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All fermentation parameters (except biomass concentration) were strongly affected by the interactions among the operation variables.
As their measure, the relative enhancement factor Er involving the operation variables was introduced for the first time.
The operation variables such as the working gas, the frequency and the mean pressure are specially considered.
Steady state relation between the cost related variables and the operation variables are approximated through response surface models.
Besides the operation variables for batch reactors, this method can also suggest the optimum mixing pattern and promising reactor configurations for mechanical design.
The operation variables studied were temperature (400 800 °C), the initial sample mass (2.5 10 g of tomato plant waste) and the particle size (0.63 2.00 mm).
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It was shown that different polymer architectures could be obtained varying these operation variables, opening the possibility of fine tuning the polymer characteristics.
The influence of the main operation variables, i.e., milk concentration (2.5 10 wt.%) and current density (100 400 A m−2), has been analysed.
The investigated operation variables presented different influences on the H2 production under fluidized bed conditions from those obtained in thermodynamic equilibrium analysis or fixed bed experiments.
The device operation variables are also directly related to the defibrillatory shocks.
All data were based on bibliographical search, where the raw material was bean coffee (Arabian from Brazil), the roasting operation variables were 200 °C of temperature and 12 min. of roasting time and the rest of the bibliography data were all the necessary tools to develop all tensors (relationship between components, phases and aggregation state).
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