The present invention provides a catalyst system for producing cyclic carbonates from carbon dioxide (CO.sub.2) and epoxide-based compounds comprising: a pre-catalyst; and a co-catalyst wherein said pre catalyst is BiCl.sub.3 and said co-catalyst is selected from tetra-n-butylammonium bromide (TBAB), tetra-n-butylammonium iodide (TBAI), tetra-n-butylphosphonium bromide (PBu.sub.4Br), tetra-n-butylphosphonium iodide (PBu.sub.4I) or mixtures thereof.

The present invention provides a catalyst system for producing cyclic carbonates comprising: a pre-catalyst, which is BiCl.sub.3 having amounts in the range from 5 to 10% by weight of silica support; a compound having formula (I) ##STR00001## wherein: Y is selected from bromide (Br.sup.?) or iodide (I.sup.?); R.sup.1, R.sup.2, and R.sup.3 are methyl group or R.sup.1, R.sup.2, and R.sup.3 are taken together to form a heteroaryl ring having formula (II) ##STR00002##
and a silica (SiO.sub.2) support.

The synthesis and structure of beta-diketiminate manganese compounds are described, as well as their use as catalysts for the hydrosilylation and hydroboration of unsaturated organic compounds and main group element-main group element bond formation via dehydrogenative coupling.

Disclosed is a catalyst and process for producing ammonia (NH.sub.3). The process includes contacting a gaseous feed mixture comprising nitrogen (N.sub.2) and hydrogen (H.sub.2) with a metal hydride material under reaction conditions sufficient to produce a product stream comprising NH.sub.3.

A palladium hydride nanomaterial includes nanostructures having a chemical composition represented by the formula: M.sub.y-Pd.sub.xH.sub.z, where M is at least one metal different from palladium; x has a non-zero value in the range of 0 to 5; y has a value in the range of 0 to 5; and z has a non-zero value in the range of 0 to 5.

Iron-based homogeneous catalysts, supported by pincer ligands, are employed in the transfer hydrogenation of esters using C.sub.2-C.sub.12 alcohols as sacrificial hydrogen donors to produce corresponding alcohols from the esters. No external H.sub.2 pressure is required. The reaction can be carried out under ambient pressure.

Iron-based homogeneous catalysts, supported by pincer ligands, are employed in the transfer hydrogenation of esters using C.sub.2-C.sub.12 alcohols as sacrificial hydrogen donors to produce corresponding alcohols from the esters. No external H.sub.2 pressure is required. The reaction can be carried out under ambient pressure.

Metal-organic framework (MOFs) compositions based on postsynthetic metalation of secondary building unit (SBU) terminal or bridging OH or OH.sub.2 groups with metal precursors or other post-synthetic manipulations are described. The MOFs provide a versatile family of recyclable and reusable single-site solid catalysts for catalyzing a variety of asymmetric organic transformations, including the regioselective boryiation and siiylation of benzyiic CH bonds, the hydrogenation of aikenes, imines, carbonyls, nitroarenes, and heterocycles, hydroboration, hydrophosphination, and cyclization reactions. The solid catalysts can also be integrated into a flow reactor or a supercritical fluid reactor.

The present invention, with the purpose of providing a catalyst composition for hydrogenation having high hydrogenation activity, provides a catalyst composition for hydrogenation, comprising: a titanocene dichloride; an organometal compound comprising one or two or more elements selected from the group consisting of Li, Na, K, Mg, Zn, Al and Ca; an unsaturated compound; and a polar compound, wherein a content ratio of the unsaturated compound to the titanocene dichloride is 0.1 or more and 8.0 or less, and a content ratio of the polar compound to the titanocene dichloride is 0.01 or more and 2.0 or less.

Provided herein are bi-metallic catalysts, methods of making, and uses thereof. In some embodiments, the bi-metallic catalyst contains two different metal catalysts that can be used in hydrocarbon metathesis reactions, in some embodiments, the methods of making the bi-metallic catalysts can include two steps utilizing a surface organometallic chemistry approach in which the two different metal catalysts are sequentially grafted onto a support.