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The process is evaluated taking as response variable the surface roughness.
A tubular photobioreactor (PBR) and urea as cheap nitrogen source were used, taking as response variables kinetic parameters and biomass composition.
Firstly, an experiment is carried out according to a central composite design for the factors percentage of methanol and pH of the carrier solution, taking as response of the design the net analyte signal (NAS) for each analyte.
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Colour strength, weight loss percentage and back staining values were taken as response factors.
Parameters specified by the European standard UNE-EN 14214 were taken as response variables.
The ratio between absorbance and the time required to break the emulsions was taken as response.
All experiments were performed in triplicate and the averages of total alkaloid content were taken as response.
All experiments were carried out in triplicate and the average of the phytase activity was taken as response (Table 2).
acid concentration, residence time and additive concentration on iron leaching (taken as response) were studied to obtain a statistical model.
Six input parameters have been investigated, two of FDM and four of VS processes while surface roughness and hardness of ABS part is taken as response.
Peak current, gap voltage, pulse on time and dielectric fluid pressure was taken as input control parameter while material removal rate and surface roughness were taken as response parameters.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com