Best practice for scale-down of gas−liquid reactions requires control of the volumetric mass transfer coefficient, k L a. It is demonstrated that the use of small bubble columns can provide well-controlled k L a and catalyst dispersion down to a scale of 3 cm 3 . This scale is several times less than has been previously demonstrated for heterogeneously catalysed reduction using gaseous hydrogen and is more easily reproduced than small scale stirred vessels. Measurements have been made at a fixed total gas flow, with the effective mass transfer rate being adjustable by dilution of the hydrogen flow with either helium or nitrogen.
■ INTRODUCTIONDuring the early stages of chemical process development, the quantity of available starting material often restricts the scale on which development work can be conducted. This can be problematical in the case of gas−liquid reactions, in particular hydrogenation, where selectivity is often sensitive to the solution concentration of hydrogen and consequently to the relative rates of reaction and mass transfer. In these cases control of the volumetric mass transfer coefficient, k L a, is necessary to ensure that laboratory experimentation can properly simulate the processing conditions expected on the manufacturing scale. There are many examples of the sensitivity of hydrogenation processes to operating conditions. Sun et al. 1 first pointed out the interplay between hydrogen pressure, the volumetric mass transfer coefficient and the intrinsic chemical kinetics in determining the rate of a hydrogenation process and further pointed out that, in the case of parallel competing processes, relative rates and hence selectivities could be a function of these three variables. A range of examples confirms the generality of this principle with respect to olefin and ketone hydrogenation. 2−4 Merck workers also encountered the effect in the catalytic hydrogenation of an imine, in which some defluorination of an aryl fluoride occurred under "hydrogen starved" conditions, 5 and were able to devise satisfactory manufacturing conditions based on a knowledge of the volumetric mass transfer coefficient under operating conditions. In the hydro-dechlorination of a benzyl chloride, dimerization instead of reduction occurred under hydrogen starved conditions. 6 Hydrogen starvation is implicated in problems with the reduction of nitro compounds, where azo and azoxy byproducts can be formed, 7 and where leaching of metal from the catalyst support can occur. 8 Reduction of nitriles is extremely sensitive to the processing conditions, and formation of secondary 9 and tertiary amines via trapping of the intermediate imines with the first-formed primary amine is well-known, and avoidance of hydrogen starvation is one component of strategies used to achieve a good yield of primary amine products. 10 As a consequence of these considerations, it is now accepted in major pharma and agrochemical companies that "best practice" in the design and scale-up of hydrogenation processes using molecular hydrogen (as op...