The effect of temperature and steam concentration on the yields of different tar compounds was investigated. Wood pellets and dried sewage sludge spheres (DSS) were pyrolyzed in a fluidized bed reactor in the temperature range of 500-800ºC. The reactor has two independent electrically heated zones, enabling independent adjustment of the temperature of generation of volatiles (release of volatiles during thermal decomposition of the fuel particle) and secondary conversion of the volatiles on homogeneous phase. The temperatures of the bed and the freeboard were varied independently keeping constant the residence time of volatiles in each zone. This work is one of the tasks within a project whose overall objective is the development of a three...
A numerical study is performed in order to evaluate the performance and optimal operating conditions...
A multi-stage fluidized bed (MSFB) by configuring the distributor with an overflow standpipe between...
The influence of reaction conditions on light gas species (CO, CO<sub>2</sub>, H<sub>2</sub> and lig...
An integrated fluidized bed (IFB) consisting of an upper transport bed section and a bottom fluidize...
Fluidized bed gasification is a promising technology for the energetic valorization of biomass and w...
The major problem of fluidized bed biomass gasification is the high tar contamination of the produce...
This paper describes studies concerning the formation of tars in a pressurized fluidized-bed gasifie...
This work investigates the fate of polycyclic aromatic hydrocarbons (PAH) in relation to the process...
Steam gasification of lignocellulosic biomass in a bubbling fluidized bed reactor was analyzed by me...
A pilot scale fluidized bed fast pyrolysis set-up was designed and operated. The fluidized bed tempe...
To utilize low rank coal cleanly and high efficiently, a new fluidized bed two-stage gasification (F...
In the chemical industry, Synthesis Gas (syngas) has been traditionally produced by steam reforming ...
To utilize low rank coal cleanly and high efficiently, a new fluidized bed two-stage gasification (F...
Cottonwood (branches) were gasified in the presence of steam in a 5.08 cm I.D. bench-scale fluidized...
Coal pyrolysis is generally performed in atmospheres without oxygen and at temperatures below 650 de...
A numerical study is performed in order to evaluate the performance and optimal operating conditions...
A multi-stage fluidized bed (MSFB) by configuring the distributor with an overflow standpipe between...
The influence of reaction conditions on light gas species (CO, CO<sub>2</sub>, H<sub>2</sub> and lig...
An integrated fluidized bed (IFB) consisting of an upper transport bed section and a bottom fluidize...
Fluidized bed gasification is a promising technology for the energetic valorization of biomass and w...
The major problem of fluidized bed biomass gasification is the high tar contamination of the produce...
This paper describes studies concerning the formation of tars in a pressurized fluidized-bed gasifie...
This work investigates the fate of polycyclic aromatic hydrocarbons (PAH) in relation to the process...
Steam gasification of lignocellulosic biomass in a bubbling fluidized bed reactor was analyzed by me...
A pilot scale fluidized bed fast pyrolysis set-up was designed and operated. The fluidized bed tempe...
To utilize low rank coal cleanly and high efficiently, a new fluidized bed two-stage gasification (F...
In the chemical industry, Synthesis Gas (syngas) has been traditionally produced by steam reforming ...
To utilize low rank coal cleanly and high efficiently, a new fluidized bed two-stage gasification (F...
Cottonwood (branches) were gasified in the presence of steam in a 5.08 cm I.D. bench-scale fluidized...
Coal pyrolysis is generally performed in atmospheres without oxygen and at temperatures below 650 de...
A numerical study is performed in order to evaluate the performance and optimal operating conditions...
A multi-stage fluidized bed (MSFB) by configuring the distributor with an overflow standpipe between...
The influence of reaction conditions on light gas species (CO, CO<sub>2</sub>, H<sub>2</sub> and lig...