C07C231/24

System for crystalizing chemical compounds and methodologies for utilizing the same

A system including a fluid receiver defined by a crystallization chamber, three or more fluid input conduits, wherein each fluid input conduit is configured to direct a fluid into the crystallization chamber such that the fluids from the fluid input conduits converge on a single spatial coordinate (X—Y—Z) within the crystallization chamber, and a fluid outlet body portion. A process for crystallization of the chemical compound is also disclosed. Polymorphs of paracetamol, carbamazapine, ketoprofen, atorvastatin, and itraconazole also are disclosed.

COOLING LOOP WITH A SUPERCRITICAL FLUID SYSTEM USING COMPRESSED REFRIGERANT FLUID FLOW WITH A POSITIVE JOULE THOMSON COEFFICIENT

Provided is a chiller and system that may be utilized in a supercritical fluid chromatography method, wherein a non-polar solvent may replace a portion or all of a polar solvent for the purpose of separating or extracting desired sample molecules from a combined sample/solvent stream. The system may reduce the amount of polar solvent necessary for chromatographic separation and/or extraction of desired samples. The system may incorporate a supercritical fluid chiller, a supercritical fluid pressure-equalizing vessel and a supercritical fluid cyclonic separator. The supercritical fluid chiller allows for efficient and consistent pumping of liquid-phase gases employing off-the-shelf HPLC pumps. The pressure equalizing vessel allows the use of off-the-shelf HPLC column cartridges. The system may further incorporate the use of one or more disposable cartridges containing silica gel or other suitable medium. The system may also utilize an open loop cooling circuit using fluids with a positive Joule-Thomson coefficient.

COOLING LOOP WITH A SUPERCRITICAL FLUID SYSTEM USING COMPRESSED REFRIGERANT FLUID FLOW WITH A POSITIVE JOULE THOMSON COEFFICIENT

Provided is a chiller and system that may be utilized in a supercritical fluid chromatography method, wherein a non-polar solvent may replace a portion or all of a polar solvent for the purpose of separating or extracting desired sample molecules from a combined sample/solvent stream. The system may reduce the amount of polar solvent necessary for chromatographic separation and/or extraction of desired samples. The system may incorporate a supercritical fluid chiller, a supercritical fluid pressure-equalizing vessel and a supercritical fluid cyclonic separator. The supercritical fluid chiller allows for efficient and consistent pumping of liquid-phase gases employing off-the-shelf HPLC pumps. The pressure equalizing vessel allows the use of off-the-shelf HPLC column cartridges. The system may further incorporate the use of one or more disposable cartridges containing silica gel or other suitable medium. The system may also utilize an open loop cooling circuit using fluids with a positive Joule-Thomson coefficient.

Process for preparing lacosamide and related compounds

There is provided a process for the preparation of Lacosamide in a particular polymorphic form, which process involves the isolation of a salt of formula I: according to the methods defined in the application. ##STR00001##

Process for preparing lacosamide and related compounds

There is provided a process for the preparation of Lacosamide in a particular polymorphic form, which process involves the isolation of a salt of formula I: according to the methods defined in the application. ##STR00001##

4-(p-trifluoromethylbenzyl)-3-fluoro-1,2,4-triphenylamine derivative and pharmaceutical composition and applications thereof

A 4-(p-trifluoromethylbenzyl)-3-fluoro-1,2,4-triphenylamine derivative, a pharmaceutical composition and applications thereof are disclosed. The general chemical formula of the derivative is shown in formula I, where, R is a C.sub.1-C.sub.6 alkyl group, a cycloalkyl group, a heteroatom-containing cycloalkyl group, an aryl group or a heteroatom-containing aryl group, the heteroatom is selected from N or O, and the n is 0, 1, 2 or 3. The pharmaceutical composition contains any one of the above-mentioned 4-(p-trifluoromethylbenzyl)-3-fluoro-1,2,4-triphenylamine derivatives as an active ingredient, and one or more pharmaceutically acceptable carriers. The derivative and the pharmaceutical composition activate KCNQ channel currents. Thus, the derivative can be applied to prepare a KCNQ potassium channel opener, and can be used as the active ingredients of an antiepileptic pharmaceutical preparation, an antianxiety pharmaceutical preparation and a neuropathic pain-relieving pharmaceutical preparation.

4-(p-trifluoromethylbenzyl)-3-fluoro-1,2,4-triphenylamine derivative and pharmaceutical composition and applications thereof

A 4-(p-trifluoromethylbenzyl)-3-fluoro-1,2,4-triphenylamine derivative, a pharmaceutical composition and applications thereof are disclosed. The general chemical formula of the derivative is shown in formula I, where, R is a C.sub.1-C.sub.6 alkyl group, a cycloalkyl group, a heteroatom-containing cycloalkyl group, an aryl group or a heteroatom-containing aryl group, the heteroatom is selected from N or O, and the n is 0, 1, 2 or 3. The pharmaceutical composition contains any one of the above-mentioned 4-(p-trifluoromethylbenzyl)-3-fluoro-1,2,4-triphenylamine derivatives as an active ingredient, and one or more pharmaceutically acceptable carriers. The derivative and the pharmaceutical composition activate KCNQ channel currents. Thus, the derivative can be applied to prepare a KCNQ potassium channel opener, and can be used as the active ingredients of an antiepileptic pharmaceutical preparation, an antianxiety pharmaceutical preparation and a neuropathic pain-relieving pharmaceutical preparation.

ALTERNATIVE PROCESS FOR THE PURIFICATION OF AN INTERMEDIATE IN THE SYNTHESIS OF NON-IONIC X-RAY CONTRAST AGENTS

Alternative continuous downstream processes for the production of 5-acetamido-N,N′-bis(2,3-dihydroxypropyl)-2,4,6-triiodoisophthalamide (“Compound A”) are described. Compound A is a key intermediate in the production of iodixanol and iohexol, which are two of the biggest commercially available non-ionic x-ray contrast media agents.

ALTERNATIVE PROCESS FOR THE PURIFICATION OF AN INTERMEDIATE IN THE SYNTHESIS OF NON-IONIC X-RAY CONTRAST AGENTS

Alternative continuous downstream processes for the production of 5-acetamido-N,N′-bis(2,3-dihydroxypropyl)-2,4,6-triiodoisophthalamide (“Compound A”) are described. Compound A is a key intermediate in the production of iodixanol and iohexol, which are two of the biggest commercially available non-ionic x-ray contrast media agents.

ALTERNATIVE PROCESS FOR THE PURIFICATION OF AN INTERMEDIATE IN THE SYNTHESIS OF NON-IONIC X-RAY CONTRAST AGENTS

Alternative continuous downstream processes for the production of 5-acetamido-N,N′-bis(2,3-dihydroxypropyl)-2,4,6-triiodoisophthalamide (“Compound A”) are described. Compound A is a key intermediate in the production of iodixanol and iohexol, which are two of the biggest commercially available non-ionic x-ray contrast media agents.