摘要:
The invention relates to phosphites of formula (I) or (II) and their metal complexes, to the production and use of said phosphites as ligands in catalytic reactions, particularly in methods for the hydroformylation of olefins.
摘要:
The invention relates to a method for producing C 5 -aldehyde mixtures from a hydrocarbon mixture containing linear butenes by terminal hydroformylation under isomerizing conditions, wherein a catalyst system is used, comprising rhodium, a bisphosphit ligand of the formula I and an amine of the formula II.
摘要:
The present invention relates to the preparation of 3-methylbut-1-ene from a hydrocarbon stream I comprising isobutene, wherein a hydrocarbon stream II which contains at least 70% by mass of isobutene in relation to the olefins present in the hydrocarbon stream and which has been obtained from hydrocarbon stream I or is identical to it is sent to a process step for hydroformylation, in which isobutene is hydroformylated in the presence of a rhodium catalyst, the aldehyde obtained from the hydroformylation of isobutene is hydrogenated to the corresponding alcohol, and 3-methylbut-1-ene is prepared from the alcohol by elimination of water.
摘要:
The invention relates to a method for enriching a homogenous catalyst from a process flow comprising said homogenous catalyst as a component, wherein the process flow is conducted over at least one membrane and wherein the membrane wholly or partially comprises a polymer that has planar polymer units connected to one another via a rigid link and wherein the linker is contorted, such that at least one planar polymer unit is connected to at least one second planar polymer unit via the link, in a non-co-planar arrangement. The invention furthermore relates to a method for producing tridecanal.
摘要:
The invention relates to a bisphosphite of the formula (I) where X = a divalent substituted or unsubstituted bisalkylene or bisarylene radical, Y = a divalent substituted or unsubstituted bisarylene or bisalkylene radical, Z = oxygen or NR9 and R1, R2, R3, R4 are identical or different, substituted or unsubstituted, linked, unlinked or fused aryl or heteroaryl radicals and R9 is hydrogen or a substituted or unsubstituted alkyl or aryl radical, a process for preparing it and also the use of this phosphite in catalysis, in particular in the catalytic hydroformylation of olefins or of organic compounds having C-C double bonds.
摘要:
The present invention relates to the preparation of 3-methylbut-1-ene from a hydrocarbon stream I comprising isobutene, wherein a hydrocarbon stream II which contains at least 70% by mass of isobutene in relation to the olefins present in the hydrocarbon stream and which has been obtained from hydrocarbon stream I or is identical to it is sent to a process step for hydroformylation, in which isobutene is hydroformylated in the presence of a rhodium catalyst, the aldehyde obtained from the hydroformylation of isobutene is hydrogenated to the corresponding alcohol, and 3-methylbut-1-ene is prepared from the alcohol by elimination of water.
摘要:
The present invention relates to the preparation of olefins or olefin mixtures having from 8 to 12 carbon atoms from one or more olefin(s) having from 4 to 6 carbon atoms by means of a four-stage synthesis. The four-stage synthesis comprises the steps of hydroformylation to form the aldehyde, hydrogenation to form the alcohol, elimination of water to form the 1-olefin and metathesis. The C 8 -C 12 -olefins obtained can be used, for example, for peparing plasticizer alcohols, in particular isononanol.
摘要:
The invention relates to a method for separating a dissolved complex catalyst of a metal of the 4th, 5th, 6th, 7th, 8th, 9th or 10th group of the periodic system of elements and/or, optionally, a present free organophosphor ligand of a non-aqueous hydroformylation reaction mixture, said mixture containing an aldehyde product and an organic solvent, from at least one membrane which is more permeable with respect to the hydroformylation product than the organophosphor ligand, whereby the separation is carried out under a carbon monoxide partial vapor pressure of more than 200 kPa.