Carbon-carbon bond forming reactions are the cornerstone of organic chemistry. A new class of ligands was developed for transition metal catalyzed cross-coupling reactions. These phosphine-urea ligands incorporate a urea subunit into the backbone of the ligand, which is designed to bind to the organometallic coupling partner and simultaneously facilitate and direct transmetalation of the nucleophile. Synthetic routes were designed and executed to synthesize phosphine-urea ligands. These ligands catalyze a wide variety of cross-coupling reactions including Suzuki, Negishi, and Buchwald-Hartwig cross-couplings. Aryl-aryl, alkyl-aryl, and alkyl-alkyl CC cross-couplings are performed successfully with these ligands. In addition, specific chiral phosphine-urea ligands catalyze Negishi cross-couplings enantioselectively from a racemic alkylzinc nucleophile.

A hydrosilylation iron catalyst prepared from a two-electron ligand (L) and a mononuclear, binuclear, or trinuclear complex of iron indicated by formula (1), Fe having bonds with carbon atoms included in X and the total number of Fe-carbon bonds being 2-10. As a result of using iron, the hydrosilylation iron catalyst is advantageous from a cost perspective as well as being easily synthesized. Hydrosilylation reactions can be promoted under mild conditions by using this catalyst.
Fe(X).sub.a(1)
(in the formula, each X independently indicates a C2-30 ligand that may include an unsaturated group excluding carbonyl groups (CO groups) and cyclopentadienyl groups, however at least one X includes an unsaturated group, a indicates an integer of 2-4 per Fe atom.)

A 4,4-divinylazoarylene-bridged diruthenium complex bearing two Ru(CO)(2-mercaptopyridine)(P.sup.iPr.sub.3).sub.2 moieties, its synthesis, and its use as a catalyst.

Subject of the invention is a process for producing a biofuel from fatty acid methyl esters (FAMEs) obtained by transesterification of vegetable oils, comprising the steps of: (a) ethenolysis of the fatty acid methyl esters in the presence of ethylene and an ethenolysis catalyst, and (b) isomerizing metathesis in the presence of an isomerization catalyst and a metathesis catalyst. The invention also relates to biofuels obtainable by the inventive process and to uses of ethylene for adjusting and optimizing biofuels.

A process can prepare an isocyanurate compound by hydrosilylation. The compound is a tris[3-(trialkoxysily)propyl] isocyanurate, a tris[3-(alkyldialkoxysilyl)propyl] isocyanurate, and/or a tris[3-(dialkylalkoxysilyl)propyl] isocyanurate. The process includes (A) preparing a mixture of at least one carboxylic acid, a platinum catalyst, and 1,3,5-triallyl-1,3,5-triazine-2,4,6(1H,3H,5H)-trione; (B) heating the mixture to a temperature in the range of 40 to 140 C.; (C) adding at least one H-silane among a hydrotrialkoxysilane, a hydroalkyldialkoxysilane, and a hydrodialkylalkoxysilane to the mixture; (D) adding at least one alcohol to the mixture prepared in step (C); and (E) isolating the isocyanurate compound.

The present invention provides a complex of formula (1),

##STR00001##

wherein, M is palladium or nickel, R.sub.1 and R.sub.2 are independently organic groups having 1-20 carbon atoms, or R.sub.1 and R.sub.2 are linked to form a ring structure with the phosphorus atom, R.sub.3 is selected from the group consisting of substituted and unsubstituted aryl, substituted and unsubstituted heteroaryl, and substituted and unsubstituted metallocenyl, R.sub.4 is an organic group having 1-20 carbon atoms, n is 0, 1, 2, 3, 4 or 5, and X is an anionic ligand. The invention also provides a process for the preparation of the complex, and its use in carbon-carbon or carbon-nitrogen coupling reactions.

Object of the present invention is an improved process for the preparation of (3R,4R)-1-benzyl-4-methylpiperidin-3-amine by means of chiral Rhodium catalysts.

A complex of formula (1), ##STR00001##
wherein, M is palladium or nickel, R.sub.1 and R.sub.2 are independently organic groups having 1-20 carbon atoms, or R.sub.1 and R.sub.2 are linked to form a ring structure with the phosphorus atom, R.sub.3 is selected from the group consisting of substituted and unsubstituted aryl, substituted and unsubstituted heteroaryl, and substituted and unsubstituted metallocenyl, R.sub.4 is an organic group having 1-20 carbon atoms, n is 0, 1, 2, 3, 4 or 5, X is an anionic ligand. A process for the preparation of the complex, and its use in carbon-carbon or carbon-nitrogen coupling reactions is also provided.

The invention deals with the separation of homogeneous catalysts from reaction mixtures with the help of organophilic nanofiltration. It is based on the object of indicating an option as to how organophilic nanofiltration can be used economically for separating off homogeneous catalysts from reaction mixtures if the separation-active material of the membrane satisfying the separation aim is not available in sufficiently large amounts or only at high cost. This object is achieved by taking into consideration a particular membrane performance indicator during the design and/or the execution of the corresponding membrane separation process.

A method for producing a catalyst composition for hydrogenation, wherein: (A): a titanocene compound represented by following general formula (1): ##STR00001## wherein R.sup.5 and R.sup.6 represent a group selected from the group consisting of hydrogen, a hydrocarbon group having 1 to 12 carbon atoms, an aryloxy group, an alkoxy group, a halogen group and a carbonyl group, and may be the same or different, and R.sup.1 and R.sup.2 represent a group selected from the group consisting of hydrogen and a hydrocarbon group having 1 to 12 carbon atoms, and may be the same or different, provided that R.sup.1 and R.sup.2 represent are not all hydrogens or all hydrocarbon groups having 1 to 12 carbon atoms; (B): a compound containing at least one element selected from the group consisting of elements Li, Na, K, Mg, Zn, Al, and Ca; and (C): an unsaturated compound
are used, and the method has: a force application step of applying a shearing force at a shearing rate of 1000 (1/s) or more to at least component (A); and a step of mixing components (A), (B), and (C).