AbstractA mathematical model of a biomass downdraft gasification process has been developed. The model was considered to be four modules that are drying, pyrolysis, oxidation, and reduction which the products of upper module will be the reactants of the next. The one-dimensional kinetic finite rate models were applied to drying and reduction modules. The pyrolysis model took place when drying temperature reached 473K. The equilibrium sequence model was used to describe the oxidation process by considering the sequence of order of reaction rates. For the model validation the comparison showed a good agreement. In the parametric study the moisture content increasing affected the height of drying, and pyrolysis zones increasing while the criti...
This paper describes a thermodynamic model of a fixed bed downdraft gasifier, based on the Cycle-Tem...
The development of a one-dimensional (1D) phenomenological model for biomass gasification in downdra...
Biomass gasification with in-situ CO2 capture, using calcium oxide as sorbent, has attracted increas...
Mathematical models and simulations are being practiced exceedingly in the field of research and dev...
A kinetic model was built to estimate the optimum working parameters of a downdraft gasifier, in whi...
Biomass gasification technology is evolving and more research through modelling alongside the experi...
AbstractIn order to optimize the operating conditions of a downdraft gasification process, mathemati...
A gasification model is developed and implemented in Matlab to simulate a downdraft gasifier using w...
Biomass containing organic materials could come from a number of sources such as from agricultural r...
A mathematical model was built to estimate the working parameters of a downdraft gasifier, in which ...
A zero-dimensional mathematical model for downdraft gasification of biomass in fixed or slowly movin...
The development of a one-dimensional (1D) phenomenological model for biomass gasification in downdra...
Gasification thermochemical processes of biomass in a 20 kW downdraft gasifier are investigated usin...
Thermochemical conversion of biomass in a gasifier for the production of syngas provides the enablin...
Gasification is a useful technology to recover energy from renewable biomass by producing a versatil...
This paper describes a thermodynamic model of a fixed bed downdraft gasifier, based on the Cycle-Tem...
The development of a one-dimensional (1D) phenomenological model for biomass gasification in downdra...
Biomass gasification with in-situ CO2 capture, using calcium oxide as sorbent, has attracted increas...
Mathematical models and simulations are being practiced exceedingly in the field of research and dev...
A kinetic model was built to estimate the optimum working parameters of a downdraft gasifier, in whi...
Biomass gasification technology is evolving and more research through modelling alongside the experi...
AbstractIn order to optimize the operating conditions of a downdraft gasification process, mathemati...
A gasification model is developed and implemented in Matlab to simulate a downdraft gasifier using w...
Biomass containing organic materials could come from a number of sources such as from agricultural r...
A mathematical model was built to estimate the working parameters of a downdraft gasifier, in which ...
A zero-dimensional mathematical model for downdraft gasification of biomass in fixed or slowly movin...
The development of a one-dimensional (1D) phenomenological model for biomass gasification in downdra...
Gasification thermochemical processes of biomass in a 20 kW downdraft gasifier are investigated usin...
Thermochemical conversion of biomass in a gasifier for the production of syngas provides the enablin...
Gasification is a useful technology to recover energy from renewable biomass by producing a versatil...
This paper describes a thermodynamic model of a fixed bed downdraft gasifier, based on the Cycle-Tem...
The development of a one-dimensional (1D) phenomenological model for biomass gasification in downdra...
Biomass gasification with in-situ CO2 capture, using calcium oxide as sorbent, has attracted increas...