Disclosed herein is a method for producing crystalline cannabinoid particles in continuous mode. The method comprises preparing a cannabinoid-rich solution that comprises a first cannabinoid, and inducing the cannabinoid-rich solution to a supersaturated state in which the first cannabinoid has a supersaturated concentration that is greater than a corresponding saturation concentration of the first cannabinoid. The method further comprises flowing the cannabinoid-rich solution through a tubular reactor in a continuous manner under turbulent flow conditions to form a plurality of crystalline cannabinoid particles and a cannabinoid-depleted solution within the tubular reactor, and separating crystalline cannabinoid particles from the plurality of crystalline cannabinoid particles and the cannabinoid-depleted solution. The turbulent flow conditions are defined by a Reynold number that is greater than a critical Reynolds number for the cannabinoid-rich solution and the tubular reactor.

The disclosure provides particles of at least 95% by weight of sorafenib, or a pharmaceutically acceptable salt thereof, wherein the particles have a specific surface area (SSA) of at least 2 m.sup.2/g and have a mean particle size by volume distribution of between about 0.7 μm and about 8 μm, methods for their use, and methods for making such particles.

Described herein are synthetic progestogens, such as 6β,7β:15β,16β-Dimethylene-3-oxo-17α-pregn-4-ene-21,17-carbolactone, as well as pharmaceutical compositions comprising the same. Also described are methods of use.

The present invention relates to a process for the preparation of spherical agglomerates of timapiprant; the invention also relates to spherical agglomerates of timapiprant obtained by the above process.

Described herein are synthetic progestogens, such as 6β,7β:15β,16β-Dimethylene-3-oxo-17α-pregn-4-ene-21,17-carbolactone, as well as pharmaceutical compositions comprising the same. Also described are methods of use.

Described herein are synthetic progestogens, such as 6β,7β:15β,16β-Dimethylene-3-oxo-17α-pregn-4-ene-21,17-carbolactone, as well as pharmaceutical compositions comprising the same. Also described are methods of use.

Described herein are synthetic progestogens, such as 6β,7β:15β,16β-Dimethylene-3-oxo-17α-pregn-4-ene-21,17-carbolactone, as well as pharmaceutical compositions comprising the same. Also described are methods of use.

A process for making nanoparticles of biocompatible materials is described, wherein an aqueous reaction mixture comprising cerous ion, ethylenediaminedisuccinic acid, an oxidant, water, and optionally citric acid, is provided along with temperature conditions to directly form within the reaction mixture, a stable dispersion of cerium oxide nanoparticles. Biocompatible nanoparticles comprised of cerium oxide, ethylenediaminedisuccinic acid, and optionally citric acid, are described. An increase in catalase-like enzyme activity is demonstrated by cerium oxide nanoparticles prepared with citric acid and ethylenediaminedisuccinic acid.

The present disclosure provides an apparatus and methods of use for isolating particles. An example apparatus includes (a) a vessel defining a pressurizable chamber, wherein the vessel includes a distal end and a proximal end, (b) an inlet of the pressurizable chamber at the proximal end of the vessel, (c) a nozzle positioned within the pressurizable chamber, wherein the nozzle includes an inlet tube in fluid communication with the inlet of the pressurizable chamber, wherein the nozzle includes an outlet aperture, wherein the nozzle is adjustable to alter a distance between the proximal end of the vessel and the outlet aperture of the nozzle, and wherein the nozzle is adjustable to alter an angle between a longitudinal axis of the vessel and a longitudinal axis of the nozzle, and (d) an outlet of the pressurizable chamber at the distal end of the vessel.

The present invention relates to a process for spray drying of a feed solution comprising the GLP-1 peptide semaglutide wherein the ratio of atomising gas flow (kg/h) to feed solution flow (kg/h) is 1.0-1.7.