Abstract: A method and an apparatus for processing and recovering bitumen (42) and aggregate (41) from asphalt (40), in which: a) the asphalt (40) is mechanically comminuted; b) the comminuted asphalt is introduced into an evacuated or evacuatable processing chamber (1); c) the processing chamber (1) is evacuated by adjusting the pressure in the processing chamber (1) to a pressure lower than ambient pressure, preferably 200 mbar or lower; d) the processing chamber (1) is then charged at least once with a liquid organic solvent; e) the liquid organic solvent is then extracted from the processing chamber (1); and then f1) the organic solvent is fed into the evacuated processing chamber (1) in the vapor phase at the reduced pressure, at a temperature at or above the flash point of the organic solvent; and/or f2) liquid organic solvent is fed into the treatment chamber (1).

Abstract: A method and an apparatus for processing and recovering bitumen (42) and aggregate (41) from asphalt (40), in which: a) the asphalt (40) is mechanically comminuted; b) the comminuted asphalt is introduced into an evacuated or evacuatable processing chamber (1); c) the processing chamber (1) is evacuated by adjusting the pressure in the processing chamber (1) to a pressure lower than ambient pressure, preferably 200 mbar or lower; d) the processing chamber (1) is then charged at least once with a liquid organic solvent; e) the liquid organic solvent is then extracted from the processing chamber (1); and then f1) the organic solvent is fed into the evacuated processing chamber (1) in the vapor phase at the reduced pressure, at a temperature at or above the flash point of the organic solvent; and/or f2) liquid organic solvent is fed into the treatment chamber (1).

Abstract: The present invention relates to a method for the reliable and reproducible preparation of 4-[17?-methoxy-17?-methoxymethyl-3-oxoestra-4,9-dien-11?-yl]benzaldehyde (E)-oxime (asoprisnil) on the pilot and manufacturing scale. Asoprisnil, which is prepared by this method, is distinguished by a very good physical stability and is therefore particularly suitable for the manufacture of solid pharmaceutical forms (tablets, coated tablets, etc.).

Abstract: The present invention relates to a method for the reliable and reproducible preparation of 4-[17?-methoxy-17?-methoxymethyl-3-oxoestra-4,9-dien-11?-yl]benzaldehyde (E)-oxime (asoprisnil) on the pilot and manufacturing scale. Asoprisnil, which is prepared by this method, is distinguished by a very good physical stability and is therefore particularly suitable for the manufacture of solid pharmaceutical forms (tablets, coated tablets, etc.).

Abstract: The process for making crystals of a 11 ?-benzaldoxim-estra-4,9-diene derivative having an average particle size of from 3 ?m to 25 ?m and a maximum particle size of 100 ?m, includes subjecting a supersaturated solution containing a special 11?-benzaldoxim-estra-4,9-diene derivative of formula (I) to a wet milling by a wet milling apparatus while crystallizing, In order to obtain a primary particle suspension. Crystals obtained according to this process and pharmaceutical preparations containing them are also described and are part of the invention.

Abstract: The process for making steroid crystals having a predetermined average particle size of from 1 ?m to 25 ?m and a maximum particle size that does not exceed a predetermined maximum value of 100 ?m, includes subjecting a supersaturated solution containing a steroid to a wet milling by wet milling apparatus while crystallizing, in order to obtain a primary particle suspension. Crystals obtained according to this process and pharmaceutical preparations containing them are also described.

Abstract: The transdermal system includes a sex hormone-containing adhesive matrix, which contains inclusions of a sex hormone in a hydrophilic non-crosslinked polymer in dissolved or dispersed form. The inclusions have a concentration of 20 to 90 percent by weight of the sex hormone, which is more than 50 percent by weight amorphous. The hydrophilic non-crosslinked polymer can be polyvinylpyrrolidone, methylcellulose, ethylcellulose or hydroxyethylcellulose. The adhesive matrix can be a polyisobutylene, ethylene-vinyl-acetate copolymer or a polystyrene-butadiene block copolymer.

Abstract: The process for making crystals of a 11&bgr;-benzaldoxim-estra-4,9-diene derivative having a predetermined average particle size in a predetermined size range and a maximum particle size that does not exceed a predetermined maximum value, includes subjecting a supersaturated solution containing a special 11&bgr;-benzaldoxim-estra-4,9-diene derivative of formula (I) to a wet milling by a wet milling apparatus while crystallizing, in order to obtain a primary particle suspension. Crystals obtained according to this process and pharmaceutical preparations containing them are also described.

Abstract: The process for making steroid crystals having a predetermined average particle size in a predetermined size range and a maximum particle size that does not exceed a predetermined maximum value, includes subjecting a supersaturated solution containing a steroid to a wet milling by a wet milling apparatus while crystallizing, in order to obtain a primary particle suspension. Crystals obtained according to this process and pharmaceutical preparations containing them are also described.

Abstract: The process for making crystals of a medicinally effective ingredient having a predetermined average particle size in a predetermined size range and a maximum particle size that does not exceed a predetermined maximum value, includes subjecting a supersaturated solution containing the medicinally effective ingredient to a wet milling by a wet milling apparatus while crystallizing, in order to obtain a primary particle suspension. Crystals obtained according to this process and pharmaceutical preparations containing them are also described.

Abstract: The process for making crystals of an adjuvant substance for pharmaceutical compositions, which have a predetermined average particle size in a predetermined size range and a maximum particle size that does not exceed a predetermined maximum value, includes subjecting a supersaturated solution containing the adjuvant substance to a wet milling by a wet milling apparatus while crystallizing, in order to obtain a primary particle suspension. Crystals obtained according to this process and pharmaceutical preparations containing them are also described.

Abstract: A homogeneous steroid-containing preformulation for production of solid and semi-solid pharmaceutical preparations containing a uniform constant dosage of at least one steroid in a range from 0.001 to 1 percent by weight is described. This steroid-containing preformulation contains of from 0.001 to 50 percent by weight of the at least one steroid. The homogeneous steroid-containing preformulation is made by a method including dissolving the at least one steroid in a solvent to form a dispersant; dispersing an adjuvant consisting of adjuvant particles in the dispersant in a mass ratio of the adjuvant to the at least one steroid of 1:1 to 1000:1 to form a suspension; and creating a spray-mist of the suspension so as to evaporate and remove the solvent from the suspension and thus to form a dried particulate which includes steroid-containing particles. The droplets in the spray mist have a droplet diameter greater than a mean diameter of the adjuvant particles.

Abstract: A homogeneous steroid-containing preformulation for production of solid and semi-solid pharmaceutical preparations containing a uniform constant dosage of at least one steroid in a range from 0.001 to 1 percent by weight is described. This steroid-containing preformulation contains of from 0.001 to 50 percent by weight of the at least one steroid. The homogeneous steroid-containing preformulation is made by a method including dissolving the at least one steroid in a solvent to form a dispersant; dispersing an adjuvant consisting of adjuvant particles in the dispersant in a mass ratio of the adjuvant to the at least one steroid of 1:1 to 1000:1 to form a suspension; and creating a spray-mist of the suspension so as to evaporate and remove the solvent from the suspension and thus to form a dried particulate which includes steroid-containing particles. The droplets in the spray mist have a droplet diameter greater than a mean diameter of the adjuvant particles.