Physiological fluid separation vehicles having improved resistance to inward migration of therapeutic agent
A composition, plasma technology, applied in the field of polyester, polyester composition
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Embodiment 1
[0043] Into a 5 L reaction flask equipped with a stirrer, inert gas inlet thermostat, and down-distilling Vigreaux fractionation column, were charged 0.3 equivalents of phthalic anhydride (442.5 g, using a scaling factor), 0.3 equivalents of methane isphthalic acid (497.5 g), 0.29 equivalents of dimer acid (1650 g), 0.3 equivalents of 1,2-propanediol (227.5 g) and 0.9 equivalents of neopentyl glycol (932.5 g). Water is distilled from the reflux while heating under an inert gas stream. The acid value after 21 hours was 3.3. The apparatus was evacuated at 200 mm Hg for 1 hour and then at 4 mm Hg for 17.5 hours. The viscosity of the resulting product is 876 cSt / 99°C, and its density (ρ 25 ) is 1.0441.
Embodiment 2
[0045] Get the product of 500g embodiment 1, handle with the acetylation of 130g acetic anhydride, the acid number of product is 1.2, ρ 25 is 1.0455 and the hydroxyl number is 1.4.
Embodiment 3
[0047] In the product of embodiment 2, add the two-nor-butyltin diacetic acid that accounts for 0.03% of product net weight, then reflux for 40 minutes, and vacuum distillation under 14-2mmHg for 65 minutes, the viscosity of gained product is 1930 cSt / 99 ℃ , ρ 25 is 1.0447.
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