023) · Science Advances · doi:10.1126/sciadv.adg2566 · Cited by 29
“Fractionation factors can be computed from the ratios of binary diffusion coefficients for two gas pairs (molecules or isotopes) ( 30 , 31 ).”
Arands, R. R., Lam, T., Massry, I. W., et al. (1997) · Water Resources Research · doi:10.1029/96wr03976 · Cited by 28
CORN ROOT INFLUENCE ON AUTOMATED MEASUREMENT OF SOIL CARBON DIOXIDE CONCENTRATIONS
Chen, D., Molina, J. A. E., Clapp, C. E., et al. (2005) · Soil Science · doi:10.1097/01.ss.0000190512.41298.fc · Cited by 28
“(5) is used to calculate CO2 diffusivity in soil air, D = DG, 4 = *, D0 is CO2 diffusivity in free air (no soil), and its values at different temperatures can be calculated with the equation of Fuller et al. (1966).”
BackgroundModelling mass transfer in the PCA process using the Maxwell–Stefan approach
de Diego, Y. P., Wubbolts, F. E., & Jansens, P. J. (2005) · The Journal of Supercritical Fluids · doi:10.1016/j.supflu.2005.07.002 · Cited by 28
Ledesma, E. B., Campos, C., Cranmer, D. J., Foytik, B. L., Ton, M. N., Dixon, E. A., Chirino, C., Batamo, S., & Roy, P. (2013) · Energy & Fuels · doi:10.1021/ef3018332 · Cited by 29
Modeling and simulation of CO2 capture using semipermeable elastic microcapsules
Finn, J. R., & Galvin, J. E. (2018) · International journal of greenhouse gas control · doi:10.1016/j.ijggc.2018.04.022 · Cited by 28
Kiel, J. H. A., Prins, W., & Swaaij, W. P. M. V. (1992) · Chemical Engineering Science · doi:10.1016/0009-2509(92)85105-k · Cited by 28
Modeling and design of vapor‐phase biofiltration for chlorinated volatile organic compounds
Den, W., & Pirbazari, M. (2002) · AIChE Journal · doi:10.1002/aic.690480921 · Cited by 28
Fate and effects of 3,4-dichloroaniline in the laboratory and in outdoor ponds: I. fate
Wolff, C. J. M., & Crossland, N. O. (1985) · Environmental Toxicology and Chemistry · doi:10.1002/etc.5620040408 · Cited by 28
High‐Temperature Steam Electrolysis
Laurencin, J., & Mougin, J. (2015) · doi:10.1002/9783527676507.ch6 · Cited by 28
Gas Heated Steam Reformer Modelling
Wesenberg, M. H. (2006) · BIBSYS Brage (BIBSYS (Norway)) · Cited by 28
Immonen, J., & Powell, K. M. (2024) · Chemical Engineering Science · doi:10.1016/j.ces.2024.120637 · Cited by 27
Torkavannejad, A., Sadeghifar, H., Pourmahmoud, N., et al. (2015) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2015.07.038 · Cited by 27
Serpentine diffusion trajectories and the Ouzo effect in partially miscible ternary liquid mixtures
Krishna, R. (2015) · Physical Chemistry Chemical Physics · doi:10.1039/c5cp04520g · Cited by 27
Tropospheric observations of CFC-114 and CFC-114a with a focus on long-term trends and emissions
Laube, J. C., Hanif, N. M., Martinerie, P., et al. (2016) · Atmospheric chemistry and physics · doi:10.5194/acp-16-15347-2016 · Cited by 27
“To our knowledge, no measurement is available for CFC-114a, but the estimation methods commonly used in firn models (Fuller et al., 1966; Chen and Othmer, 1962; Marsh et al., 2007) provide the same diffusion coefficient for CFC-114 and CFC-114a within uncertainties, which we therefore use here.”
MethodModelling study of two chemical looping reforming reactor configurations: looping vs. switching
Morgado, J. F., Cloete, S. W. P., Morud, J. C., Gurker, T., & Amini, S. (2016) · Powder Technology · doi:10.1016/j.powtec.2016.11.059 · Cited by 27
Heal, M. R., LAXEN, D. P. H., & Marner, B. (2019) · Atmosphere · doi:10.3390/atmos10070357 · Cited by 26
“[56] for the ‘Fuller’ semi-empirical estimation method for gas-phase diffusion coefficients [57,58], 999 the absolute values are substantially smaller than the value of D = 0.”
MethodSohaib, Q., Gómez‐Coma, L., Albo, J., Druon-Bocquet, S., Irabien, Á., Younas, M., & Sánchez, J. (2019) · Journal of Chemical Technology & Biotechnology · doi:10.1002/jctb.6265 · Cited by 28
Fache, A., & Marías, F. (2019) · Renewable Energy · doi:10.1016/j.renene.2019.11.081 · Cited by 27
Chen, C., Wang, J., Li, L., Xu, W., & Liu, J. (2020) · Environment International · doi:10.1016/j.envint.2020.105718 · Cited by 29
Aydın, M., Britten, G. L., Montzka, S. A., et al. (2020) · Journal of Geophysical Research Atmospheres · doi:10.1029/2020jd033074 · Cited by 27
“Molecular diffusivities are calculated from empirical relationships (Fuller et al., 1966; Wilke & Lee, 1955).”
MethodThe ignition of fine iron particles in the Knudsen transition regime
Jean-Philyppe, J., Fujinawa, A., Bergthorson, J. M., et al. (2023) · Combustion and Flame · doi:10.1016/j.combustflame.2023.112869 · Cited by 27
“The oxidizer mass diffusivity in the binary mixture is computed with the Fuller-Schettler-Giddins semi-empirical correlation [36]:”
MethodHe, X., Shen, J., Iyer, S., et al. (2023) · Atmospheric measurement techniques · doi:10.5194/amt-16-4461-2023 · Cited by 27
“imental values; (2) calculated by kinetic theory; or (3) calculated based on elemental composition using Fuller’s method (Fuller et al., 1966).”
MethodLlano-Restrepo, M., & Araujo-López, E. (2015) · International journal of greenhouse gas control · doi:10.1016/j.ijggc.2015.08.008 · Cited by 27
Oh, S.-K. (2013) · Journal of Thermodynamics · doi:10.1155/2013/828620 · Cited by 27
Model-based hazard identification in multiphase chemical reactors
Labovská, Z., Labovský, J., Jelemenský, Ľ., et al. (2014) · Journal of Loss Prevention in the Process Industries · doi:10.1016/j.jlp.2014.02.004 · Cited by 27
Ji, G., Wang, G., Hooman, K., et al. (2014) · Chemical Engineering Science · doi:10.1016/j.ces.2014.02.006 · Cited by 27
An easy parameter estimation procedure for modeling a HT-PEMFC
Úbeda, D., Pinar, F. J., Cañizares, P., et al. (2012) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2012.04.157 · Cited by 27
Worton, D. R., Sturges, W. T., Reeves, C. E., Newland, M. J., Penkett, S. A., Atlas, E., Stroud, V., Johnson, K., Schmidbauer, N., Solberg, S., et al. (2012) · Atmospheric Environment · doi:10.1016/j.atmosenv.2012.02.084 · Cited by 27
Application of Stefan–Maxwell approach to azeotropic separation by membrane distillation
BANAT, F. A., Al‐Rub, F. A. A., Jumah, R., et al. (1999) · Chemical Engineering Journal · doi:10.1016/s1385-8947(99)00016-9 · Cited by 27
Martin, N. A., Leming, E. J., Henderson, M. H., et al. (2010) · Atmospheric Environment · doi:10.1016/j.atmosenv.2010.06.014 · Cited by 27
Guo, Z., & Roache, N. F. (2003) · The Annals of Occupational Hygiene · doi:10.1093/annhyg/meg035 · Cited by 27
Advances in Computational Fluid Dynamics (CFD) Modeling of In-Cylinder Biodiesel Combustion
Cheng, X., Ng, H. K., Gan, S., et al. (2013) · Energy & Fuels · doi:10.1021/ef4005237 · Cited by 27
Pourmahmoud, N., Sadeghifar, H., & Torkavannejad, A. (2016) · International Journal of Heat and Mass Transfer · doi:10.1016/j.ijheatmasstransfer.2016.12.058 · Cited by 27
Chen, L., Wang, C., Wang, Z., et al. (2017) · Fuel · doi:10.1016/j.fuel.2017.07.018 · Cited by 27
Prokop, T. A., Berent, K., Moździerz, M., et al. (2019) · Energies · doi:10.3390/en12244784 · Cited by 27
“where p is the total pressure in Pascals, Mn is the molar mass of species i, vi is its specific, cross sectional constant in the Fuller–Schettler–Giddings correlation [37], and dpore (m) is the pore diameter.”
BackgroundBirkham, T. K., Hendry, M. J., Wassenaar, L. I., Mendoza, C. A., & Lee, E. S. (2002) · Environmental Science & Technology · doi:10.1021/es020587c · Cited by 27
Development of a Passive Sampler To Measure Personal Exposure to Gaseous PAHs in Community Settings
Fan, Z. T., Jung, K. H., & Lioy, P. J. (2006) · Environmental Science & Technology · doi:10.1021/es060474j · Cited by 27
Diffusion of Sorbing Organic Chemicals in the Liquid and Gaseous Phases of Repacked Soil
Olesen, T., Gamst, J., Møldrup, P., et al. (2001) · Soil Science Society of America Journal · doi:10.2136/sssaj2001.1585 · Cited by 27
Hendry, M. J., Wassenaar, L. I., & Birkham, T. K. (2002) · Geochimica et Cosmochimica Acta · doi:10.1016/s0016-7037(02)00949-3 · Cited by 27
Modeling of air stripping from volatile organic compounds in biological treatment processes
Soltanali, S., & Hagani, Z. S. (2008) · International Journal of Environmental Science and Technology · doi:10.1007/bf03326030 · Cited by 27
“The diffusivities of VOCs in air were estimated, using the method of Fuller, Schetter and Giddings (Fuller et al., 1966): ( ) 3 1.7510 21/3 1/3 T Mr DAVOC P V V BA − = + Jarvis and Lugg (1968) state that this is the most accurate method for chlorinated aliphatics, aromatics, alkanes and ketones and…”
MethodInfluentialGas-polarographic multifunctional sensor: oxygen-humidity sensor
Usui, T., Kurumiya, Y., Nuri, K., et al. (1989) · Sensors and Actuators · doi:10.1016/0250-6874(89)85005-x · Cited by 27
Zamehrian, M., & Sedaee, B. (2024) · Gas Science and Engineering · doi:10.1016/j.jgsce.2024.205217 · Cited by 26
Shin, M.-S., Park, N., Park, M., et al. (2013) · Fuel Processing Technology · doi:10.1016/j.fuproc.2013.09.006 · Cited by 26
The Kinetics of Isothermal Hydrogen Reduction of Nanocrystalline Fe2O3 Powder
Lee, G., Choi, J., Song, J.-I., et al. (2014) · MATERIALS TRANSACTIONS · doi:10.2320/matertrans.m2014182 · Cited by 26
Zaidiza, D. A., Wilson, S. G., Belaissaoui, B., et al. (2016) · Chemical Engineering Science · doi:10.1016/j.ces.2016.01.053 · Cited by 26
Hybrid global model of water cluster ions in atmospheric pressure Ar/ H 2 O RF capacitive discharges
Tavant, A., & Lieberman, M. A. (2016) · Journal of Physics D Applied Physics · doi:10.1088/0022-3727/49/46/465201 · Cited by 26
Wu, X., & Ghoniem, A. F. (2017) · ChemSusChem · doi:10.1002/cssc.201701372 · Cited by 26
Modeling and simulation of water-gas shift in a heat exchange integrated microchannel converter
Bac, S., Keskın, S., & Avci, A. K. (2017) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2017.09.141 · Cited by 26
Abdelaziz, A., Zaitsau, D. H., Buzyurov, A. V., Minakov, A. A., Verevkin, S. P., & Schick, C. H. (2019) · Thermochimica Acta · doi:10.1016/j.tca.2019.05.008 · Cited by 26
Time-resolved flow field and thermal loads in a single-element GOx/GCH4 rocket combustor
Zips, J., Traxinger, C., & Pfitzner, M. (2019) · International Journal of Heat and Mass Transfer · doi:10.1016/j.ijheatmasstransfer.2019.118474 · Cited by 26
Fernandez‐Bou, A. S., Dierick, D., Allen, M. F., & Harmon, T. C. (2020) · Global Change Biology · doi:10.1111/gcb.15194 · Cited by 26
Adsorption of methyl iodide on reduced silver‐functionalized silica aerogel: Kinetics and modeling
Tang, S., Choi, S., Nan, Y., et al. (2020) · AIChE Journal · doi:10.1002/aic.17137 · Cited by 26
Synthesis of hollow spherical nickel oxide and its gas‐sensing properties
Geng, W., Cao, X.-R., Xu, S.-L., et al. (2021) · Rare Metals · doi:10.1007/s12598-020-01639-3 · Cited by 26
Gurrala, P., Balusamy, S., Banerjee, S., et al. (2021) · Fluid dynamics & materials processing · doi:10.32604/fdmp.2021.014126 · Cited by 26
“The average diffusion coefficient is calculated as [51] Figure 9: Comparison of the evolutions of the normalized volume a binary droplet of ethanol 50% + water 50% V=V0 ð Þ with normalized time t=te ð Þ obtained from the experiments and theoretical modeling at (a) Ts 1⁄4 25 C and (b) 50 C, respectively (done by Gurral…”
MethodPulsating propagation and extinction of hydrogen detonations in ultrafine water sprays
Xu, Y. C., & Zhang, H. (2022) · Combustion and Flame · doi:10.1016/j.combustflame.2022.112086 · Cited by 26
“where Sh is the Sherwood number, Df is the vapor mass diffusivity in the gas phase [41], and Sc is the Schmidt number of gas phase.”
BackgroundIannello, S., Foscolo, P. U., & Materazzi, M. (2021) · Chemical Engineering Journal · doi:10.1016/j.cej.2021.133807 · Cited by 26
Song, T., & Xu, J. (2023) · Combustion and Flame · doi:10.1016/j.combustflame.2023.112946 · Cited by 26
Multiphase Multicomponent Transport Modeling of Cyclic Solvent Injection in Shale Reservoirs
Ma, M., & Emami‐Meybodi, H. (2023) · SPE Journal · doi:10.2118/210480-pa · Cited by 26
Metadata
- Authors
- Fuller, E. N., Schettler, P. D., & Giddings, J. C.
- Venue
- Industrial & Engineering Chemistry
- Publisher
- American Chemical Society (ACS)
- Published
- 1966-05-01
- Volume
- 58
- Issue
- 5
- Pages
- 18-27
- ISSN
- 0019-7866 (ISSN-L)
- 1541-5724
- OpenAlex
- W2075886908
- Cited by
- 2,515
- References
- 0
- Citations by year
- 2026: 141 · 2025: 141 · 2024: 160 · 2023: 130 · 2022: 148 · 2021: 136 · 2020: 134 · 2019: 124 · 2018: 113 · 2017: 108 · 2016: 101 · 2015: 81 · 2014: 99 · 2013: 71 · 2012: 99
- FWCI
- 2.12
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- Industrial & Engineering Chemistry (publishedVersion)
- Topics
- Physical Sciences › Chemistry › Physical and Theoretical Chemistry › Diffusion Coefficients in Liquids
- Physical Sciences › Chemistry › Physical and Theoretical Chemistry › Adsorption, diffusion, and thermodynamic properties of materials
- Physical Sciences › Mathematics › Applied Mathematics › Gas Dynamics and Kinetic Theory
- Keywords
- diffusion coefficient, forecasting methods, gas mixtures, transport properties
About these checks
Registry, retraction, Cites and statistics results are computed, not judged, with one exception: a printed reference that no index lists is read once by a model before it counts as a citation error. Claims are extracted by a model and kept only when their quote appears verbatim in the text; each cited source is then checked, with a model’s help, for whether it says what the claim relies on. Those verdicts can be wrong — read the claim’s quote and the cited source before relying on one.
Statistics and arithmetic are recomputed, not judged.
Confidence bands are shown only for fields calibrated on our annotated test set. None is calibrated yet, so no band is shown.
What counts as a claim ›How we measure confidence ›How we check this ›
Are you an author, or do you see a problem with this page? Request a review