A co-rotating twin screw processor for preparing dry granules including an input zone having one or more powder feeders for feeding an input material into the processor, a steam feeder configured to introduce steam as a granulation activating agent in to the processor, a granulation zone for granulating the input material in the presence of steam to form granules, a controller configured to control operation and feed rate of at least one of the powder feeder or the steam feeder such that 2.5 to 5 percent w/w of the steam with respect to the input material is available for granulation, and a discharge zone haring a non-extruding opening for collecting dry granules.

A medicine grinder has a grinding assembly having a ring burr and a frustoconical burr being mutually rotatable relative to each other. The ring burr is tubular. The frustoconical burr is disposed within the ring burr and has multiple rough grinding edges, multiple recesses, and a non-grinding portion. The multiple rough grinding edges surround a center of the frustoconical burr. Each one of the grinding edges spirally extends about the center of the frustoconical burr. The multiple recesses are divided by the multiple rough grinding edges. One of the multiple recesses has a capacity being larger than a capacity of each one of the other recesses to define a non-grinding portion. Therefore, multiple receiving spaces are formed between the frustoconical burr and the ring burr.

The present disclosure relates to a non-invasive, non-gravitationally dependent, pressurized method for the rapid selective extraction, volume expansion, and reclamation of medication and medication metabolites (including but not limited to naturally occurring or engineered hormones, chemicals, antibodies, enzymes, lipids, proteins or pharmaceutical products) from urine. The disclosure further relates to methods for reclamation of medication from urine in a pressurized system and methods of using the medication reclaimed from that urine.

The present disclosure relates to a non-invasive, non-gravitationally dependent, pressurized method for the rapid selective extraction, volume expansion, and reclamation of medication and medication metabolites (including but not limited to naturally occurring or engineered hormones, chemicals, antibodies, enzymes, lipids, proteins or pharmaceutical products) from urine. The disclosure further relates to methods for reclamation of medication from urine in a pressurized system and methods of using the medication reclaimed from that urine.

A method is provided for preparing spray dried powder containing vancomycin hydrochloride. The method comprises providing a vancomycin hydrochloride solution with a chromatographic purity of at least 95%, adding an excipient to the vancomycin hydrochloride solution to form a mixture solution of the vancomycin hydrochloride solution and the excipient, concentrating the mixed solution of the vancomycin hydrochloride solution and the excipient to form a 20% to 30% vancomycin concentrate, filtering the vancomycin concentrate to form a final filtrate and spray crying the final filtrate to form a spray dried vancomycin hydrochloride powder with EP impurity B level of not more than 1.5%.

A method is provided for preparing spray dried powder containing vancomycin hydrochloride. The method comprises providing a vancomycin hydrochloride solution with a chromatographic purity of at least 95%, adding an excipient to the vancomycin hydrochloride solution to form a mixture solution of the vancomycin hydrochloride solution and the excipient, concentrating the mixed solution of the vancomycin hydrochloride solution and the excipient to form a 20% to 30% vancomycin concentrate, filtering the vancomycin concentrate to form a final filtrate and spray crying the final filtrate to form a spray dried vancomycin hydrochloride powder with EP impurity B level of not more than 1.5%.

The present invention provides a new process for stabilizing the particle size of micronized glycopyrronium salt (such as glycopyrronium bromide) which yields a micronized product exhibiting improved chemical and polymorphic stability even after prolonged storage. The invention also relates to compositions comprising said stabilized glycopyrronium salt (such as glycopyrronium bromide) and to dry powder inhaler devices and capsules or blisters comprising the stabilized glycopyrronium salt (such as glycopyrronium bromide). The glycopyrronium salt (such as glycopyrronium bromide) or compositions of the invention may be used as a medicament, for instance in the treatment of asthma, chronic obstructive pulmonary disease or cystic fibrosis or related diseases.

The present invention provides a new process for stabilizing the particle size of micronized glycopyrronium salt (such as glycopyrronium bromide) which yields a micronized product exhibiting improved chemical and polymorphic stability even after prolonged storage. The invention also relates to compositions comprising said stabilized glycopyrronium salt (such as glycopyrronium bromide) and to dry powder inhaler devices and capsules or blisters comprising the stabilized glycopyrronium salt (such as glycopyrronium bromide). The glycopyrronium salt (such as glycopyrronium bromide) or compositions of the invention may be used as a medicament, for instance in the treatment of asthma, chronic obstructive pulmonary disease or cystic fibrosis or related diseases.

Compositions are provided that include having at least 95% by weight of a taxane, or a pharmaceutically acceptable salt thereof, where the particles have a mean bulk density between about 0.050 g/cm.sup.3 and about 0.15 g/cm.sup.3, and/or a specific surface area (SSA) of at least 18 m.sup.2/g, 20 m.sup.2/g, 25 m.sup.2/g, 30 m.sup.2/g, 32 m.sup.2/g, 34 m.sup.2/g, or 35 m.sup.2/g. Methods for making and using such compositions are also provided.

Compositions are provided that include having at least 95% by weight of a taxane, or a pharmaceutically acceptable salt thereof, where the particles have a mean bulk density between about 0.050 g/cm.sup.3 and about 0.15 g/cm.sup.3, and/or a specific surface area (SSA) of at least 18 m.sup.2/g, 20 m.sup.2/g, 25 m.sup.2/g, 30 m.sup.2/g, 32 m.sup.2/g, 34 m.sup.2/g, or 35 m.sup.2/g. Methods for making and using such compositions are also provided.