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The optimized response (at pH 7.0) had a sensitivity of 661.0 μA mM−1 cm−2 and a limit of detection (3 × S/N) of 0.1 μM.
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The turn-over-frequency (TOF) of the optimized responses demonstrated a slightly higher value than the one which was not optimized.
The operating conditions that set the optimized responses not always coincide with the most stable process.
The optimized responses were determined to be R = 87.37% and qe = 24.74 mg g−1.
The optimized responses are chip compression ratio (Kh), effective shear angle (βeff), friction coefficient at the tool rake surface and the chip-tool interface temperature.
The crystal phases purity and the mass of powder batch were the optimized responses of the powder synthesis and the concentration of calcium ions and volume of ammonium hydroxide were the experimental variables.
The process variables studied were: initial metal ion concentration and spatial time, and the optimized responses were: adsorption capacity of the bed (Qmax), efficiency of the adsorption process (EAP), and effective use of the bed (H).
The optimized responses for Ni and Cr rejection and pure water flux were 87.093, 83.271 and 71.801 (Lit m−2 h−1) respectively at optimum membrane formulations of PAN: 23.93%, PEG: 0.41% and TiO2: 0.82%.
The two optimized responses are the sensitivity and the 97th quantile of the positioning error.
Furthermore, the equalized maximum likelihood (EML) receiver is proposed, and its performance is improved because of the optimized target response.
A parametric analysis investigated the optimized system response to the variation of total tunnel volume, inlet water temperature, production rate, pipe diameter and insulation layer thickness, from the energetic point of view.
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