Tall oil rosin acid, a forest product industry residue, has been converted
into a diesel fuel additive in a single step process. Fractionation of crud
e tall oil produces an excess of rosin acids. This material is an abundant,
inexpensive and chemically desirable feedstock. Two components, abietic ac
id and dehydroabietic acid, comprise about 70% of the rosin acid fraction o
f tall oil, The carboxylic acid functionality of these compounds must be re
moved and double bonds in the ring structure hydrogenated to obtain diesel
fuel additives. Hydrotreatment of the rosin acid fraction achieves both goa
ls. The experiments were performed in a laboratory-scale batch reactor usin
g three commercial sulfided Ni-Mo and Co-Mo catalysts. For each of the cata
lysts, three different factors were studied: temperature, hydrogen pressure
, and reaction time. Experiments probe the effects of these variables on li
quid product yield, cetane index, hydrogen-to-carbon ratio, and degree of c
racking. The liquid products, mainly saturated tricyclic ring compounds, we
re analyzed by elemental analysis (C, H, S, and O) and by GC-MS. Boiling po
int distributions and densities were also determined. From these data, ceta
ne indexes were calculated.