Journal
HOLZFORSCHUNG
Volume 69, Issue 6, Pages 751-760Publisher
WALTER DE GRUYTER GMBH
DOI: 10.1515/hf-2014-0254
Keywords
biorefinery; black liquor (BL); hydrogen production; phenolic compounds; supercritical water gasification (SCWG); thermodynamic calculation
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Funding
- Institut Carnot Energie du Futur
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Supercritical water gasification of weak sulfur-free black liquor (BL) was performed in a batch autoclave at temperatures between 430 degrees C and 470 degrees C, pressure between 24 and 27 MPa and residence time between 2 and 63 min. Results show that the gas produced was a mixture of mainly hydrogen, methane, and carbon dioxide. Maximum conversion was achieved at 470 degrees C and 60 min. Energy recovery (ER, ratio between the energy in the gas and in the initial BL) was 46%. Thirty-four percent of the carbon and 53% of the hydrogen initially present in BL were converted into gases. Nearly 15% of initial organic carbon remains in the liquid phase and consists mainly of phenolic compounds, which are stable under those conditions. A higher temperature is needed to convert all the organic carbon. Thermodynamic equilibrium should be reached at 700 degrees C leading to a complete conversion and a better efficiency. Sodium recovery is close to typical kraft recovery value and compatible with causticizing.
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