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50 g L−1 influent glucose at 1 d HRT.
38 g L−1 influent glucose and 22 g L−1 influent xylose at 1 d HRT.
The operating features of the experiments were as follows: REED-1: 50 g L−1 influent glucose at 1 d HRT REED-2: 38 g L−1 influent glucose and 22 g L−1 influent xylose at 1 d HRT REED-3: 54 g L−1 influent glucose and 34 g L−1 influent xylose at 1 d HRT REED-4: 54 g L−1 influent glucose and 34 g L−1 influent xylose at 2 d HRT.
Results obtained from REED-1 were directly comparable to the continuous experiment with 50 g L−1 influent glucose concentration (C-1, Table 3).
H2 production rates increased from 89 to 220 mL/h L of reactor when influent glucose concentrations were varied from 1.0 to 10.5 g/L.
Wheat straw hydrolysate contained 55 and 35 g L−1 glucose and xylose, respectively, so the results obtained were directly comparable to the results of the experiment REED-3 of the present study (with 54 and 34 g L−1 influent glucose and xylose, respectively).
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Although the reactors were operated in distinct variations in temperature (9 27°C) or influent wastewater (inorganic medium, glucose, or glutamate addition), these variations did not influence the inhibition of ANAMMOX bacteria in reactor.
The first (C-1) was fed with an influent of 50 g L−1 glucose, while the second (C-2) was fed with a mixture of glucose (38 g L−1) and xylose (22 g L−1).
Influent and effluent from each cycle were taken for glucose and pH measurement.
Optimization of influent factors showed that 2.5 and 1 g/l are the suitable concentrations of glucose and yeast extract, respectively.
Morphine and glucose.
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