A simple heat transfer model is utilized to determine the heat transfer coefficients for multiple tubes immersed in an industrial fluidized bed reactor supporting an exothermic reaction. From the temperatures at their outlets, superheating occurs in some blocks of tubes, but not in others. A four-zone heat transfer model is then used to evaluate the axial and lateral temperature differences due to the existence of a bottom un-cooled entrance zone and two cooled zones, corresponding to the regions where superheating does and does not occur
Heat transfer between particle-fluid media and solid surfaces has wide applications in industries su...
Suspension-to-wall heat transfer in circulating fluidized beds is modeled considering both the reac...
A hypothetical core-disruptive accident (HCDA) in a liquid metal fast breeder reactor (LMFBR) may re...
The heat transfer from a fluidized bed to the cooling jacket of the vessel has been studied for vari...
Graduation date: 1964Local and average heat transfer coefficients for heat transfer\ud from internal...
© Published under licence by IOP Publishing Ltd. A numerical study of the fluidized bed apparatus in...
The adequate modeling of industrial packed bed catalytic reactors with low tube to particle diameter...
The heat transfer coefficients for horizontally immersed tubes have been studied in model internally...
There have been few studies modelling both flow and heat transfer in fluidised beds. The kinetic the...
A compartment/population balance model is presented for describing heat transfer in gas-solid fluidi...
In this paper experimental and numerical investigations on heat transfer within a bubbling fluidized...
Heat transfer to single particles in the transport zone of circulating fluidized beds and heat trans...
A method is proposed for predicting heat transfer coefficients in hot fluidized-bed combustors by tr...
In the present work, the multiphase flow dynamics in fluidized beds is modelled using the Two-Fluid ...
While providing a fast and accurate tool of simulating fluidized beds, the major limitation of class...
Heat transfer between particle-fluid media and solid surfaces has wide applications in industries su...
Suspension-to-wall heat transfer in circulating fluidized beds is modeled considering both the reac...
A hypothetical core-disruptive accident (HCDA) in a liquid metal fast breeder reactor (LMFBR) may re...
The heat transfer from a fluidized bed to the cooling jacket of the vessel has been studied for vari...
Graduation date: 1964Local and average heat transfer coefficients for heat transfer\ud from internal...
© Published under licence by IOP Publishing Ltd. A numerical study of the fluidized bed apparatus in...
The adequate modeling of industrial packed bed catalytic reactors with low tube to particle diameter...
The heat transfer coefficients for horizontally immersed tubes have been studied in model internally...
There have been few studies modelling both flow and heat transfer in fluidised beds. The kinetic the...
A compartment/population balance model is presented for describing heat transfer in gas-solid fluidi...
In this paper experimental and numerical investigations on heat transfer within a bubbling fluidized...
Heat transfer to single particles in the transport zone of circulating fluidized beds and heat trans...
A method is proposed for predicting heat transfer coefficients in hot fluidized-bed combustors by tr...
In the present work, the multiphase flow dynamics in fluidized beds is modelled using the Two-Fluid ...
While providing a fast and accurate tool of simulating fluidized beds, the major limitation of class...
Heat transfer between particle-fluid media and solid surfaces has wide applications in industries su...
Suspension-to-wall heat transfer in circulating fluidized beds is modeled considering both the reac...
A hypothetical core-disruptive accident (HCDA) in a liquid metal fast breeder reactor (LMFBR) may re...