The addition of solvents
is an option for reducing the viscosity
of fast pyrolysis bio-oil and for slowing down the reaction rate of
aging reactions. For this purpose, conventional organic solvents with
low molecular mass are deployed, with alcohols in particular. They
can determine the costs and overall ecological performance of the
final product. In this context, the use of CO2, which is
a side product of pyrolysis, that occurs in the noncondensable pyrolysis
gas, can be a favorable option. However, CO2 has not been
used for conditioning of fast pyrolysis bio-oil so far. This work
is an evaluation of the influence that pressurized CO2 as
an agent has on the viscosity of fast pyrolysis bio-oil. The utilization
of CO2 can be an asset in the context of further processing
steps such as atomization, filtration, or transfer by pumping. The
results are compared to the effect of ethanol on the viscosity. It
was found that CO2 at 50 bar leads to a reduction of the
original viscosity by 70–80%, as does 5 wt % ethanol in fast
pyrolysis bio-oil. In the case of CO2 usage, there is an
approximately linear relationship between the relative viscosity and
CO2 pressure. Furthermore, the temperature dependence of
the relative viscosity change for pure fast pyrolysis bio-oil was
examined. It reveals Arrhenius-like behavior with a formal activation
energy of 66 kJ mol–1. The addition of CO2 (10 bar) reduces this value to 42 kJ mol–1, while
it remains almost unchanged upon the addition of 5 wt % ethanol. The
Vogel–Fulcher–Tammann equation was used to describe
the temperature dependence but showed no further advantage over the
Arrhenius-type equation.