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Optimal operating policy choice is based on the minimum amount of required P2Ox that ensures an imposed reaction conversion and maximum reactor productivity under various technological constraints, and for catalase/P2Ox ratios of 200 300 U/U.
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The enhanced biomass in broth and adsorbed bacteria was apparently another reason for butanol production improvement because high cell concentrations resulted in high reactor productivity [ 20].
Thus the catalyst inventory and reactor productivity are strongly increased.
However, operating the reactor with a large excess of one reactant lowers the reactor productivity.
Increased thermal management allows maximum reactor temperatures above 1400°C.
To understand this behavior better, we look at the maximum reactor temperature, presented in Fig. 15.
Fixed criteria are used for reactor conversion, maximum reactor temperature, and pressure drop.
Increasing reactor productivity through application of high-density cell concentration reduces downstream harvesting costs.
According to the reports the sludge density 52 55% [ 88] showed the maximum reactor performance.
Subsequently, the ethanol productions and the reactor productivities of batch fermentation and immobilized cells were compared.
To achieve the desired reactor productivities, a highly active cobalt catalyst is needed.
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