TY - GEN
T1 - Deposition Properties of Biomass Fly Ash
AU - Laxminarayan, Y.
AU - Jensen, P. A.
AU - Wang, G.
AU - Wu, H.
AU - Sander, B.
AU - Frandsen, F. J.
AU - Glarborg, P.
PY - 2018
Y1 - 2018
N2 - This study investigated deposit formation of biomass fly ash on steel tubes, in a lab-scale Entrained Flow Reactor. Experiments were conducted using model biomass fly ash, prepared from mixtures of K2Si4O9, KCl, K2SO4, CaO, SiO2 and KOH, as well as three different boiler fly ashes: a wood fly ash, a straw fly ash, and a straw + wood cofired fly ash. The fly ashes were injected into the reactor, to form deposits on an air-cooled deposit probe, simulating deposit formation on superheater tubes in boilers. The results revealed that increasing flue gas temperature, probe surface temperature, time, fly ash flux and fly ash particle size increased the rate of deposit formation. However, increasing flue gas velocity resulted in a decrease in the deposit formation rate. A mechanistic model was developed for predicting deposit formation in the reactor. Inertial impaction was the primary mechanism of deposit formation, when pure K2Si4O9, SiO2 or CaO was injected into the reactor, forming deposits only on the upstream side of the steel tube. However, feeding KCl, K2SO4 or KOH into the reactor resulted in deposit formation on both sides of the steel tube, via condensation, thermophoresis, and inertial impaction
AB - This study investigated deposit formation of biomass fly ash on steel tubes, in a lab-scale Entrained Flow Reactor. Experiments were conducted using model biomass fly ash, prepared from mixtures of K2Si4O9, KCl, K2SO4, CaO, SiO2 and KOH, as well as three different boiler fly ashes: a wood fly ash, a straw fly ash, and a straw + wood cofired fly ash. The fly ashes were injected into the reactor, to form deposits on an air-cooled deposit probe, simulating deposit formation on superheater tubes in boilers. The results revealed that increasing flue gas temperature, probe surface temperature, time, fly ash flux and fly ash particle size increased the rate of deposit formation. However, increasing flue gas velocity resulted in a decrease in the deposit formation rate. A mechanistic model was developed for predicting deposit formation in the reactor. Inertial impaction was the primary mechanism of deposit formation, when pure K2Si4O9, SiO2 or CaO was injected into the reactor, forming deposits only on the upstream side of the steel tube. However, feeding KCl, K2SO4 or KOH into the reactor resulted in deposit formation on both sides of the steel tube, via condensation, thermophoresis, and inertial impaction
KW - Biomass
KW - Fly ash
KW - Deposit formation
KW - Fouling
KW - Ash sticking probability
KW - Entrained flow reactor
U2 - 10.5071/26thEUBCE2018-2AO.8.2
DO - 10.5071/26thEUBCE2018-2AO.8.2
M3 - Article in proceedings
VL - 2018
T3 - Proceedings of European Biomass Conference and Exhibition
SP - 440
EP - 452
BT - Proceedings of 26th European Biomass Conference and Exhibition
PB - ETA-Florence Renewable Energies
T2 - 26th European Biomass Conference and Exhibition (EUBCE 2018)
Y2 - 14 May 2018 through 17 May 2018
ER -