Representation of NH3-H2S-H2O, NH3-CO2-H2O, and NH3-SO2-H2O Vapor-Liquid Equilibria

1978111 citationsJournal Article

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ADVERTISEMENT RETURN TO ISSUEPREVArticleNEXTRepresentation of NH3-H2S-H2O, NH3-CO2-H2O, and NH3-SO2-H2O Vapor-Liquid EquilibriaDidier Beutier and Henri RenonCite this: Ind. Eng. Chem. Process Des. Dev. 1978, 17, 3, 220–230Publication Date (Print):July 1, 1978Publication History Published online1 May 2002Published inissue 1 July 1978https://pubs.acs.org/doi/10.1021/i260067a002https://doi.org/10.1021/i260067a002research-articleACS PublicationsRequest reuse permissionsArticle Views998Altmetric-Citations103LEARN 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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Process Optimization and Integration Phase Equilibria and Thermodynamics Thermal and Kinetic Analysis

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Published in: Industrial & Engineering Chemistry Process Design and Development

Volume 17, Issue 3, pp. 220-230

DOI: 10.1021/i260067a002

Field-Weighted Citation Impact: 7.66

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Representation of NH<sub>3</sub>-H<sub>2</sub>S-H<sub>2</sub>O, NH<sub>3</sub>-CO<sub>2</sub>-H<sub>2</sub>O, and NH<sub>3</sub>-SO<sub>2</sub>-H<sub>2</sub>O Vapor-Liquid Equilibria

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