Alkali release was
studied in a 10 kW
th
chemical looping
pilot operated with a Linz–Donawitz (LD) slag oxygen carrier
(OC) and three biomass fuels. Experiments were performed at three
temperatures and in three operation modes: chemical looping combustion
(CLC), chemical looping gasification (CLG), and oxygen-carrier-aided
combustion (OCAC). Gas-phase alkali release was measured with a surface
ionization detector (SID). Fuel reactor (FR) gas-phase alkali emissions
increased with the temperature. This occurred as a result of increased
evaporation of KCl and enhanced decomposition of alkali salts during
char conversion. Air reactor (AR) alkali emissions were lower than
in the FR and independent of the operating temperature. In comparison
of operating modes, CLC and CLG modes resulted in similar gas-phase
alkali emissions due to the similar extent of char conversion. In
contrast, operation of the reactor system in OCAC mode resulted in
significantly lower levels of gas-phase alkalis. The difference in
alkali emission was attributed to the steam-rich atmosphere of CLC.
The effect of steam was further investigated in CLC and OCAC tests.
Lowering steam concentrations in CLC operation resulted in lower gas-phase
alkali emissions, while introducing steam to the FR during OCAC operation
resulted in higher alkali emissions. It was concluded that steam likely
enhances gas-phase K release through a reaction of K
2
CO
3
within the fuel char with steam to produce KOH(g). Solid
sampling and analysis for K content was used along with SID measurements
to develop a K mass balance for the reactor system. Mass balance results
for the straw pellet fuel tests showed that LD slag OC absorbs approximately
15–51% of fuel K, 2.2% of fuel K is released to the gas phase,
and up to 3.4% of fuel K is captured in the AR fly ash. The residual
40–80% of fuel K was determined to leave the FR as K-rich fly
ash.