Patent EA-001608-B1 (EA)
Title: Processes employing indicator ligands
Inventor: BRYANT DAVID ROBERT
IPC: F04D29/28
Filed: 1996-12-05
Abstract: 1. A hydroformylation process which comprises reacting one or more reactants in the presence of a metal-organopolyphosphite ligand complex catalyst and optionally free organopolyphosphite ligand, and an amount of a sterically hindered organophosphorus ligand different from the organopolyphosphite ligand of said metal-organopolyphosphite ligand complex catalyst, to produce one or more products, wherein said sterically hindered organophosphorus ligand (i) has a coordination strength with respect to the metal of said metal-organopolyphosphite ligand complex catalyst less than the organopolyphosphite ligand of said metal-organopolyphosphite ligand complex catalyst, (ii) when complexed with the metal to form a metal-sterically hindered organophosphorus ligand complex catalyst, provides a reaction rate of at least 25 percent of the reaction rate provided by the organopolyphosphite ligand of said metal-organopolyphosphite ligand complex catalyst, (iii) optionally has a coordination strength with respect to the metal of said metal-organopolyphosphite ligand complex catalyst greater than carbon monoxide, and (iv) optionally when complexed with the metal to form a complex-indicator, provides a normal:branched product isomer ratio lower than the normal:branched product isomer ratio provided by the organopolyphosphite ligand of said metal-organopolyphosphite ligand complex catalyst. 2. A process according Claim 1, which comprises (i) reacting in at least one reaction zone one or more reactants in the presence of a metal-organopolyphosphite ligand complex catalyst and optionally free organopolyphosphite ligand to produce a reaction product fluid comprising one or more products and (ii) separating in at least one separation zone or in said at least one reaction zone the one or more products from said reaction product fluid, the process is conducted in the presence of a sterically hindered organophosphorus ligand which is determined in Claim 1. 3. A method of monitoring organopolyphosphite ligand depletion in a process claimed in Claim 1, wherein sterically hindered organophosphorus ligand is used in an amount sufficient to monitor said organopolyphosphite ligand depletion. 4. A reaction mixture comprising one or more products in which said reaction mixture is prepared by a process which claimed in Claim 1. 5. A batchwise or continuously generated reaction mixture obtained by method, claimed in Claim 1, and comprising, based on 100 percent of the weight of the reaction mixture and exclusive of any water present: (1) greater than about 25, preferably greater than about 90 weight percent of one or more products; (2) less than about 30, preferably less than about 10 weight percent of one or more reactants; (3) less than about 10, preferably less than about 1 weight percent of a metal-organopolyphosphite ligand complex catalyst; (4) less than about 10, preferably less than about 5 weight percent of a sterically hindered organophosphorus ligand different from the organopolyphosphite ligand of said metal-organopolyphosphite ligand complex catalyst; and (5) less than about 5, preferably less than about 1 weight percent of a metal-sterically hindered organophosphorus ligand complex catalyst; wherein said sterically hindered organophosphorus ligand is as determined in Claim 1. 6. A catalyst precursor composition comprising a metal-organopolyphosphite ligand complex catalyst and a sterically hindered organophosphorus ligand different from the organopolyphosphite ligand of said metal-organopolyphosphite ligand complex catalyst, wherein said sterically hindered organophosphorus ligand is as determined in Claim 1. 7. The process of Claims 1 and 2, the method of Claim 3, the reaction mixture of Claims 4 and 5 and the catalyst precursor composition of Claim 6, wherein said metal-organopolyphosphite ligand complex catalyst is homogeneous or heterogeneous. 8. The process of Claims 1 and 2 and the process employed in Claim 3 wherein said processes are carried out in the presence of from about 1.1 to about 4 moles of organopolyphosphite ligand per mole of metal present in the reaction medium. 9. The process of Claims 1 and 2 and the process employed in Claims 3 wherein said sterically hindered organophosphorus ligand is present in an amount greater than about 0.05 equivalents of the metal employed. 10. The process of Claims 1 and 2, the method of Claim 3, the reaction mixtures of Claims 4 and 5 and the catalyst precursor composition of Claim 6 wherein said metal-organopolyphosphite ligand complex catalyst comprises rhodium, complexed with an organopolyphosphite ligand represented by the formula:   wherein X<1> represents a substituted or unsubstituted _n_-valent hydrocarbon bridging radical containing from 2 to 40 carbon atoms, each R<9> is the same or different and represents a divalent hydrocarbon radical containing from 4 to 40 carbon atoms, each R<10> is the same or different and represents a substituted or unsubstituted monovalent hydrocarbon radical containing from 1 to 24 carbon atoms, _a_ and _b_ can be the same or different and each have a value of 0 to 6, with the proviso that the sum of _a_+_b_ is 2 to 6 and _n_ equals _a_+_b_. 12. The process of Claims 1 and 2, the method of Claim 3, the reaction mixtures of Claims 4 and 5 and the catalyst precursor composition of Claim 6 wherein said metal-organopolyphosphite ligand complex catalyst comprises rhodium, complexed with an organopolyphosphite ligand having the formula selected from:   wherein X<1> represents a substituted or unsubstituted divalent hydrocarbon bridging radical containing from 2 to 40 carbon atoms, each R<9> is the same or different and represents a divalent hydrocarbon radical containing from 4 to 40 carbon atoms, and each R<10> is the same or different and represents a substituted or unsubstituted monovalent hydrocarbon radical containing from 1 to 24 carbon atoms. 12. The process of Claims 1 and 2, the method of Claim 3, the reaction mixtures of Claims 4 and 5 and the catalyst precursor composition of Claim 6 wherein said metal-organopolyphosphite ligand complex catalyst comprises rhodium, complexed with an organopolyphosphite ligand having the formula selected from:     wherein X<1> represents a substituted or unsubstituted divalent hydrocarbon bridging radical containing from 2 to 40 carbon atoms, R<9> is a divalent hydrocarbon radical containing from 4 to 40 carbon atoms, each R<10> is the same or different and represents a substituted or unsubstituted monovalent hydrocarbon radical containing from 1 to 24 carbon atoms, each Ar is the same or different and represents a substituted or unsubstituted aryl radical, each _y_ is the same or different and has a value of 0 or 1, Q represents a divalent bridging group selected from -C(R<5>)2-, -O-, -S-, -NR<6>-, Si(R<7>)2- and -CO-, wherein each R<5> is the same or different and represents hydrogen, alkyl radicals having from 1 to 12 carbon atoms, phenyl, tolyl, and anisyl, R<6> represents hydrogen or a methyl radical, each R<7> is the same or different and represents hydrogen or a methyl radical, and _m_ has a value of 0 or 1. 13. The process of Claims 1 and 2, the method of Claim 3, the reaction mixtures of Claims 4 and 5 and the catalyst precursor composition of Claim 6 wherein said metal-sterically hindered organophosphorus ligand complex catalyst having the formula selected from: (i) a triorganophosphine ligand represented by the formula:   wherein R<1> is the same or different and represents a substituted or unsubstituted monovalent hydrocarbon radical containing from 1 to 24 carbon atoms or greater; (ii) a monoorganophosphite represented by the formula:   wherein R<3> represents a substituted or unsubstituted trivalent hydrocarbon radical containing from 4 to 40 carbon atoms or greater; (iii) a diorganophosphite represented by the formula:   wherein R<4> represents a substituted or unsubstituted divalent hydrocarbon radical containing from 4 to 40 carbon atoms or greater and W represents a substituted or unsubstituted monovalent hydrocarbon radical containing from 1 to 18 carbon atoms or greater; (iv) a triorganophosphite represented by the formula:   wherein each R<8> is the same or different and represents a substituted or unsubstituted monovalent hydrocarbon radical; and (v) an oxide of an organopolyphosphite represented by the formula:   wherein X<1> represents a substituted or unsubstituted _n_-valent hydrocarbon bridging radical containing from 2 to 40 carbon atoms, each R<9> is the same or different and represents a divalent hydrocarbon radical containing from 4 to 40 carbon atoms, each R<10> is the same or different and represents a substituted or unsubstituted monovalent hydrocarbon radical containing from 1 to 24 carbon atoms, _a_ and _b_ can be the same or different and each have a value of 0 to 6, with the proviso that the sum of _a_+_b_ is 2 to 6 and _n_ equals _a_+_b_. 14. The process of Claims 1 and 2, the method of Claim 3, the reaction mixtures of Claims 4 and 5 and the catalyst precursor composition of Claim 6 wherein said sterically hindered organophosphorus ligand comprises a sterically hindered organophosphine or organophosphite ligand. 15. The process of Claim 14 wherein said sterically hindered organophosphine ligand comprises a substituted triphenylphosphine, a substituted tricyclohexylphosphine, a substituted cyclohexyldiphenylphosphine, or a substituted dicyclohexylphenylphosphine. 16. The process of Claim 14 wherein said sterically hindered organophosphite ligand comprises an oxide of an organopolyphosphite represented by the formula: