Patent classifications
C07C2531/12
CHIRAL PLATINUM COMPLEX, METHOD FOR PREPARING THE SAME, AND METHOD FOR USING THE SAME
A chiral platinum complex having a chemical formula (I):
##STR00001##
A method for synthesizing the chiral platinum complex (I), includes: dissolving 0.700 g of Pt(DMSO).sub.2(NO.sub.3).sub.2 in 30 mL of dichloromethane as a solvent to yield a solution; adding 0.450 g of 1,4-(4R)-diphenyl-2-oxazolinyl benzene to the solution, and reflux a resulting mixture for reaction for 48 hrs, and stopping the reaction; filtrating reaction products; and adding dichloromethane and petroleum ether, and naturally volatilizing to yield a binuclear platinum complex single crystal. A method for condensation of benzophenone imine and trimethylsilitrile by using the chiral platinum complex as a catalyst. A method for treating cancer includes administering the chiral platinum complex to a patient in need thereof. The cancer includes: lung cancer (A549), nasopharyngeal carcinoma (KB), anti-drug-resistant nasopharyngeal carcinoma (KB-VIn), and human breast cancer (MCF-7).
ACYCLIC CARBENE LIGAND FOR RUTHENIUM COMPLEX FORMATION, RUTHENIUM COMPLEX CATALYST, AND USE THEREOF
Provided are a novel acyclic carbene ligand for ruthenium complex formation; a ruthenium complex catalyst using the ligand; a method of using the complex as a catalyst in an ethylene-metathesis ethenolysis reaction; a method of preparing the ruthenium complex catalyst; and a method of preparing a linear alpha-olefin, the method including the step of reacting a linear or cyclic alkene compound in the presence of the ruthenium complex catalyst.
The acyclic carbene ligand of the present invention and the ruthenium complex catalyst using the same have high selectivity and turnover number for terminal olefin formation in an ethylene-metathesis ethenolysis reaction, and thus linear -olefins may be prepared with a high yield.
Flexible manufacturing system for selectively producing different linear alpha olefins
A flexible manufacturing system for selectively producing different alpha-olefins from ethylene includes: (a) a reaction section 18 with ethylene feed operative to oligomerize ethylene; (b) a catalyst feed system 12, 14, 16 comprising a plurality of independent homogeneous catalyst feeders connected with the reaction section for alternatively providing different selective homogeneous catalyst compositions to the reaction section; (c) an ethylene recycle column 22 coupled to the reaction section and adapted to receive crude product and unreacted ethylene therefrom, the recycle column being operative to separate ethylene and optionally lower oligomers from the crude product which are recycled to the ethylene feed to the reaction section, the ethylene recycle column being further operative to provide a crude product bottoms stream; (d) a catalyst removal section 20 coupled to the reaction section adapted to remove spent catalyst from the system; and (e) a first product separation column 24 connected to the recycle column receiving the crude product stream therefrom, the product separation column being operative to separate purified oligomer from the crude product stream. Optionally provided is a second product separation column 26.
APPLICATION OF METAL HYDRIDE/PALLADIUM COMPOUND SYSTEM IN PREPARATION OF 1,3-DICARBONYL COMPOUND IN CASCADE REACTION OF ELECTRON-DEFICIENT ALKENE COMPOUND
Provided is an application of a metal hydride/palladium compound system in the preparation of a 1,3-dicarbonyl compound in a cascade reaction of an electron-deficient alkene compound, said reaction comprising the following steps: under the protection of nitrogen, a palladium compound and a metal hydride are suspended and stirred in a solvent, then an electron-deficient alkene compound is added; the mixture reacts at 0 C. to 100 C. for 0.3 to 10 hours; a saturated ammonium chloride aqueous solution is added to stop the reaction, and then extraction, drying by evaporation and purification by column chromatography are performed to obtain the product of 1,3-dicarbonyl compound. The hydride and palladium compound catalysts used in the method are reagents easily obtained in a laboratory; compared with the commonly used methods of hydrogenation with hydrogen gas, the method can be easily operated, and has high safety, mild conditions and high reaction yield.
Method for continuously synthesizing propellane compound
Disclosed is a method for continuously synthesizing a propellane compound. The method includes the following steps: using 1,1-dibromo-2,2-bis(chloromethyl)cyclopropane or a derivative thereof as a raw material to form a ring with a lithium metal agent by a continuous reaction, so as to synthesize the propellane compound. A technical scheme of the present disclosure is applied, and a continuous reaction device is used.
Process for producing an oligomerization catalyst
The invention relates to a process for producing an oligomerization catalyst comprising nickel oxide and a silicon-alumina support material, wherein the silica-alumina support material is in the ammonium form. The present invention further relates to a process for oligomerization of C3- to C6-olefins using the oligomerization catalyst produced according to the invention.
Process for the preparation of dicidal
Process for the preparation of dicidal.
Flexible Manufacturing System for Selectively Producing Different Linear Alpha Olefins
A flexible manufacturing system for selectively producing different alpha-olefins from ethylene includes: (a) a reaction section 18 with ethylene feed operative to oligomerize ethylene; (b) a catalyst feed system 12, 14, 16 comprising a plurality of independent homogeneous catalyst feeders connected with the reaction section for alternatively providing different selective homogeneous catalyst compositions to the reaction section; (c) an ethylene recycle column 22 coupled to the reaction section and adapted to receive crude product and unreacted ethylene therefrom, the recycle column being operative to separate ethylene and optionally lower oligomers from the crude product which are recycled to the ethylene feed to the reaction section, the ethylene recycle column being further operative to provide a crude product bottoms stream; (d) a catalyst removal section 20 coupled to the reaction section adapted to remove spent catalyst from the system; and (e) a first product separation column 24 connected to the recycle column receiving the crude product stream therefrom, the product separation column being operative to separate purified oligomer from the crude product stream. Optionally provided is a second product separation column 26.
Reduced polymer formation for selective ethylene oligomerizations
Disclosed herein are processes, systems, and reaction systems for the oligomerization of ethylene to form an ethylene oligomer product in a reaction zone using a catalyst system having i) a chromium component comprising a heteroatomic ligand chromium compound complex of the type disclosed herein, and ii) an aluminoxane. A C.sub.3+ olefin can be present in the reaction zone for a period of time, where the C.sub.3+ olefin is not an ethylene oligomer formed in-situ within the reaction zone.
GROUP 5 METAL COMPLEXES FOR CATALYTIC AMINE FUNCTIONALIZATION
This application pertains to group 5 metal complexes having the structure of Formula I:
##STR00001##
and their potential utility in catalyzing -alkylation of secondary amine-containing moieties.