Controlling the selectivity to chemicals from catalytic depolymerization of kraft lignin with in-situ H2

Catalytic depolymerization of kraft lignin was successfully carried out in isopropanol/water mixture system over Rh/La 2 O 3 /CeO 2 -ZrO 2 catalyst at 373 °C for 2 h with Fe as reductant. The selectivity of in-situ H 2 was increasing from 67 wt% to 98 wt% by changing the proportion of isopropanol and water with metal Fe. A one-to-one correspondence was established between liquid products distribution and H 2 . It was an efficient method for predicting the composition of the liquid oil by H 2 selectivity detection or converting kraft lignin to desirable liquid products optionally, which administered to reduce the dependence on the specific catalysts. Other temperatures and catalysts were a viable option for the relationship.