Masters Theses
Date of Award
8-1989
Degree Type
Thesis
Degree Name
Master of Science
Major
Chemical Engineering
Major Professor
Paul R. Bienkowski
Committee Members
H. D. Cochran, H. W. Hsu
Abstract
Supercritical fluid extraction is receiving widespread attention as a possible separation process for the food and pharmaceutical Industries since it can be conducted at near-ambient conditions with non-toxic solvents. This study is concerned with investigating the feasibility of separation and isolation of penicillin V using supercritical fluids. A flow apparatus has been constructed and used to determine the high pressure solid-fluid equilibrium solubilities. An absorption spectroscopic method is used to analyze the sample solutions. The solubility of penicillin V in supercritical Carbon dioxide has been measured from 314.85 K to 334.85 K and from 1144 psig to 4050 psig. The solubility ranges from 5.2 x 105 to 5.6 x 104 mole fraction. It was determined that penicillin V can dissolve In supercritical carbon dioxide at concentrations 106-108 greater than that predicted by the ideal gas law. The problems associated with penicillin V and mixed solvents are discussed. The equilibrium solubility is correlated using a compressed gas model with the Peng-Robinson equation of state. The unknown physical properties of penicillin V are estimated using group contribution methods. This model correlates penicillin V solubilities within about 60 %.
Recommended Citation
Ko, Min-Jin, "Solubility studies on the antibiotic penicillin V using supercritical fluids. " Master's Thesis, University of Tennessee, 1989.
https://trace.tennessee.edu/utk_gradthes/12990