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Formation of Bioerodible Polymeric Microspheres and Microparticles by Rapid Expansion of Supercritical Solutions
Author(s) -
Tom Jean W,
Debenedetti Pablo G
Publication year - 1991
Publication title -
biotechnology progress
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.572
H-Index - 129
eISSN - 1520-6033
pISSN - 8756-7938
DOI - 10.1021/bp00011a004
Subject(s) - supercritical fluid , solubility , microparticle , polymer , nucleation , chemistry , nuclear chemistry , solvent , chemical engineering , lactic acid , acetone , microsphere , polymer chemistry , materials science , chromatography , organic chemistry , biology , bacteria , engineering , genetics
Polyhydroxy acids [poly(L‐lactic acid) (L‐PLA),poly(D,L‐lactic acid) (DL‐PLA), and poly(glycolic acid) (PGA)], biocompatible and bioerodible polymers that are being investigated for controlled delivery of pharmaceuticals and are approved by the Food and Drug Administration for in vivo sutures and bone repair implants, have been dissolved in supercritical CO 2 and precipitated by rapid expansion of the resulting supercritical solutions (RESS). The formation of these microparticles and microspheres is a first step toward the goal of producing, in a single processing step, drug‐loaded polymeric microspheres for use in controlled release applications. Nucleation of poly(L‐lactic acid) from CO 2 and CO 2 ‐acetone mixtures produced microparticles and microspheres ranging from 4 to 25 μm. Microspheres (2‐20 μm) were also obtained with chlorotrifluoromethane as solvent. Commercial L‐PLA precipitated after extraction of low molecular weight oligomers showed degradation kinetics similar to that of the starting material. The precipitation of DL‐PLA from CO 2 produced irregular‐sized particles (10‐20 μm). PGA, a polymer insoluble in most organic solvents, was found to be soluble in supercritical CO 2 . Nucleation of PGA from CO 2 produced both regular‐sized particles and needles of 10–40‐μm length. The total solubility of commercial L‐PLA in supercritical CO 2 at 250 bar and 55 °C decreased from 0.14 wt % to less than 0.05 wt % and then leveled off as the cumulative flow of CO 2 per unit mass of L‐PLA loaded in the extractor increased beyond 20 standard L of CO 2 /g of L‐PLA. Use of acetone (1 wt %) as a cosolvent increased L‐PLA solubility by ∼500%.