The lower and upper whiskers illustrate minimum and maximum yields, respectively and the median yield separates the box into upper and lower quartiles.
Leaf analyses for N, P and K, related with maximum yield, were respectively, 15 18, 1.8 2.2 and 15 20 g kg−1, for samples taken from fruit bearing terminals.
Thus, both the fresh feed and cycle oil can react over regenerated catalyst with high activity and under the most favorable conditions for maximum light oil yield, respectively.
The response surface methodology was used to determine the optimum value of the operating variables for maximum conversion as well as maximum yield of OLP and gasoline fraction, respectively.
The overall yield and productivity were 0.195 g/g and 0.143 g/L/h, respectively, while the maximum yield and productivity were 0.270 g/g and 0.253 g/L/h during the lipid accumulation phase of the fermentation.
The particle size range, sweep gas flow rate and operating temperature were optimized as 0.5 mm–0.99 mm, 8 L/min and 450 °C respectively for obtaining maximum yield of bio-oil (48%) and bio-char (35.1%).
Under these optimized conditions, the maximum yield and the product e.e. wer 97.7%and>99%9%, respectively, which are much higher than the corresponding values previously reported.
The maximum ethanol concentration and yield were 17.9 g/L and 53% yield, respectively, after 120 hours.
After 120 h, the maximum bioethanol concentration and yield were 17.9 g/L and 53% yield, respectively.
And maximum yield of cellulase and xylanase were obtained 437.54 U/gds and 273.83 U/gds, respectively at 30 °C and pH 6.0 after 5 days of incubation.
