In this study, Oscillatoria sp. BTA-170 was grown in a photobioreactor for 15 days, yielding 3.1 g/L of biomass. During the composition analysis of biomass, the moisture, protein, carbohydrate, lipid, and ash contents were found to be 83.27, 6.36, 5.48, 3.79, and 1.1% on a wet basis (w.b), respectively. The tray drying properties of cyanobacterial biomass were investigated at temperatures of 40, 60, and 80 C with constant air velocity of 0.6 m/s. To reduce the moisture content of biomass from 83.27% to <10%, drying time required 2, 12, and 30 hr at 80, 60, and 40 C, respectively. The calculated effective moisture diffusivity of biomass was 5.10 Â 10 À9 , 6.34 Â 10 À8 , and 2.30 Â 10 À7 m 2 /s at 40, 60, and 80 C, respectively, and the activation energy was found to be 28.01, 31.04, and 33.27 kJ/mol at 40, 60, and 80 C, respectively. The logarithmic and Henderson and Pabis models showed the highest R 2 values of 0.997 and 0.996 at 80 C, respectively, and were thus employed to explain biomass drying characteristics. The drying constant value grew with increasing temperature, with the highest value obtained using the logarithmic model at 80 C being 0.523 (hr À1 ). The bulk density of biomass powder dried at 80 C was 598.21 kg/m 3 and the tapped density was 652.80 kg/m 3 , with Hausner ratio and Carr index of 1.091 and 8.363, respectively, showing that biomass powder had excellent flow qualities. The dried cyanobacterial biomass is a great source of protein, according to FTIR measurements. Similarly, after selecting four models based on the sorption isotherm, the GAB model was shown to be the best fit to represent the sorption behavior of Oscillatoria sp. BTA-170 powder.
Practical ApplicationsThe drying characteristics of Oscillatoria sp. BTA-170 biomass were evaluated using thin-layer drying models. The primary goal of drying biomass is to remove water from the solids to a point where microorganisms and degradation chemical processes are considerably reduced. The analysis of drying properties aids in the development of a cost-effective dryer. By hastening the manufacture of biomass powder, the effective design of the drying process helps to decrease time and processing costs. After the drying process, an FTIR analysis can be used to determine the presence of