Agglomeration behaviour of high ash Indian coals in fluidized bed gasification pilot plant

Abstract Although gasification of high ash Indian coals is gaining importance, the resultant uncertainties associated with agglomerate formation are still unresolved. To address this, a suitable pilot scale Fluidized Bed Gasifier was utilized in this study. Stabilized operating conditions in terms of coal feed rate, air feed rate, bed temperature, etc., already identified for maximum possible carbon conversion, were maintained in all experiments and the steam flow rate was only varied. Though the ash fusion temperature of the coals were above 1200 °C, agglomerate was formed during gasification at 950 °C with ‘steam to coal ratio’ less than 0.15 (kg/kg). On increasing this ratio above 0.2 local heat-concentration and agglomeration could be avoided with certainty. Chemical composition alone was not sufficient to explain the relative strength of ash-agglomerates. Compositional variation and state of iron within the matrix were assessed through SEM-EDX and electron paramagnetic resonance (EPR) study, respectively. The probing also required the ash-loading and iron-loading factors to be freshly defined in the context of gasification. Localized heat, large compositional variation, presence of iron in Fe 2+ state, ash-loading/iron-loading factors influenced intensity of agglomerate formation. Finally, low temperature agglomerate formation was explained by SiO 2 –Al 2 O 3 –FeO phase diagram.

[1]  A. Rao,et al.  Experimental determination of bed agglomeration tendencies of some common agricultural residues in fluidized bed combustion and gasification , 1998 .

[2]  Bryan M. Jenkins,et al.  Bed agglomeration in fluidized combustor fueled by wood and rice straw blends , 2010 .

[3]  A. Lyngfelt,et al.  Ash behaviour in a CFB boiler during combustion of coal, peat or wood , 1998 .

[4]  Kim Dam-Johansen,et al.  Agglomeration in bio-fuel fired fluidized bed combustors , 2003 .

[5]  Hari B. Vuthaluru,et al.  Effect of coal blending on particle agglomeration and defluidisation during spouted-bed combustion of low-rank coals , 2001 .

[6]  John F. Unsworth,et al.  Coal Quality and Combustion Performance: An International Perspective , 1991 .

[7]  M. Llorente,et al.  Comparing methods for predicting the sintering of biomass ash in combustion , 2005 .

[8]  Mikko Hupa,et al.  The ash chemistry in fluidised bed gasification of biomass fuels. Part I: predicting the chemistry of melting ashes and ash–bed material interaction , 2001 .

[9]  B. Kulkarni,et al.  Development of data-driven models for fluidized-bed coal gasification process , 2012 .

[10]  Carlos F. Valdés,et al.  Co-gasification of Colombian coal and biomass in fluidized bed: An experimental study , 2009 .

[11]  B. Moghtaderi,et al.  The sintering temperature of ash, agglomeration, and defluidisation in a bench scale PFBC , 2005 .

[12]  Sanjay M. Mahajani,et al.  Underground coal gasification: A new clean coal utilization technique for India , 2007 .

[13]  Ravi Kumar,et al.  A Novel tool for assessing slagging propensity of coals in PF boilers , 2008 .

[14]  E. Kakaras,et al.  Agglomeration in fluidised bed gasification of biomass , 2008 .

[15]  J. C. V. Dyk Understanding the influence of acidic components (Si, Al, and Ti) on ash flow temperature of South African coal sources , 2006 .

[16]  Anders Nordin,et al.  Mechanisms of Bed Agglomeration during Fluidized-Bed Combustion of Biomass Fuels , 2005 .

[17]  Matti Hiltunen,et al.  Sintering mechanisms of FBC ashes , 1994 .