Abstract
One-pot deoxygenation of kraft lignin to aromatics and hydrocarbons of fuel-range quality is a promising way to improve its added value. Since most of the commercially resourced kraft lignins are impure (Na, S, K, Ca, etc., present as impurities), the effect of these impurities on the deoxygenation activity of a catalyst is critical and was scrutinized in this study using a NiMoS/Al2O3 catalyst. The removal of impurities from the lignin indicated that they obstructed the depolymerization. In addition, they deposited on the catalyst during depolymerization, of which the major element was the alkali metal Na which existed in kraft lignin as Na2S and single-site ionic Na+. Conditional experiments have shown that at lower loadings of impurities on the catalyst, their promotor effect was prevalent, and at their higher loadings, a poisoning effect. The number of moles of impurities, their strength, and the synergism among the impurity elements on the catalyst were the major critical factors responsible for the catalyst’s deactivation. The promotor effects of deposited impurities on the catalyst, however, could counteract the negative effects of impurities on the depolymerization.
Highlights
Lignin valorization can improve the economic viability of a lignocellulosic biorefinery
The elemental analysis of the catalyst after its 2nd recycle (i.e., 3rd run) showed a significant amount of Na (357 ppm), K (180 ppm), Ca (180 ppm), and Fe (183 ppm) (Table 2) on it. This confirms that the impurities of kraft lignin were deposited on the catalyst during the depolymerization changing its composition
This study indicates that the number of moles of impurity elements on the lignin is important apart from their amount in deactivating the catalyst
Summary
Lignin valorization can improve the economic viability of a lignocellulosic biorefinery. The performance of a typical HDO catalyst, such as NiMoS/Al2O3, in consecutive kraft lignin HDO runs, especially after its thermal regeneration, to investigate the deposition of impurities from the lignin to the catalyst, and the role of these impurities on the catalytic activity has, to our knowledge, not been studied. This was the objective of the current study. The effect of these inorganic impurity elements of kraft lignin on the deoxygenation activity of a NiMoS/Al2O3 catalyst during subsequent runs is reported. The product yield obtained over the pretreated lignin was compared with the untreated lignin to reveal the benefits of the pretreatment
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