Economic and environmental considerations of fossil fuel use, such as its shortage and impact on the air quality,
as well as contribution to the climate change process, has lead to the necessity to develop biomass-based energy supply
systems. Biomass is a renewable resource, which is an alternative for the fossil fuel. However, use of solid biomass is limited
by the applicable technologies – it is not possible to use it in gas turbines or internal combustion engines, which are applied
for the efficient combined heat and power generation. Therefore, biomass gasification is considered as a means of perspective
energy conversion. In gasification, the intrinsic chemical energy of solid biomass is converted into the energy of combustible
gas that can be used in gas-consuming engines. Tar is a by-product of gasification; it mainly consists of organic substances
heavier than benzene and leads to clogging of pipes and downstream equipment because of its condensation on the inner
surfaces. Determination of tar mass concentration and composition depending on the gasifier operational mode is the first
step for process optimization aiming to get the maximal yield of useful syngas. An industrial experiment is examined in the
paper, the gasifier model is compared with the results of practical measurements, and the method for tar determination is
tested? on a real object. The predicted tar value in the model was 58 g/mn3, practical measurements showed that gravimetric
tar mass concentration is in the range of 0.54…5.64 g/mn3.