Hydrothermal gasification of biomass model compounds (cellulose and lignin alkali) and model mixtures

• Hydrothermal gasification of biomass model compounds were investigated.
• The effect of operating parameters on the product distribution was examined.
• Lignin suppresses hydrogen and methane formation.
• The highest gas yields were reached at 600 °C in the presence of K2CO3.

Biomass model compounds (cellulose and lignin alkali) and their mixtures were gasified at sub- and super-critical water conditions in the absence and presence of alkali catalyst (K2CO3). Hydrothermal gasification was performed in batch reactor at temperature range of 300–600 °C and pressure range of 90–410 bar with a reaction time of 1 h. Product yields of gaseous, aqueous and residue were investigated for model compounds (cellulose/lignin alkali) and their mixtures with weight ratios of 80/20, 60/40, 40/60 and 20/80 (wt./wt.). These mixtures were arranged to define the interaction between degradation products of model compounds of lignocellulosic biomass. In addition, gaseous and aqueous product compositions were identified to highlight prevailing reaction pathways during decomposition of model compounds. The highest hydrogen and methane yields were reached at 600 °C in the presence of K2CO3.

Effects of cellulose/lignin alkali weight ratio and alkali catalyst on gaseous product composition for hydrothermal gasification at 600 °C.Figure optionsDownload as PowerPoint slide