Precipitation-driven synthesis offers the possibility of obtaining high reaction yields using very low volume reactors and is finding increasing applications in biocatalysis. Here, a model that allows straightforward prediction of when such a precipitation-driven reaction will be thermodynamically feasible is presented. This requires comparison of the equilibrium constant, K_eq, with the saturated mass action ratio, Z_sat, defined as the ratio of product solubilities to reactant solubilities. A hypothetical thermodynamic cycle that can be used to accurately predict Z_sat in water is described. The cycle involves three main processes: fusion of a solid to a supercooled liquid, ideal mixing of the liquid with octanol, and partitioning from octanol to water. To obtain the saturated mass action ratio using this cycle, only the melting points of the reactants and products, and in certain cases the pK_a of ionisable groups, are required as input parameters. The model was tested on a range of enzyme-catalysed peptide syntheses from the literature and found to predict accurately when precipitation-driven reaction was possible. The methodology employed is quite general and the model is therefore expected to be applicable to a wide range of other (bio)-catalysed reactions.

Although great care is generally taken to buffer aqueous enzyme reactions, active control of acid-base conditions for biocatalysis in low-water media is rarely considered. Here we describe a new class of solid-state acid-base buffers suitable for use in organic media. The buffers, composed of a zwitterion and its sodium salt, are able to set and maintain the ionisation state of an enzyme by the exchange of H⁺ and Na⁺ ions. Surprisingly, equilibrium is established between the different solid components quickly enough to provide a practical means of controlling acid-base conditions during biocatalysed reactions. We developed an organosoluble chromoionophore indicator to screen the behaviour of possible buffer pairs and quantify their relative H⁺/Na⁺ exchange potential. The transesterification activity of an immobilised protease, subtilisin Carlsberg, was measured in toluene in the presence of a range of buffers. The large observed difference in rates showed good correlation with that expected from the measured exchange potentials. The maximum water activities accessible without formation of hydrates or solutions of the buffers are reported here. The indicator was also used to monitor, for the first time in situ, changes in the acid-base conditions of an enzyme-catalysed transesterification reaction in toluene. We found that even very minor amounts of an acidic by-product of hydrolysis were leading to protonation of the enzyme, resulting in rapid loss of activity. Addition of solid-state buffer was able to prevent this process, shortening reaction times and improving yields. Solid-state buffers offer a general and inexpensive way of precisely controlling acid-base conditions in organic solvents and thus also have potential applications outside of biocatalysis.