C07C255/03

Processes for stabilizing antimony catalysts

The present disclosure relates to a process for stabilizing an antimony ammoxidation catalyst in an ammoxidation process. The process may comprise providing an antimony ammoxidation catalyst to a reactor; reacting propylene with ammonia and oxygen in the fluidized bed reactor in the presence of the antimony ammoxidation catalyst to form a crude acrylonitrile product; and adding an effective amount of an antimony-containing compound to the antimony ammoxidation catalyst to maintain catalyst conversion and selectivity; wherein the antimony-containing compound has a melting point less than 375° C. The present disclosure also relates to catalyst compositions and additional processes using the antimony ammoxidation catalyst stabilized by an antimony-containing compound.

Crystalline phases of 5,6-dichloro-2-(isopropylamino)-(1-beta-L-ribofuranosyl)-1H-benzimidazole

The invention relates to novel crystalline phases of 5,6-dichloro-2-(isopropylamino)-1-(β-L-ribofuranosyl)-1H-benzimidazole (Maribavir), pharmaceutical compositions thereof and their use in medical therapy.

Crystalline phases of 5,6-dichloro-2-(isopropylamino)-(1-beta-L-ribofuranosyl)-1H-benzimidazole

The invention relates to novel crystalline phases of 5,6-dichloro-2-(isopropylamino)-1-(β-L-ribofuranosyl)-1H-benzimidazole (Maribavir), pharmaceutical compositions thereof and their use in medical therapy.

Regulators for controlling linear and pseudo-ring expansion polymerization of vinyl monomers

New regulator compounds for a novel polymerization process for vinyl monomers, which yields polymers with improved control over composition and nearly full to full conservation of architectural integrity up to high conversion. The regulator compounds are defined by according to anyone of the Formulas 1A, 1B, 1C, 1D, 1E, 1F, 1G, 1H and 1I: ##STR00001## wherein R.sup.1 stands for an optionally substituted secondary or tertiary alkyl or secondary or tertiary aralkyl; Z.sup.1 stands for CN or a carboxylic acid ester of formula C(O)OR.sup.21; Z.sup.2 may be chosen from the group of CN, carboxylic acid, salts of carboxylic acids, carboxylic acid ester, carboxylic acid amides, (hetero)aryl, alkenyl and halogen; R.sup.2, R.sup.3, R.sup.4 and R.sup.5 are each independently chosen from the group of H, alkyl, aralkyl, (hetero)aryl, CN and carboxylic acid ester of formula C(O)OR.sup.22; R.sup.7 stands for a primary alkyl or primary aralkyl, CN or hydrogen; Y stands for a bridging group and n is 2, 3, 4, 5 or 6; in case R.sup.1 stands for tertiary alkyl or tertiary aralkyl, R.sup.6 stands for a primary alkyl or primary aralkyl, CN or a carboxylic acid ester of formula C(O)OR.sup.26; in case R.sup.1 stands for a secondary alkyl or secondary aralkyl, R.sup.6 stands for a primary or secondary alkyl or primary or secondary aralkyl, CN, a carboxylic acid ester of formula C(O)OR.sup.26 or a phosphonic acid ester of formula P(O)(OR.sup.27).sub.2, a (hetero)aryl or an alkenyl; R.sup.21, R.sup.22, R.sup.26 and R.sup.27 each independently stand for alkyl or aralkyl having from 1-30 carbon atoms, optionally containing heteroatoms.

Regulators for controlling linear and pseudo-ring expansion polymerization of vinyl monomers

New regulator compounds for a novel polymerization process for vinyl monomers, which yields polymers with improved control over composition and nearly full to full conservation of architectural integrity up to high conversion. The regulator compounds are defined by according to anyone of the Formulas 1A, 1B, 1C, 1D, 1E, 1F, 1G, 1H and 1I: ##STR00001## wherein R.sup.1 stands for an optionally substituted secondary or tertiary alkyl or secondary or tertiary aralkyl; Z.sup.1 stands for CN or a carboxylic acid ester of formula C(O)OR.sup.21; Z.sup.2 may be chosen from the group of CN, carboxylic acid, salts of carboxylic acids, carboxylic acid ester, carboxylic acid amides, (hetero)aryl, alkenyl and halogen; R.sup.2, R.sup.3, R.sup.4 and R.sup.5 are each independently chosen from the group of H, alkyl, aralkyl, (hetero)aryl, CN and carboxylic acid ester of formula C(O)OR.sup.22; R.sup.7 stands for a primary alkyl or primary aralkyl, CN or hydrogen; Y stands for a bridging group and n is 2, 3, 4, 5 or 6; in case R.sup.1 stands for tertiary alkyl or tertiary aralkyl, R.sup.6 stands for a primary alkyl or primary aralkyl, CN or a carboxylic acid ester of formula C(O)OR.sup.26; in case R.sup.1 stands for a secondary alkyl or secondary aralkyl, R.sup.6 stands for a primary or secondary alkyl or primary or secondary aralkyl, CN, a carboxylic acid ester of formula C(O)OR.sup.26 or a phosphonic acid ester of formula P(O)(OR.sup.27).sub.2, a (hetero)aryl or an alkenyl; R.sup.21, R.sup.22, R.sup.26 and R.sup.27 each independently stand for alkyl or aralkyl having from 1-30 carbon atoms, optionally containing heteroatoms.

Process for Preparing Fluorobenzene by Direct Fluorination

The invention relates to a use of a fluorination gas, wherein the elemental fluorine (F.sub.2) is present in a high concentration, for example, in a concentration of elemental fluorine (F.sub.2), especially of equal to much higher than 15% or even 20% by volume (i.e., at least 15% or even 20% by volume), and to a process for the manufacture of a fluorinated benzene by direct fluorination employing a fluorination gas, wherein the elemental fluorine (F.sub.2) is present in a high concentration. The process of the invention is directed to the manufacture of a fluorinated benzene by direct fluorination. Especially the invention is of interest in the preparation of fluorinated benzene, final products and as well intermediates, for usage in agro-, pharma-, electronics-, catalyst, solvent and other functional chemical applications. The fluorination process of the invention may be performed batch-wise or in a continuous manner. If the process of the invention is performed batch-wise, a column (tower) reactor may be used. If the process of the invention is continuous a microreactor may be used. The invention is characterized in that the starting compound is benzene, and the fluorinated compound produced is a fluorinated benzene, preferably monofluorobenzene.

Process for Preparing Fluorobenzene by Direct Fluorination

The invention relates to a use of a fluorination gas, wherein the elemental fluorine (F.sub.2) is present in a high concentration, for example, in a concentration of elemental fluorine (F.sub.2), especially of equal to much higher than 15% or even 20% by volume (i.e., at least 15% or even 20% by volume), and to a process for the manufacture of a fluorinated benzene by direct fluorination employing a fluorination gas, wherein the elemental fluorine (F.sub.2) is present in a high concentration. The process of the invention is directed to the manufacture of a fluorinated benzene by direct fluorination. Especially the invention is of interest in the preparation of fluorinated benzene, final products and as well intermediates, for usage in agro-, pharma-, electronics-, catalyst, solvent and other functional chemical applications. The fluorination process of the invention may be performed batch-wise or in a continuous manner. If the process of the invention is performed batch-wise, a column (tower) reactor may be used. If the process of the invention is continuous a microreactor may be used. The invention is characterized in that the starting compound is benzene, and the fluorinated compound produced is a fluorinated benzene, preferably monofluorobenzene.

METHOD FOR PRODUCING NITRILE

The present invention provides a method of producing a nitrile from a primary amide, characterized in that the primary amide is subjected to a dehydration reaction in a supercritical fluid in the presence of an acid catalyst. The present invention achieves the object of reducing the corrosion of a reactor and the thermal decomposition of raw materials, as well as provides the effect of improving the reaction rate and nitrile selectivity.

METHOD FOR PRODUCING NITRILE

The present invention provides a method of producing a nitrile from a primary amide, characterized in that the primary amide is subjected to a dehydration reaction in a supercritical fluid in the presence of an acid catalyst. The present invention achieves the object of reducing the corrosion of a reactor and the thermal decomposition of raw materials, as well as provides the effect of improving the reaction rate and nitrile selectivity.

SUBSTITUTED (1,2,3,4-TETRAHYDROCYCLOPENTA[b]INDOL-3-YL)ACETIC ACID DERIVATIVES USEFUL IN THE TREATMENT OF AUTOIMMUNE AND INFLAMMATORY DISORDERS

The present invention relates to certain substituted 1,2,3,4-tetrahydrocyclopenta[b]indol-3-yl)acetic acid derivatives of Formula (Ia) and pharmaceutically acceptable salts thereof, which exhibit useful pharmacological properties, for example, as agonists of the S1P1 receptor.

##STR00001##

Also provided by the present invention are pharmaceutical compositions containing compounds of the invention, and methods of using the compounds and compositions of the invention in the treatment of S1P1 receptor-associated disorders, for example, psoriasis, rheumatoid arthritis, Crohn's disease, transplant rejection, multiple sclerosis, systemic lupus erythematosus, ulcerative colitis, type I diabetes, acne, microbial infections or diseases and viral infections or diseases.