Process for producing microparticles
An object of the present invention is to provide a solvent which is able to produce microparticles where content of the drug is still high and no initial burst takes place even when a drug having a low solubility in a halogenated hydrocarbon solvent is used. The present invention provides a process for production by a solvent-evaporation microencapsulation method, of microparticles which are composed of biodegradable polymer and contain a drug having a low solubility in a halogenated hydrocarbon, which is characterized in that the drug and the biodegradable polymer are dissolved in a mixed solvent comprising a first solvent: halogenated hydrocarbon, and a second solvent: a water-immiscible organic solvent in which solubility of the above-mentioned drug is 0.3% (w/v) or more.
1. A process for production, by a solvent-evaporation microencapsulation method, of microparticles which are composed of a biodegradable polymer and contain a steroid agent, wherein the steroid agent and the biodegradable polymer are dissolved in a mixed solvent comprising dichloromethane and a phenylalkyl alcohol, wherein a mixing ratio of the dichloromethane to the phenylalkyl alcohol is 1:1 to 1:10, a particle size of the microparticles is 500 nm to 150 μm and an initial burst of the steroid agent in the microparticles is lower than in microparticles produced using a non-halogenated solvent and phenylalkyl alcohol.
2. The process for production according to claim 1 , wherein the steroid agent is betamethasone, dexamethasone or prednisolone.
3. The process for production according to claim 1 , wherein the biodegradable polymer is poly(lactic acid) or (lactic acid)-(glycolic acid) copolymer.
4. A process for production of microparticles in which a steroid agent and a biodegradable polymer are dissolved in a mixed solvent comprising dichloromethane and a phenylalkyl alcohol to form an oily phase, the oily phase is mixed with an aqueous phase to form an o/w type emulsion and then said mixed solvent is removed to produce the microparticles, wherein a mixing ratio of the dichloromethane and the phenylalkyl alcohol is 1:1 to 1:10, a particle size of the microparticles is 500 nm to 150 μm, and an initial burst of the steroid agent in the microparticles is lower than in microparticles produced using a non-halogenated solvent and phenylalkyl alcohol.
5. The process for production according to claim 1 , wherein the steroid agent is betamethasone; the biodegradable polymer is poly(lactic acid) or (lactic acid)-(glycolic acid) copolymer; and the phenylalkyl alcohol is benzyl alcohol.
6. The process for production according to claim 4 , wherein the steroid agent is betamethansone; the biodegradable polymer is poly(lactic acid) or (lactic acid)-(glycolic acid) copolymer; and the phenylalkyl alcohol is benzyl alcohol.
7. An injection preparation comprising the microparticles produced by the process according to claim 1 .
8. An injection preparation comprising the microparticles produced by the process according to claim 2 .
9. An injection preparation comprising the microparticles produced by the process according to claim 3 .
10. An injection preparation comprising the microparticles produced by the process according to claim 4 .
11. An injection preparation comprising the microparticles produced by the process according to claim 5 .
12. An injection preparation comprising the microparticles produced by the process according to claim 6 .