Diniz Filho, Paulo Tasso [UNESP]Silveira, Jose Luz [UNESP]Tuna, Celso Eduardo [UNESP]Lamas, Wendell de Queiroz [UNESP]2014-05-272014-05-272013-05-14Applied Thermal Engineering, v. 57, n. 1-2, p. 116-124, 2013.1359-4311http://hdl.handle.net/11449/75395This work aims to study the thermodynamic, ecological and fluid-dynamic aspects of a circulating fluidized bed gasifier using sugar cane bagasse as biomass, in order to estimate a model of its normal operation. In the initial stage was analysed the composition of biomass selected (sugar cane bagasse) and its lower heating value (LHV) was calculated. The energy balance of the gasifier was done, being the volumetric flow of air, synthesis gas and biomass estimated. Also the power produced by this gasifier was theoretically estimated. Then the circulating fluidized bed gasifier was designed for operation with approximately 100 kg/h of processed biomass. Cross-sectional area of the reactor, feeder size, diameter of the exit zone of the gases and minimum height of the expanded bed were selected. Some bed gasifier hydrodynamic factors were also studied. The minimum fluidization velocity, fluidization terminal velocity, and average fluidizing velocity were calculated, in order to understand the fluid-dynamic behaviour of gasification of this fuel. It was obtained a theoretical model that can support a possible prototype of circulating fluidized bed gasifier biomass. Finally, there were studied the ecological aspects of the gasifier, through an overall methodology. Ecological efficiencies were estimated for two scenarios: first considering the carbon cycle and thereafter disregarding the carbon cycle. In both cases, it can be proved the ecological viability of the project. © 2013 Elsevier Ltd. All rights reserved.116-124engBiomass gasificationFluidized bed gasifier modelingSugar and alcohol industryAlcohol industryBiomass GasificationCirculating fluidized bed gasifierCross sectional areaEcological efficiencyFluid-dynamic analysisFluidized bed gasifiersMinimum fluidization velocityBiomassCarbonChemical industryEcologyFluid dynamicsFluidizationFluidized bedsSynthesis gasGasificationArtigo10.1016/j.applthermaleng.2013.01.045WOS:000320976500015Acesso restrito2-s2.0-8487735335117501542673055309535897335897207