Hydrothermal liquefaction (HTL) of Kraft lignin was investigated with different salt catalysts (namely, the basic salts K₂CO₃, CaCO₃; acidic salts ZrOCl₂·8H₂O and AlK(SO₄)₂·12H₂O, and neutral salt KCl) in the temperature range of 200–350 °C for 40 min in a batch reactor. With an increase in reaction temperature from 200 to 350 °C, the bio-oil yield first increased up to 300 °C and then decreased at 350 °C. The highest total bio-oil yield of ∼48.5 wt %, which involved ∼7.5 wt % water-soluble organics (WSO) and lowest char formation (∼19.1 wt %), was obtained at 300 °C over K₂CO₃ catalyst. The GC-MS results showed that WSO fractions were comprised of mainly guaiacol and catechol-type monomers, whereas the heavy bio-oil fractions contained mostly long-chain acids, aldehydes, and ketone-type compounds. In comparison with the other salt catalysts, the insertion of K₂CO₃ resulted in significant reduction in oxygen, nitrogen, and sulfur contents and consequently increased the high heating value (HHV) of 18.9 MJ/kg (in the original Kraft lignin) to 29.3 MJ/kg (in the bio-oil obtained with K₂CO₃ catalyst). The overall results suggested that K₂CO₃ in a subcritical water system was more efficient for the production of high-quality bio-oil in comparison to other tested acidic and neutral salt catalysts. The solid and liquid products obtained in different experiments were analyzed by FT-IR, SEM, GC-MS, and elemental analysis methods.
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