Mass balancing in kinetic resolution: calculating yield and enantiomeric excess using chiral balance.

When kinetic resolution is applied for the production of enantiomerically pure compounds, process options may be used which involve more than one chiral substrate and one chiral product, such as sequential or parallel enzymatic kinetic resolutions or hydrolysis of diastereomers. Although the relation between the yields (y) of the chiral compounds is straightforward in these cases, the relation between their enantiomeric excess (ee) values is not. Combining mass balances into a so-called chiral balance (Sigma y x ee(R) = 0) provides the relation between enantiomeric excess values in a useful manner. This chiral balance easily shows which nonmeasured enantiomeric excess values and yields can be calculated from measured values. The chiral balance is only valid when configurations at chiral centers are conserved.

Kinetic analysis of enzymatic chiral resolution by progress curve evaluation.

The present study deals with kinetic modeling of enzyme-catalyzed reactions by integral progress curve analysis, and shows how to apply this technique to kinetic resolution of enantiomers. It is shown that kinetic parameters for both enantiomers and the enantioselectivity of the enzyme may be obtained from the progress curve measurement of a racemate only.A parameter estimation procedure has been established and it is shown that the covariance matrix of the obtained parameters is a useful statistical tool in the selection and verification of the model structure. Standard deviations calculated from this matrix have shown that progress curve analysis yields parameter values with high accuracies.Potential sources of systematic errors in (multiple) progress curve analysis are addressed in this article. Amongst these, the following needed to be dealt with: (1) the true initial substrate concentrations were obtained from the final amount of product experimentally measured (mass balancing); (2) systematic errors in the initial enzyme concentration were corrected by incorporating this variable in the fitting procedure as an extra parameter per curve; and (3) enzyme inactivation is included in the model and a first-order inactivation constant is determined.Experimental verification was carried out by continuous monitoring of the hydrolysis of ethyl 2-chloropropionate by carboxylesterase NP and the alpha-chymotrypsin-catalyzed hydrolysis of benzoylalanine mathyl ester in a pH-stat system. Kinetic parameter values were obtained with high accuracies and model predictions were in good agreement with independent measurements of enantiomeric excess values or literature data. (c) 1994 John Wiley & Sons, Inc.

A simple method to determine the enantiomeric ratio in enantioselective biocatalysis.

The enantiomeric ratio (E) is commonly used to characterize the enantioselectivity in enzyme-catalyzed kinetic resolution. In this paper this parameter is directly derived from the enantiomeric excess of substrate and product. This is formally more correct than using Chen's equation after calculating the degree of conversion from both ee values using the relation of Sih and Wu. New expressions and useful graphs have been generated for reversible and irreversible uni-uni reactions. The theoretical predictions have been verified experimentally for various reactions. Values for E and the thermodynamic equilibrium constant, KEQ, were obtained for a (DL)-dehalogenase-catalyzed dehalogenation, a hydrolysis reaction by porcine pancreatic lipase, and for C. Cylindracea lipase-catalyzed esterification and transesterification. In view of the current developments in the field of chiral analysis, this method is an easily available tool in the quantitative treatment of enzyme-catalyzed resolution of enantiomers.

Effect of thermodynamic water activity on amino-acid ester synthesis catalyzed by agarose-chymotrypsin in 3-pentanone.

Chymotrypsin linked to agarose beads by multi-point covalent attachment catalyzes synthesis of Ac-Trp-OEt in 3-pentanone even when the thermodynamic water activity (aw) of the system is reduced to as low as 0.4. If fully hydrated catalyst is added to the reaction mixture before removal of water, product is formed linearly once aw has stabilized. The initial rate is reduced from that if aw is kept close to 1 (0.47 mmol s-1 (kg enzyme)-1), to 50% (aw 0.9), 25% (aw 0.4) and < 1% (aw 0.25). The large drop between aw of 1 and 0.9 probably reflects the effects of water removal on the agarose gel structure. Catalyst partly dried (even only to aw 0.86) before adding to the organic phase is inactive. At reduced aw, the equilibrium (when reached) is shifted in favor of the ester, as expected.