2014
DOI: 10.1016/j.powtec.2014.01.049
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Analysis of bed agglomeration during gasification of wheat straw in a bubbling fluidised bed gasifier using mullite as bed material

Abstract: The quantity and composition of the ash content of straw poses technical challenges to its thermal conversion and have been widely reported to cause severe ash sintering and bed agglomeration during fluidised bed gasification. Literature indicates that a combination of reactor design and bed material measures is required to avoid defluidisation at temperatures above 800 °C. Using scanning electron microscopy and energy dispersive X-ray spectroscopy this study investigated the initial agglomeration of a mullite… Show more

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Cited by 30 publications
(10 citation statements)
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“…Based on the different compound formations between combustion and gasification conditions, the oxidation state of the Fe oxides (Fe 2+ , Fe 3+ ) and formation of vivianite (Fe 3 (PO 4 ) 2 ) may be the dominating factor for the decreased IMT under gasification conditions. This case is important to consider since a large fraction of P in precipitated SS may be bound to Fe 2+ as vivianite [24], an important resource for P recovery [25].…”
Section: Melt Formationmentioning
confidence: 99%
“…Based on the different compound formations between combustion and gasification conditions, the oxidation state of the Fe oxides (Fe 2+ , Fe 3+ ) and formation of vivianite (Fe 3 (PO 4 ) 2 ) may be the dominating factor for the decreased IMT under gasification conditions. This case is important to consider since a large fraction of P in precipitated SS may be bound to Fe 2+ as vivianite [24], an important resource for P recovery [25].…”
Section: Melt Formationmentioning
confidence: 99%
“…In general, larger amount of ash provides larger amount of AAEM and thus more active sites will be provided for the catalytic gasification of the coal. However, for the silica or silica-contained ashes, the aggregation of ash particles could occur on the coal surface more easily so that the total active surface area of the coal sample was decreased, resulting in the decrease of its reactivity [51,52]. …”
Section: Effect Of the Biomass Ash Amount On The Gas Production Rate mentioning
confidence: 99%
“…The deposit formation involves a decrease in the heat exchanges as well as corrosion problems. The fluidized beds are sensible to bed material agglomeration, sintering and defluidisation, these problems may lead to total device failure [23]. A special care have to be taken when mixing WWS and waste, since their ash content can reach 30% mass fraction of dm to 40% mass fraction of dm [24,25].…”
Section: Introductionmentioning
confidence: 99%