Cited by 2,515Diffusion Coefficients in LiquidsAdsorption, diffusion, and thermodynamic properties of materialsGas Dynamics and Kinetic Theory

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NEW METHOD FOR PREDICTION OF BINARY GAS-PHASE DIFFUSION COEFFICIENTS

Fuller, Edward N., Schettler, Paul D., Giddings, J. Calvin.·1966·Industrial & Engineering Chemistry

DOI 10.1021/ie50677a007

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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

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“The Henry’s law constant and diffusion coefficient of prussic acid in the membrane pores were taken to be 1.64 3 10 3 (unitless, ratio of gas- to liquid-phase concentration) (Benjamin, 2002) and 1.82 3 10 5 m2/s (Fuller et al., 1966), respectively.”
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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
DOI: 10.1021/ie50677a007
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

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NEW METHOD FOR PREDICTION OF BINARY GAS-PHASE DIFFUSION COEFFICIENTS

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