The objective of the present work is to obtain dry bio-oil, i.e.with very low water content, from the pyrolysis of Kraft lignin in order to generate a high value and stable feedstock for the possible production of phenols and fuel products. Kraft lignin is pyrolyzed in a modified bubbling fluidized bed equipped with an internal mechanical stirrer, and the resulting bio-oil vapors are fraction atedusing a three-condenser train to obtain a dry bio-oil. The effect of reactor temperature on the yield and characteristics of dry bio-oil will also be studied.