Biomass
gasification produces a wide range of species, from permanent gases
to condensable hydrocarbons, with different composition and boiling
points. This complicates the mass balance of the system, as multiple
techniques are needed to quantify the various components of the produced
raw gas. In this study, a high-temperature reactor for thermal conversion
of raw gas at 1700 °C was developed to generate a gas stream
that consisted primarily of CO, CO2, H2, and
H2O. The reactor was experimentally evaluated and subsequently
used for measurements of the raw gas from the Chalmers 2-4–MW
dual fluidized bed gasifier. The gas stream that exits the reactor
is analyzed to obtain the total elemental flows of C, H, O, and N,
which facilitate determinations of the fuel conversion and oxygen
transport in a dual fluidized bed reactor. The proposed system was
operated in parallel with a gas-cleaning system, to determine the
yield of condensable species, including tar and GC-undetectable species.
A simplified approach is proposed for quantifying the average energy
content of the condensable species, thereby allowing the wet raw gas
efficiency and lower heating value (LHV) to be calculated.