A process for separating one or more organophosphorus ligand degradation products, one or more reaction byproducts and one or more products from a reaction product fluid comprising one or more unreacted reactants, a metal-organophosphorus ligand complex catalyst, optionally free organophosphorus ligand, said one or more organophosphorus ligand degradation products, said one or more reaction byproducts, said one or more products, one or more polar reaction solvents and one or more nonpolar reaction solvents, wherein said process comprises (1) supplying said reaction product fluid from a reaction zone to a separation zone, (2) subjecting said reaction product fluid in said separation zone to fractional countercurrent extraction with at least two immiscible extraction solvents, said at least two immiscible extraction solvents comprising at least one polar extraction solvent and at least one nonpolar extraction solvent, to obtain by phase separation a polar phase comprising said one or more unreacted reactants, said metal-organophosphorus ligand complex catalyst, said optionally free organophosphorus ligand, said one or more polar reaction solvents and said at least one polar extraction solvent and a nonpolar phase comprising said one or more organophosphorus ligand degradation products, said one or more reaction byproducts, said one or more products, said one or more nonpolar reaction solvents and said at least one nonpolar extraction solvent, and (3) recovering said nonpolar phase from said polar phase;
- wherein (i) the selectivity of the polar phase for the organophosphorus ligand with respect to the one or more products is expressed by the following partition coefficient ratio Ef1:
- Ef1 = Partition coefficient Kp1 of organophosphorus ligand Partition coefficient Kp2 of one or more products
- in which said partition coefficient Kp1 is the ratio of the concentration of organophosphorus ligand in the polar phase after extraction to the concentration of organophosphorus ligand in the nonpolar phase after extraction, said partition coefficient Kp2 is the ratio of the concentration of products in the polar phase after extraction to the concentration of products in the nonpolar phase after extraction, and said Ef1 is a value greater than about 2.5, (ii) the selectivity of the polar phase for the organophosphorus ligand with respect to the one or more organophosphorus ligand degradation products is expressed by the following partition coefficient ratio Ef2:
- Ef2 = Partition coefficient Kp1 of organophosphorus ligand Partition coefficient Kp3 of one or more organophosphorus ligand degradation products
- in which said partition coefficient Kp1 is as defined above, said partition coefficient Kp3 is the ratio of the concentration of organophosphorus ligand degradation products in the polar phase after extraction to the concentration of organophosphorus ligand degradation products in the nonpolar phase after extraction, and said Ef2 is a value greater than about 2.5, and (iii) the selectivity of the polar phase for the organophosphorus ligand with respect to the one or more reaction byproducts is expressed by the following partition coefficient ratio Ef3:
- Ef3 = Partition coefficient Kp1 of organophosphorus ligand Partition coefficient Kp4 of one or more reaction byproducts
- in which said partition coefficient Kp1 is as defined above, said partition coefficient Kp4 is the ratio of the concentration of reaction byproducts in the polar phase after extraction to the concentration of reaction byproducts in the nonpolar phase after extraction, and said Ef3 is a value greater than about 2.5.