Process for producing porous particles of a polyhydroxyalkanoate (PHA), porous particles obtainable from said process and cosmetic compositions comprising the same
A process for producing porous particles of a polyhydroxyalkanoate (PHA) includes the following steps: providing a spray drying atomization chamber heated to an operating temperature comprised between 50° C. and 300° C.; providing an aqueous suspension having the PHA and an expanding agent which decomposes at the operating temperature of the atomization chamber, with the formation of at least one gaseous compound; and injecting the aqueous suspension into the atomization chamber provided at the operating temperature, so as to cause instantaneous evaporation of the aqueous suspension and decomposition of the expanding agent, with formation of the porous PHA particles. The particles obtained from said process can be used to obtain cosmetic compositions that are soft to the touch, with high oil absorbing capacities and high flow index, able to generate a uniform, filling effect for wrinkles and skin furrows, making the skin more glossy and compact.
1. A process for producing porous particles of a polyhydroxyalkanoate (PHA), which comprises the following steps:
providing a spray drying atomization chamber heated to an operating temperature comprised between 50° C. and 300° C.,
providing an aqueous suspension comprising the PHA and an expanding agent which decomposes at the operating temperature of the atomization chamber, with formation of at least one gaseous compound, and
injecting the aqueous suspension into the atomization chamber provided at the operating temperature, so as to cause instantaneous evaporation of the aqueous suspension and decomposition of the expanding agent, with formation of the porous PHA particles.
2. The process according to claim 1 , wherein the expanding agent is a carbonate or bicarbonate of an alkali or alkaline earth metal or of ammonium.
3. The process according to claim 2 , wherein the expanding agent is selected from: ammonium bicarbonate, ammonium carbonate, sodium bicarbonate, calcium carbonate, magnesium carbonate, or mixtures thereof.
4. The process according to claim 1 , wherein the operating temperature of the atomization chamber is comprised between 100° C. and 200° C.
5. The process according to claim 1 , wherein the PHA is present in the aqueous suspension at a concentration comprised between 1% w/v and 50% w/v, the % being expressed by weight with respect to the total volume of the suspension.
6. The process according to claim 1 , wherein the expanding agent is present in the aqueous suspension at a concentration comprised between 0.5% w/v and 30% w/v, the % being expressed by weight with respect to the total volume of the suspension.