Hydrocyanation process with reduced yield losses
By using a catalyst precursor composition of zero-valent nickel and multidentate phosphorus-containing ligands in the hydrocyanation reaction to control the reaction conditions, the adverse impact of 2-pentenenitrile on the catalyst efficiency was solved and the yield of adiponitrile was improved. efficiency and product purity, simplifying the process and reducing costs.
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Embodiment 1
[0195] Ligand "A" of Example 1 may be prepared by any suitable synthetic means known in the art. For example, 3,3'-diisopropyl-5,5',6,6'-tetramethyl-2,2'-linked Phenol, said U.S. Published Patent Application 2003 / 0100802 is incorporated herein by reference, wherein 4-methylthymol can be present in a copper chlorohydroxide-TMEDA complex (TMEDA is N, N, N', N'-tetramethylethylenediamine) and air for oxidative coupling with substituted biphenols.
[0196] For example, o-cresol chlorophosphite (C 7 h 7 O) 2 PC1, said US Published Patent Application 2004 / 0106815 is hereby incorporated by reference. For the selective formation of this chlorophosphite, anhydrous triethylamine and o-cresol can be added separately and simultaneously in a controlled manner to PCl dissolved in a suitable solvent under temperature-controlled conditions. 3 middle.
[0197] For example, according to the method disclosed in US Pat. Reaction of biphenols to form the desired ligand "A," said US Patent 6...
Embodiment 2
[0237] Use Ligand "A" and use ZnCl 2 As a Lewis acid cocatalyst, the continuous hydrocyanation process of the present invention is demonstrated.
[0238] Target reaction rate = 1.6 x 10 -4 moles of HCN / L-s
[0239] Temperature = 50°C
[0240] Mole % of 2PN feed = 20.6%
[0241] The target feed rates for the reaction components are as follows.
[0242] Reagent Feed rate, g / hr HCN a 0.29 3, 4PN (3PN+4PN) 0.94 2PN 0.25 Ni catalyst, calculated as Ni metal 0.0013 total ligand b 0.027 wxya 2 Co-catalyst 0.0020
[0243] Notes: a HCN other than PN solvents. b Mixture of ligand "A" and the corresponding monodentate phosphite as described above.
[0244] The total feed molar ratio of 2PN to all unsaturated nitriles was about 0.21, while the total feed molar ratio of HCN to all unsaturated nitriles was about 0.70.
[0245] Average GC analysis of reaction products withdrawn from 49 to 53 hours after the onset of continuous...
Embodiment 3
[0261] Using Ligand "B" shown below and using FeCl 2 As a Lewis acid cocatalyst, the continuous hydrocyanation process of the present invention is demonstrated.
[0262]
[0263] Ligand "B"
[0264] target reaction rate = 1.6 x 10 -4 moles of HCN / L-s
[0265] Temperature = 50°C
[0266] Mole % of 2PN feed = 15.4%
[0267] The target feed rates for the reaction components are as follows.
[0268] Reagent Feed rate, g / hr HCN a 0.29 3, 4PN (3PN+4PN) 0.95 2PN 0.175 Ni catalyst, calculated as Ni metal 0.0013 total ligand b 0.029 FeCl 2 Co-catalyst 0.0019
[0269] Notes: a HCN other than PN solvents. b Mixture of ligand "B" and the corresponding monodentate phosphite as described above.
[0270] The total feed molar ratio of 2PN relative to all unsaturated nitriles was about 0.15, while the total feed molar ratio of HCN relative to all unsaturated nitriles was about 0.80.
[0271] Average GC ana...
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Abstract
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