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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
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“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]
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“volume calculated by the method of Fuller et al. (1966) .”
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“(PVP6) 1016c 49.0c 68.3c a Wohlfarth and Wohlfarth (1997), b VDI-Wärmeatlas (1994), c Own measurements, d Wilke and Chang (1955), e Fuller et al. (1966).”
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“The error bars indicate ±10 % around the Matsunaga et al. (1993, 1998, 2002) values (or Chen and Othmer (1962) for CH3CCl3 and Fuller et al. (1966) for HCFC-141b where Matsunaga et al. (1993, 1998, 2002) values are not available).”
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“[59]; is the voidage in the particulate phase and 2 , the tortuosity, corrects for the fact that some area for flow is occupied by fluidised particles, and that the diffusion path is lengthened by gas having to diffuse around these particles.”
Background
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
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