Defluidization in fluidized bed gasifiers using high-alkali content fuels. (August 2016)

• Record Type: Journal Article
• Authors: Narayan, Vikas; Jensen, Peter Arendt; Henriksen, Ulrik Birk; Glarborg, Peter; Lin, Weigang; Nielsen, Rasmus Glar
• Is Part Of: Biomass and bioenergy. Volume 91(2016:Aug.)
• Page Start: 160
• Page End: 174
• Publication Date: 2016-08
• Subjects: De-fluidization -- Alkali -- Agglomerate -- Biomass -- Gasification; Biomass energy -- Periodicals; Biomass -- Periodicals; Energy-Generating Resources -- Periodicals; Bioénergie -- Périodiques; 333.9539
• DOI: 10.1016/j.biombioe.2016.05.009
• Languages: English
• ISSNs: 0961-9534

Abstract

Abstract: A major concern in thermal conversion of biomass encountered in fluidized beds is bed agglomeration, which may result in de-fluidization, leading to unscheduled downtime and additional costs. Biomass fuels, especially herbaceous plants, often contain significant amounts of silicon, potassium and calcium, which may form viscous melts that adhere on the surface of the colliding bed particles and bind them to form agglomerates. In this paper, studies were made to understand the behavior of inorganic elements (mainly K, Si and Ca) on agglomeration and de-fluidization of alkali rich bed-material samples under non-oxidizing conditions in a bench-scale fluidized bed reactor set up. The de-fluidization studies involved measurements with sand and pure potassium salts (KCl and K2 CO3 ) as well as with bed material samples obtained from a 6 MW Low Temperature Circulating Fluidized Bed (LTCFB) gasifier using straw as a fuel. It was seen that in sand + KCl agglomerates, the sand particles were bound by KCl melts. Only very limited chemical reaction was observed between KCl and the sand particles and no presence of silicate melts in the agglomerates. For sand + K2 CO3 mixtures and for LTCFB bed material samples, agglomeration could be attributed to viscous silicate melts formed from reaction of inorganic alkaline and alkali earth species with silica from the bed particles. A mathematical model that addresses the de-fluidization behavior of alkali-rich samples was developed based on the experiments performed in the bench-scale fluidized bed reactor as well as on results from literature. The model was then used to predict the de-fluidization behavior of alkali-rich bed material in a large-scale LTCFB gasifier. Highlights: Effect of fuel K, Ca and Si on de-fluidization has been quantified. K addition by KCl or K2 CO3 leads to different de-fluidization mechanisms. Presence of Ca and Mg increased de-fluidization temperatures of bed material. A model for de-fluidization of alkali-rich bed materials was developed. The model predicts de-fluidization temperatures of experiments with reasonable precision.