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The biogas potential was measured in batch trials for several stillage streams and for the pentose-rich stream after filtration of the pretreated material (data not shown).
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Methane production was determined in laboratory-scale batch trials.
Table 1 Example saline aquifer parameters Parameter Value Parameter Value Parameter Value Common parameters NaClaquifer 5 g L−1 NaCl product water 2.5 g L−1 N G 90% Φ 50% S w 70% T h 1 m A r 100 m3 d−1 P w (Catalyst A) 0.030 t m−3 P w (Catalyst B, 2015) 0.0005 t m−3 1st Quartile Median 3rd Quartile Catalyst A Position in 2015 as demonstrated by batch trials (0.2 to 10L·batch-1)- Fig. 2-7,12.
For the batch trials, 0.2 g of each adsorbent was placed in contact with 50 mL of 1 × 10−3 M Cr VI) solution in the plastic-sealed beaker.
The third laboratory trial was carried out in nitrogen starvation in batch conditions; the trial was started by inoculating the alga in the growth medium deprived of nitrogen.
The use of the catalytic bed reactor has given the possibility to perform the transesterification maintaining the catalyst separated from the reactants, without loss of efficiency; in fact the comparison between trials in batch reactor and in catalytic bed system has not shown differences in yields.
The first trials in the GWP-II (Table 10, trial 7), in batch regime, were performed in July - August, to test growth at high temperatures on the isolation medium of each strain or in parallel in BG11 and F medium; cooling was not activated.
To simulate the conditions of gravitational stabilization of particulate materials in the presence of polymers, in this investigation batch settling trials were carried out for prolonged durations with the model colloidal alumina and polyacrylic acid (PAA) flocculants of different molecular weights.
The first trial was performed in batch regime while the second in semi-continuous regime (30% of the culture volume was harvested daily and replaced with fresh medium).
The CHN analyses of granules from these dried samples and those of batches used in the pot trials were then carried out using the method described above.
The CaO-based WTR demonstrated effective removal of DOC and P in column trials, and a high capacity for P sorption in batch experiments.
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