1. Bio-carbon production by oxidation and hydrothermal carbonization of paper recycling black liquor
- Author
-
Andrew M. Gordon, Naresh V. Thevathasan, Ranjan Pradhan, Yi Wai Chiang, Animesh Dutta, and Zainab Al-Kaabi
- Subjects
Renewable Energy, Sustainability and the Environment ,Chemistry ,020209 energy ,Strategy and Management ,05 social sciences ,chemistry.chemical_element ,Sulfuric acid ,02 engineering and technology ,Building and Construction ,Raw material ,Pulp and paper industry ,Industrial and Manufacturing Engineering ,Industrial waste ,Paper recycling ,Hydrothermal carbonization ,chemistry.chemical_compound ,050501 criminology ,0202 electrical engineering, electronic engineering, information engineering ,Hydrogen peroxide ,Carbon ,Black liquor ,0505 law ,General Environmental Science - Abstract
Black liquor, an industrial waste, also generally called spent liquor is a promising feedstock for production of bio-carbon due to its high lignin and energy contents. Mild processing conditions and sustainable resource utilization can drive commercial utilization of this industrial waste. A novel oxidative procedure using hydrogen peroxide as a green liquid oxidant at room temperature for processing of paper recycling neutral sulphite semi-chemical spent liquor was established and evaluations were carried out for its efficiency. Standard hydrothermal carbonization was carried out for comparing bio-carbon production qualitatively and quantitatively using the same spent liquor. The oxidation procedure was performed at room temperature using 5% of H2O2 followed by washing in diluted sulfuric acid (0.15 N) while hydrothermal carbonization was performed at 250 °C. The bio-carbon produced were similar in terms of ash percentage and ranged from 1.25 ± 0.05 to 1.48 ± 0.05% for oxidation method and from 1.11 ± 0.03 to 1.45 ± 0.04% for hydrothermal carbonization. The carbon contents for the oxidation method ranged from 60.54 to 61.50% and 66.81–67.31% for hydrothermal carbonization while higher heating values ranged from 25.32 to 26.11 MJ/kg and from 28.68 to 29.34 MJ/kg respectively. The mass yield ranged from 29.98 to 31.88% by the oxidation, while it was 15.02–16.08% by hydrothermal carbonization.
- Published
- 2019
- Full Text
- View/download PDF