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The MSDTIRC-PV structure is capable of providing a maximum power concentration of 4.2× when compared to a similar cell without the concentrator.
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In terms of oxytetracycline hydrochloride concentration, the maximum power density firstly enhanced when oxytetracycline hydrochloride concentration increased to 0.5 mmol/L, then dropped dramatically with further increasing of oxytetracycline hydrochloride concentration to 2.0 mmol/L.
For the electrolyte concentration, the maximum power density and STH and FF all increases with increasing the electrolyte concentration.
The actual lowest CO concentration and maximum power density based on the reactor volume were 90 ppm and 0.8 kW/L, respectively.
It was found that the cell performance was substantially improved with an increase in methanol concentration; a maximum power density of 20 mwasm2 wachievedved with 5.0 M methanol solution.
At 10 mM glucose-6-phosphate (G6P) as a substrate concentration, the maximum power density of 0.06 mW cm−2 and retaining 42% of power output after 11 days were obtained through the method of chemical cross-linking with carbon nanotubes, approximately 6-fold and 3.5-fold better than those of the electrostatic force-based method, respectively.
Results demonstrated that at dye concentration of 112.5 mg/L, maximum power density of 27.5 mwas2 wachievedved.
Maximum of 0.631 V open circuit potential for 100 mg/L Cu2+ concentration was obtained and accordingly, maximum power density was 835.21 ± 1.40 mW/m3 for rGO/PPy along with 82.8% Cu2+ removal as compare to 79.9% for rC60/PPy modified MFC.
Power density as a function of wastewater concentration was modeled according to saturation kinetics, with a maximum power density of Pmax = 164 mW/m2 (fixed 100 Ω resistor) and half-saturation concentration of Ks = 259 mg/l.
At a concentration of 3000 mg-COD/L, the maximum power density achieved was 175 mW/m2.
Single cells with active area of 6 cm2 showed a maximum power density of 40 mW/cm2 at 4 M of methanol concentration at room temperature.
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