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Phase equilibria of long-chain polyunsaturated fish oil fatty acid ethyl esters and carbon dioxide,ethane, or ethylene at reduced gas temperatures of 1.03 and 1.13
Affiliation:1. Healthy-Lipids Group, Sección Departamental de Ciencias de la Alimentación, Faculty of Sciences, Universidad Autónoma de Madrid, 28049 Madrid, Spain;2. Pharmacy and Biotechnology Department, School of Biomedical Sciences, Universidad Europea de Madrid, Madrid, Spain;3. Department of Biocatalysis, Institute of Catalysis, CSIC, 28049 Madrid, Spain;1. Midwest Biomedical Research/MB Clinical Research, Glen Ellyn, IL, United States;2. Great Lakes Clinical Trials, Chicago, IL, United States;1. School of Mathematics and Statistics, Ningbo University, Ningbo, 315211, Zhejiang Province, PR China;2. School of Mathematical Sciences, East China Normal University, Shanghai 200241, PR China;3. School of Mathematical Sciences, University of Science and Technology of China, Hefei, 230026, Anhui Province, PR China;1. Laboratory of Extraction, Applied Thermodynamics and Equilibrium (ExTrAE), Department of Food Engineering (DEA), Faculty of Food Engineering (FEA), University of Campinas (UNICAMP), Monteiro Lobato St. 80, 13083-862, Campinas, SP, Brazil;2. Faculty of Technology, University of Campinas (UNICAMP), Pascoal Marmo St. 1888, 13484-332, Limeira, SP, Brazil;1. DSM Nutritional Products, 6480 Dobbin Rd., Columbia, MD 21045, USA;2. DSM Nutritional Products, Wurmisweg 576, 4303 Kaiseraugst, Switzerland;3. Charles River Laboratories Preclinical Services, Spencerville, OH 45887, USA
Abstract:Phase equilibria of a mixture of long-chain polyunsaturated fish oil fatty acid ethyl esters (FAEEs) with carbon dioxide were measured at 313.2 and 343.2 K, with ethane at 314.0 and 344.6 K, and with ethylene at 290.9 and 318.6 K. The temperatures correspond to reduced gas temperatures of approximately 1.03 and 1.13. The experimental pressures range from 1.6 to 25 MPa. The FAEE mixture is rich in eicosapentaenoic acid ethyl ester (EPA, 52.5 wt.%), and docosahexaenoic acid ethyl ester (DHA, 36.1 wt.%), and a total of 10 components were identified. The experimental temperatures, pressures, solubilities, mass fractions, and calculated equilibrium ratios are reported in tables and graphs. The mass fractions and the equilibrium ratios are reported on a solvent-free basis.
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