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Stage II is the devolatilization stage, during which the main pyrolytic process occurs.
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Meanwhile, the interaction among the components during pyrolytic process was evidenced and briefly overviewed, in order to shorten the distance between the pyrolysis of biomass and pyrolytic behavior of its main components and design the new-concept co-pyrolysis process for promoting the production of oxygenated compounds.
The assay does not measure the yield of gas from the pyrolytic process, which can be substantial.
Kinetic and thermodynamic results will be useful input for the design of pyrolytic process using castor residue as feedstock.
The results of Fourier transform infrared (FTIR) spectroscopy to analyze the pyrolytic process indicated the complete combustion of peanut shells happened at 3 and 4 h at 400 °C.
Biochar materials were found to be highly hydrophobic (low H/C values) with high aromaticity, irrespective of biomass feedstock and pyrolytic process.
From the results, a comparative analysis was done for the biomasses, and a one-step global model was used to simulate the flash pyrolytic process and predict the yield of volatile products during pyrolysis.
This pyrolytic process was conducted, modeled and optimized using experimental design method when the process parameters, including temperature, time, particles size of tire rubber, the flow rate of inert gas (Ar), and amount of Fe2CuO4/rGO nanocomposite as the catalyst were controlled.
And in fact, the pyrolytic process is much closer to this mechanism than the solvothermal, most probably due to the low reaction time and violent conditions that are taking place inside the autoclave.
Apart from this, the reduction of voluminous waste biomass to produce biochar through pyrolytic process provides possible ways to solve the management and disposal of the waste biomass in an efficient manner.
In this stage, various volatile components are gradually released, resulting in a large weight loss and formation of the main pyrolytic products.
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