process for the manufacture of wax plant emulsifiante designed as a feedstock for manufacturing liquid emulsion cosmetic and pharmaceutical and creams and device for obtaining it.

摘要

the present invention is characterized by a process for the manufacture of an emulsifying and emulsifying wax plant particularly characterized by the fact that one or more vegetable oils rich in essential fatty acids, and soluble fibre amphiphiles, in this case in the present invention, or the inventor has chosen the huilignaneu00ae.that is an oil extracted from the seeds of flax or sesame seeds or any other similar plant, activated by a catalyst, saponifie, as a result of the reaction, a vegetable wax such as beeswax, stearic acid, or any other similar.after a pause of stabilization, the melting temperature of the mass and the amount of fats and vegetable oils are incorporated in a rapid mixing. the mass is provided, and under pressure to a fusion packing unit.according to the present invention, it can achieve excellent emulsifying wax emulsified material and, in addition, and in contrast to the emulsifying), plant and it is this very good biocompatibility and complete biodegradability. it is intended as a base material for the manufacture of emulsions and creams, cosmetics and pharmaceuticals.the method and the device of manufacturing is that the lid (2) is opened, and the rotary shaft is mounted as it is shown in figure 1: the stearic acid plant is placed in the tank (1).under the effect of the heat generated by the water within the tank and mary (13) through which electrical heating elements (20) are controlled by a thermostat system (40), (41) will merge under gentle agitation of the rotary shaft (26).the level of hot water in the tank (13) is controlled by the level detector (22), and restored automatically after the evaporation of water from the system (23) which is controlled by (42). after the merger of the stearic acid, huilignaneu00ae, or any other similar oil is incorporated in small doses in the body under gentle agitation.after a short reaction time (about 5 minutes), the speed of rotation of the central shaft (26) is increased to a maximum at a time of rapid mixing for about three minutes, after which, in the absence of any reaction, molten fats and vegetable oils are included as rapid mixing in a reaction time of 5 minutes.the mixing system (29) is stopped (off).when the mass thus obtained is no trace of reaction and it is homogeneous and transparent, the rotary shaft (26) is removed and the lid (2) is sealed by the n2 fixing (5) on the gasket (9), the pressure of air conditioning is introduced through the pipe (4) is controlled by the pressure gauge (8).the air conditioning is performed in the compressed air storage tank (45). the air generated by a compressor dry air (44) is filtered through the air filter (46), and circulates through the tubing (50) which is heated by the element (47) which is fed by the connector (50). the heat insulation material (48) ensures the tightness of the storage tank (45).the hot air thus produced is carried by the driving shaft (51) to the station (1).the heating element (10) that is energized by the connection (11) when the temperature of the drive (7), which carries the product to the packaging unit, is the temperature of the tank, the valve core (1). (6) is then applied, which will start the pressure transfer.the mass of the tank with central unit (1) for packaging or casting