scholarly journals Hydrogen from biomass: large-scale hydrogen production based on a dual fluidized bed steam gasification system

2011 ◽  
Vol 1 (1) ◽  
pp. 55-61 ◽  
Author(s):  
Stefan Müller ◽  
Martin Stidl ◽  
Tobias Pröll ◽  
Reinhard Rauch ◽  
Hermann Hofbauer
2018 ◽  
Vol 111 ◽  
pp. 320-329 ◽  
Author(s):  
Michael Kraussler ◽  
Matthias Binder ◽  
Philipp Schindler ◽  
Hermann Hofbauer

Energy ◽  
2019 ◽  
Vol 173 ◽  
pp. 1256-1272 ◽  
Author(s):  
A.M. Mauerhofer ◽  
J.C. Schmid ◽  
F. Benedikt ◽  
J. Fuchs ◽  
S. Müller ◽  
...  

Fuel ◽  
2014 ◽  
Vol 127 ◽  
pp. 178-185 ◽  
Author(s):  
Stefan Penthor ◽  
Karl Mayer ◽  
Stefan Kern ◽  
Hannes Kitzler ◽  
David Wöss ◽  
...  

Author(s):  
Anna Magdalena Mauerhofer ◽  
Florian Benedik ◽  
Johannes Christian Schmid ◽  
Hermann Hofbauer

Author(s):  
Anna Magdalena Mauerhofer ◽  
Stefan Müller ◽  
Florian Benedikt ◽  
Josef Fuchs ◽  
Alexander Bartik ◽  
...  

Abstract A 100 kWth dual fluidized bed steam gasification pilot plant has been developed at TU Wien to convert different types of biogenic fuels into a valuable product gas. In this paper, the conversion of different biogenic fuels in combination with the utilization of CO2 as alternative gasification agent was investigated in the mentioned pilot plant. For this purpose, five experimental campaigns were carried out aiming at the investigation of softwood as reference fuel, and rapeseed cake, bark and lignin as alternative fuels. Pure olivine as well as a mixture (90/10 wt%) of olivine and limestone were used as bed materials. The product gas compositions of the different biogenic fuels changed depending on the elemental composition of the biogenic fuels. Thus, a high amount of carbon in the fuel enhanced CO formation, whereas an increased content of oxygen led to higher CO2 contents. Additionally, the presence of alkali metals in the biomass ash favoured the production of CO. The addition of limestone enhanced the H2 and CO contents via the water gas shift reaction as well as steam and dry reforming reactions, but had no significant effect on tar contents. Overall, this paper presents the feasibility of the dual-fluidized bed gasification process of different biogenic fuels with CO2 as gasification agent.


Author(s):  
Andreas Kreuzeder ◽  
Christoph Pfeifer ◽  
Hermann Hofbauer

Gasification of biomass is an attractive technology for combined heat and power (CHP) production. A dual fluidized bed steam gasifier is in commercial operation at the biomass CHP plant in Guessing/Austria since 2002. For circulating fluidized bed applications the bed material consumption is economically crucial. Thus, cyclones for circulating fluidized beds need to be designed properly. Some erosion and caking in the cyclone of the gasifier could be observed with increasing hours of operation. The influences of these effects as well as the influence of the solid circulation rate between the two units on the separation efficiency were investigated by fluid-dynamic investigations using a scaled cold model. The results show that due to erosion and caking elutriation rates are increased, especially for smaller particles. However, the cyclone achieves fractional separation efficiencies of more than 99.9%.


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