Purification of Phosphoric Acid by Extraction with 2-Ethyl-1-Hexanol: Equilibrium Data and Mass Transfer Coefficients
Author:
Affiliation:
1. Departamento Ingeniería Química, Universidad de Alicante, Apartado 99, 03080 Alicante, Spain
Publisher
American Chemical Society (ACS)
Subject
Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/ie000065a
Reference38 articles.
1. PURIFICATION OF WET PROCESS PHOSPHORIC ACID BY SOLVENT EXTRACTION WITH ISOAMYL ALCOHOL. PART I. LIQUID-LIQUID EQUILIBRIUM OF THE WATER-PHOSPHORIC ACID-ISOAMYL ALCOHOL AT 25°C.
2. PURIFICATION OF WET PROCESS PHOSPHORIC ACID BY SOLVENT EXTRACTION WITH ISOAMYL ALCOHOL. PART II. STUDY OF THE IMPURITIES DISTRIBUTION.
3. Liquid-liquid equilibria for the quaternary system water-phosphoric acid-1-hexanol-cyclohexanone at 25.degree.C
4. Quaternary liquid–liquid equilibrium: water–phosphoric acid–1-butanol–2-butanone at 25°C
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