A heat balance over the fluid-dynamic boundary layer of a circulating fluidized bed furnace has been formullated in order to calculate the heat transfer to the walls. The convective heat transfer is related to a horizontal particle flow from the core to the wall region, and an additive radiative heat transfer constituent is calculated for the particulate medium. An empirical description of the vertical distribution of solids and the transversal temperature profile are needed for the evaluation. The calculated heat transfer coefficients were compared with measurements in three commercial boilers and the deviation was less than 40%, which is in the same order as the uncertainty of the experimental data
Four different experimental methods have been used for the estimation of the bed-to-membranewall hea...
The characteristic features of heat transfer in circulating fluidized bed boilers are described. Fir...
Suspension-to-wall heat transfer in circulating fluidized beds is modeled considering both the reac...
A heat balance over the fluid-dynamic boundary layer of a circulating fluidized bed furnace hasbeen ...
Heat transfer to single particles in the transport zone of circulating fluidized beds and heat trans...
Conditions of significance for heat transfer in circulating fluidized bed boilers, such as the shap ...
Intensity of heat transfer to screen surfaces in the furnaces with a circulating fluidized bed (CFB)...
Three methods of estimating Ihe effective emissivily of a gas-particle suspension are eoml~ared and ...
A considerable amount of work, mostly measurements, has been dedicated to heat transfer in circulati...
A 3-dimensional model for the heat transfer in the furnace of a fluidized bed boiler is presented. T...
The heat transfer coefficient was measured with dark (steel) and light (silver) spherical probes, 5-...
The aim of this work is to find a method for translation of heat transfer data from cold laboratory ...
Heat transfer to wall panels in the furnace of a circulating fluidized bed (CFB) is investigated by ...
The heat and mass balance of the bottom region of a fluidized bed boiler burning biomass is establis...
The heat balance of different circulating fluidized bed boiler designs is investigated for variation...
Four different experimental methods have been used for the estimation of the bed-to-membranewall hea...
The characteristic features of heat transfer in circulating fluidized bed boilers are described. Fir...
Suspension-to-wall heat transfer in circulating fluidized beds is modeled considering both the reac...
A heat balance over the fluid-dynamic boundary layer of a circulating fluidized bed furnace hasbeen ...
Heat transfer to single particles in the transport zone of circulating fluidized beds and heat trans...
Conditions of significance for heat transfer in circulating fluidized bed boilers, such as the shap ...
Intensity of heat transfer to screen surfaces in the furnaces with a circulating fluidized bed (CFB)...
Three methods of estimating Ihe effective emissivily of a gas-particle suspension are eoml~ared and ...
A considerable amount of work, mostly measurements, has been dedicated to heat transfer in circulati...
A 3-dimensional model for the heat transfer in the furnace of a fluidized bed boiler is presented. T...
The heat transfer coefficient was measured with dark (steel) and light (silver) spherical probes, 5-...
The aim of this work is to find a method for translation of heat transfer data from cold laboratory ...
Heat transfer to wall panels in the furnace of a circulating fluidized bed (CFB) is investigated by ...
The heat and mass balance of the bottom region of a fluidized bed boiler burning biomass is establis...
The heat balance of different circulating fluidized bed boiler designs is investigated for variation...
Four different experimental methods have been used for the estimation of the bed-to-membranewall hea...
The characteristic features of heat transfer in circulating fluidized bed boilers are described. Fir...
Suspension-to-wall heat transfer in circulating fluidized beds is modeled considering both the reac...