1477-55-0Relevant articles and documents
Isophthalonitrile (IPN) hydrogenation over K modified Ni-Co supported catalysts: Catalyst characterization and performance evaluation
Liu, Chang,Wang, Tiefeng
, p. 63725 - 63733 (2014)
The hydrogenation of isophthalonitrile (IPN) to meta-xylylenediamine (m-XDA) is usually catalyzed by the Raney or supported Ni based catalysts in the presence of basic additive. Although the supported catalysts are safer than the Raney Ni catalysts, they have lower selectivity to m-XDA. This work revealed that the acid sites of NiCo/Al2O3 were responsible for the condensation reactions between amines and imines, which were the dominant side reactions. Besides the original acid sites on γ-Al2O3, the loading of Ni-Co introduced new acid sites, which had a greater contribution to the condensation reactions. The K modification significantly enhanced the selectivity to m-XDA by reducing the two kinds of acid sites. Due to the formation mechanism of new acid sites and the K modification mechanism on these sites, both the K loading and K impregnation sequence affected the catalytic performance. When 3.0 wt% K was introduced to NiCo/Al2O3 by co-impregnation (3KNiCo/Al2O3), the catalyst acidity decreased by 82%, and the selectivity to m-XDA increased from 45.5% to 99.9%. The superiority of the optimized catalyst 3KNiCo/Al2O3 was also confirmed when no basic additive was used.
Role of acid sites and surface hydroxyl groups in isophthalonitrile hydrogenation catalyzed by supported Ni-Co catalysts
Liu, Chang,Hou, Ruijun,Wang, Tiefeng
, p. 26465 - 26474 (2015)
meta-Xylylenediamine (m-XDA) is industrially produced by the hydrogenation of isophthalonitrile (IPN) using Raney Ni/Co and basic additives. Compared with Raney Ni/Co, the supported Ni/Co catalysts are safer and have better mechanical strength. This work aimed at studying the catalytic performance of the supported Ni-Co catalysts in hydrogenation of IPN to m-XDA. The active sites for the condensation side reactions were studied using Ni-Co catalysts supported on different oxides and with different loadings. It was found that the acid sites catalyzed the condensation reactions between intermediate imines and amines. Two types of acid sites existed on the supported Ni-Co catalysts, namely, the original acid sites of the support and new acid sites formed by Ni/Co aluminates. In addition to acid sites, the surface hydroxyl groups on the oxide supports also catalyzed the condensation reactions, but were not active for the hydrogenation reaction. By increasing the Ni-Co loading, the selectivity to m-XDA was significantly enhanced, which was attributed to the suppression of both acid sites and hydroxyl groups. Compared to the low-loading catalysts (5Ni-1.25Co/Al2O3 and 5Ni-1.25Co/SiO2), the high-loading catalysts (20Ni-5Co/Al2O3 and 20Ni-5Co/SiO2) increased the m-XDA selectivity from ~45.5 to 99.9%.
METHOD FOR PRODUCING m-XYLYLENE DIAMINE
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Paragraph 0061-0073; 0075; 0079, (2021/08/13)
PROBLEM TO BE SOLVED: To provide a method for producing m-xylylene diamine that makes it possible to efficiently produce m-xylylene diamine by reducing the formation of by-products even when a reaction temperature is lowered in a hydrogenation reaction step. SOLUTION: In the presence of a catalyst with palladium carried on carbon and in the absence of ammonia and an amine compound (excluding a reaction product), 1,3-dicyanobenzene and hydrogen are reacted at 0°C or higher and 50°C or lower, and hydrogen is added to the 1,3-dicyanobenzene, producing m-xylylene diamine. SELECTED DRAWING: None COPYRIGHT: (C)2021,JPOandINPIT
Cobalt pincer complexes for catalytic reduction of nitriles to primary amines
Schneek?nig, Jacob,Tannert, Bianca,Hornke, Helen,Beller, Matthias,Junge, Kathrin
, p. 1779 - 1783 (2019/04/27)
Various cobalt pincer type complexes 1-6 were applied for the catalytic hydrogenation of nitriles to amines. Among these, catalyst 4 is the most efficient, allowing the reduction of aromatic as well as aliphatic nitriles in moderate to excellent yields.
Facile synthesis of supported Ru-Triphos catalysts for continuous flow application in selective nitrile reduction
Konrath, Robert,Heutz, Frank J.L.,Steinfeldt, Norbert,Rockstroh, Nils,Kamer, Paul C.J.
, p. 8195 - 8201 (2019/09/19)
The selective catalytic hydrogenation of nitriles represents an important but challenging transformation for many homogeneous and heterogeneous catalysts. Herein, we report the efficient and modular solid-phase synthesis of immobilized Triphos-type ligands in very high yields, involving only minimal work-up procedures. The corresponding supported ruthenium-Triphos catalysts are tested in the hydrogenation of various nitriles. Under mild conditions and without the requirement of additives, the tunable supported catalyst library provides selective access to both primary amines and secondary imines. Moreover, the first application of a Triphos-type catalyst in a continuous flow process is presented demonstrating high catalyst life-time over at least 195 hours without significant activity loss.