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The higher concentration of H2 in solution in semi-continuous batch reactor tests with respect to batch reactor tests leads to a more relevant deactivation in Pd-SiO2 with respect to Pd-SBA-15, but a higher initial activity, due to the fact that H2 accelerates the reduction of the Pd species which are less reducible in Pd-SiO2 than in Pd-SBA-15.
With the emergence of (digital) computers at that item, iterative processing proved to be preferable with respect to batch processing as in the Wiener filter.
The fermenter productivity with 100 g/l of glucose concentration and oleyl alcohol or the mixture of oleyl alcohol and ethyl benzoate as extractant was increased 60% with respect to batch process (Roffler et al. 1987).
For traditional analysis of gene expression, experimental groups were balanced with respect to batch membership.
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Due to its countercurrent purification principle, the performance increase with respect to the batch process can be up to 10× in productivity and even more at higher yields.
With respect to discontinuous batch chromatography they have proven their ability to improve the process performance in terms of productivity, eluent consumption and product concentration especially for larger production rates.
With respect to (a) batch index b within sequence and (b) iteration index ℓ for b = 1.
In other studies, the productivity in extractive fermentation using fed-batch operation, without immobilization, a glucose concentration of 300 g/l and oleyl alcohol as extractant, increased 70% with respect to conventional batch process (Roffler et al. 1988).
Also in this case the higher fractions of solubilized biomass must be related to the better mass transfer regime obtained in the semi-continuous system with respect to the batch reactor.
Not only the productivity is enhanced by strongly reducing residence times with respect to the batch process (from hours to minutes or even seconds) but also a high degree of control over the resulting product characteristics (size, shape, crystalline phase) can be obtained by simply changing the composition of the gas used to create the slugs.
When the systems were compared at 50 g/L of nominal loading of biomass in water with 20 min of treatment time (Exp. 2FT and 2MW in Tables 4, 5), lower concentrations and yields of dissolved xylose and arabinose were obtained in the open system with respect to the batch reactor.
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