Add to ORKGThis work investigates the lateral mixing process of fuel in a cold flow model of a fluidized-bed gasification chamber in an indirect gasification system. The bed has a significant cross-flow of bulk solids and the fuel mixing is investigated with respect to how operational conditions (fluidization velocity and solids circulation rate) and the fuel-feed location influence the fuel residence time in the gasification chamber. Fluidization velocity and fuel feeding location are found to influence fuel residence time the most, whereas solids circulation rate has no significant effect at the conditions tested
The aim of this thesis was to improve the fuel conversion in Chalmers bubbling fluidized bed (BFB) g...
A 1-dimensional model is used to analyse how solids material circulation, biomass reactivity and gas...
A Monte Carlo model was proposed to characterize the fuel particles motion in a large-scale fluidize...
This work investigates the lateral mixing process of fuel in a cold flow model of a fluidized-bed ga...
This work investigates the lateral mixing process of fuel in a cold flow model of a fluidized-bed ga...
This work investigates the lateral fuel mixing in fluidized beds with a crossflow of solids by means...
Operational conditions, such as the fluidization velocity or the solids cross-flow, have been found ...
For solid fuels, thermochemical conversion processes such as combustion and gasification are especia...
Abstract – This work investigates the lateral fuel mixing in fluidized beds with a cross-flow of sol...
In typical dual fluidized bed systems — used e.g. in chemical looping combustion or indirect gasific...
For solid fuels, thermochemical conversion processes such as combustion and gasification are especia...
Operational conditions, such as the fluidization velocity and the solids cross-flow, affect the degr...
A semiempirical model for the mixing of fuel particles in a fluidized bed is presented and validated...
The mixing pattern of a tracer particle which simulates a fuel particle is studied in a cold 2-dimen...
Fluidized bed technology is used for thermal conversion of solid fuels (combustion and gasification)...
The aim of this thesis was to improve the fuel conversion in Chalmers bubbling fluidized bed (BFB) g...
A 1-dimensional model is used to analyse how solids material circulation, biomass reactivity and gas...
A Monte Carlo model was proposed to characterize the fuel particles motion in a large-scale fluidize...
This work investigates the lateral mixing process of fuel in a cold flow model of a fluidized-bed ga...
This work investigates the lateral mixing process of fuel in a cold flow model of a fluidized-bed ga...
This work investigates the lateral fuel mixing in fluidized beds with a crossflow of solids by means...
Operational conditions, such as the fluidization velocity or the solids cross-flow, have been found ...
For solid fuels, thermochemical conversion processes such as combustion and gasification are especia...
Abstract – This work investigates the lateral fuel mixing in fluidized beds with a cross-flow of sol...
In typical dual fluidized bed systems — used e.g. in chemical looping combustion or indirect gasific...
For solid fuels, thermochemical conversion processes such as combustion and gasification are especia...
Operational conditions, such as the fluidization velocity and the solids cross-flow, affect the degr...
A semiempirical model for the mixing of fuel particles in a fluidized bed is presented and validated...
The mixing pattern of a tracer particle which simulates a fuel particle is studied in a cold 2-dimen...
Fluidized bed technology is used for thermal conversion of solid fuels (combustion and gasification)...
The aim of this thesis was to improve the fuel conversion in Chalmers bubbling fluidized bed (BFB) g...
A 1-dimensional model is used to analyse how solids material circulation, biomass reactivity and gas...
A Monte Carlo model was proposed to characterize the fuel particles motion in a large-scale fluidize...