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Approximately 120 L of warm (48°C to 50°C), 0.5 wt% H2SO4 was prepared beforehand in the recirculation tank.
Approximately 120 L of warm (48° to 50°C), 0.5 wt % H2SO4 solution was prepared in a recirculation tank.
Acid impregnation was carried out using 120 L of ~45 °C 0.5 wt% H2SO4 in a 200 L recirculation tank.
For control experiments, acid impregnation was carried out using 120 L of warm (40°C to 50°C) 0.5 wt% H2SO4 contained in a 200-L recirculation tank.
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Biogas production from stillage was included in all simulations of the integrated 1G + 2G plant, and was modelled as continuous recirculation tanks instead of stirred tank reactors.
The capital cost evaluation was updated to the first quarter of 2011, as were vendor quotations for the CHP plant, the filter press and the biogas recirculation tanks.
Finally, the concentration evolution in both feed tank and recirculation loop has been successfully modelled.
The semi-analytical solution is subsequently used to optimize the LNG storage tank and recirculation loop designs.
The recirculation system consisted of a fish tank, a sludge tank with membrane filtration treatment, and a hydroponic tank.
A Silverson 150/250MS rotor-stator was used in the recirculation loop of a stirred tank.
In particular, the overall removal could be increased even to 97% and 99%, at 60 and 120 min, respectively, when the recirculation point was the first tank.
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