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    • 1. 发明专利
    • DE69017346D1
    • 1995-04-06
    • DE69017346
    • 1990-10-17
    • MITSUBISHI CHEM IND
    • MIYAZAWA CHIHIROMIKAMI HIROSHI
    • B01J31/24C07B61/00B01J31/22C07C45/50C07C47/02
    • A process for hydroformylation of an olefin, which comprises reacting an olefin with carbon monoxide and hydrogen in the presence of a rhodium catalyst having a trivalent organic phosphorus compound as a ligand, wherein the hydroformylation reaction is conducted by two stage reactor systems i.e. a first stage reactor system comprising a reactor or reactors having a mixing characteristic of the liquid phase being substantially of complete mixing type, and a second stage reactor system being a reaction system of a catalyst solution circulating type and comprising a reactor or reactors having a mixing characteristic of piston flow type wherein when the mixing characteristic of the liquid phase is represented by a diffusion model, a non-dimensional number U (hereinafter referred to as a "flow mixing parameter") defined by the formula (I): U IDENTICAL uL/2E (I) wherein u is an average flow velocity (cm/sec), L is the length (cm) of the reaction layer, and E is an average diffusion coefficient (cm /sec), is at least 0.4, a gaseous product or gas-liquid mixture discharged from the first stage reactor system, is separated into a stream containing the unreacted olefin and other stream, and a part or whole of the stream containing the unreacted olefin is supplied to the second stage reactor system.
    • 6. 发明专利
    • BR8707021A
    • 1988-08-09
    • BR8707021
    • 1987-12-23
    • MITSUBISHI CHEM IND
    • MIYAZAWA CHIHIROMIKAMI HIROSHITSUBOI AKIOHAMANO KATSUHIDE
    • C07C45/50C07C45/49
    • A process for the hydroformylation of an olefin, which comprises hydroformylating an olefinic compound by reacting it with carbon monoxide and hydrogen in a hydroformylation reaction zone in the presence of a catalyst solution containing rhodium and an oxide of an organic trivalent phosphorus compound to form an aldehyde having a carbon number larger by one than that of the olefinic compound; adding an organic trivalent phosphorus compound to the reaction mixture, followed by distillation to separate a distillate containing the aldehyde from a high-boiling residue containing rhodium; oxidizing the high-boiling residue at the same time as or subsequent to the distillation to convert the organic trivalent phosphorus compound to its oxide; and recycling the oxidized residue to the hydroformylation reaction zone as a recycling catalyst solution, wherein the hydroformylation reaction is conducted under a condition such that the proportion of an alcohol content supplied as contained in the recycling catalyst solution is maintained at a level of not higher than 14% by weight based on the total amount of the olefinic compound and the catalyst solution supplied to the hydroformylation reaction zone.
    • 10. 发明专利
    • PROCESS FOR HYDROFORMYLATION OF AN OLEFIN
    • CA2027991A1
    • 1991-04-20
    • CA2027991
    • 1990-10-18
    • MITSUBISHI CHEM INDMITSUBISHI CHEM CORP
    • MIYAZAWA CHIHIROMIKAMI HIROSHI
    • B01J31/22B01J31/24C07B61/00C07C45/50C07C47/02
    • A process for hydroformylation of an olefin, which comprises reacting an olefin with carbon monoxide and hydrogen in the presence of a rhodium catalyst having a trivalent organic phosphorus compound as a ligand, wherein the hydroformylation reaction is conducted by two stage reactor systems i.e. a first stage reactor system comprising a reactor or reactors having a mixing characteristic of the liquid phase being substantially of complete mixing type, and a second stage reactor system being a reaction system of a catalyst solution circulating type and comprising a reactor or reactors having a mixing characteristic of piston flow type wherein when the mixing characteristic of the liquid phase is represented by a diffusion model, a non-dimensional number U (hereinafter referred to as a "flow mixing parameter") defined by the formula (I): U = ~L/2~ (I) wherein ~ is an average flow velocity (cm/sec), L is the length (cm) of the reaction layer, and ~ is an average diffusion coefficient (cm2/sec), is at least 0.4, a gaseous product or gas-liquid mixture discharged from the first stage reactor system, is separated into a stream containing the unreacted olefin and other stream, and a part or whole of the stream containing the unreacted olefin is supplied to the second stage reactor system.