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    • 1. 发明授权
    • Process for hydroformylation of an olefin
    • 烯烃氢化方法
    • US5105018A
    • 1992-04-14
    • US596383
    • 1990-10-12
    • Chihiro MiyazawaHiroshi Mikami
    • Chihiro MiyazawaHiroshi Mikami
    • B01J31/22B01J31/24C07B61/00C07C45/50C07C47/02
    • C07C45/50
    • 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 (hereafter referred to as a "flow mixing parameter") defined by the formula (I):U.tbd.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.sup.2 /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.