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Biomass productivities per unit power input achieved in this reactor configuration (0.60 0.69 dry g W−1 day−1) were comparable to or better than those reported in the literature for different photobioreactor designs (0.10 0.51 dry g W−1 day−1).
The mass of the biosorbent (dry) (g).
In continuous mode, the maximum volumetric biomass productivity was 0.19 dry g L−1 day−1.
rho {text{s}}left( {frac{text{g}}{{ {text{cm}}3}}} right) = frac{text{Ms}}{text{Vb}}where ρs = soil bulk density (g cm−3), Ms = mass of soil after oven dry (g), Vb = bulk volume of the soil (cm−3).
In batch mode, a maximum volumetric biomass productivity of 0.085 dry g L−1 day−1 was achieved under sparging at a CO2-to-air ratio of 1%, and a maximum CO2 utilization efficiency of 33% was achieved at a CO2-to-air ratio of 0.25%.
To prepare water-insoluble materials, pretreated CS from both pretreatments was washed with distilled water at a ratio 1 dry g (input CS to pretreatment) to 50 mL of water.
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For the initial enrichment in each experiment, wetted switchgrass was inoculated with 10 wt % [g dry compost (g dry solid)−1] compost.
Hence, (4) Fiber fraction recovery % = Dry mass out g Dry mass in g ∗ 100%%, Liquid fraction recovery % = Amount in the filtrate g Dry mass in g ∗ 100%%.
After 3 weeks of storage, fresh feedstock was inoculated with 10 wt % [g dry stored sample (g dry solid)−1] of the stored community.
The plant yield was 12.5 g dry powder/50 g powdered leaf.
Dosage of SPEZYME® Xtra in liquefaction: 0.30 kg/ton dry solids g.
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