scholarly journals Interactions between Automotive Shredder Residue and Olivine Bed Material during Indirect Fluidized Bed Gasification

Author(s):  
Robin Faust ◽  
Panida Aonsamang ◽  
Jelena Maric ◽  
Alyona Tormachen ◽  
Martin Seemann ◽  
...  
2010 ◽  
Vol 181 (1-3) ◽  
pp. 827-835 ◽  
Author(s):  
J. Van Caneghem ◽  
C. Block ◽  
I. Vermeulen ◽  
A. Van Brecht ◽  
P. Van Royen ◽  
...  

Energies ◽  
2021 ◽  
Vol 14 (2) ◽  
pp. 399
Author(s):  
Selina Hafner ◽  
Max Schmid ◽  
Günter Scheffknecht

Finding a way for mitigating climate change is one of the main challenges of our generation. Sorption-enhanced gasification (SEG) is a process by which syngas as an important intermediate for the synthesis of e.g., dimethyl ether (DME), bio-synthetic natural gas (SNG) and Fischer–Tropsch (FT) products or hydrogen can be produced by using biomass as feedstock. It can, therefore, contribute to a replacement for fossil fuels to reduce greenhouse gas (GHG) emissions. SEG is an indirect gasification process that is operated in a dual-fluidized bed (DFB) reactor. By the use of a CO2-active sorbent as bed material, CO2 that is produced during gasification is directly captured. The resulting enhancement of the water–gas shift reaction enables the production of a syngas with high hydrogen content and adjustable H2/CO/CO2-ratio. Tests were conducted in a 200 kW DFB pilot-scale facility under industrially relevant conditions to analyze the influence of gasification temperature, steam to carbon (S/C) ratio and weight hourly space velocity (WHSV) on the syngas production, using wood pellets as feedstock and limestone as bed material. Results revealed a strong dependency of the syngas composition on the gasification temperature in terms of permanent gases, light hydrocarbons and tars. Also, S/C ratio and WHSV are parameters that can contribute to adjusting the syngas properties in such a way that it is optimized for a specific downstream synthesis process.


2003 ◽  
Vol 36 (7) ◽  
pp. 782-787 ◽  
Author(s):  
Tadaaki Shimizu ◽  
Jun Asazuma ◽  
Masayuki Shinkai ◽  
Sayako Matsunaga ◽  
Kazuaki Yamagiwa ◽  
...  

2015 ◽  
Vol 23 (2) ◽  
pp. 417-424 ◽  
Author(s):  
Francesco Ferella ◽  
Ida De Michelis ◽  
Agostino Scocchera ◽  
Mario Pelino ◽  
Francesco Vegliò

2018 ◽  
Vol 57 ◽  
pp. 143-153 ◽  
Author(s):  
Shuangqiao Yang ◽  
Feng Zhong ◽  
Meng Wang ◽  
Shibing Bai ◽  
Qi Wang

2007 ◽  
Vol 11 (1) ◽  
pp. 5-15 ◽  
Author(s):  
Kyriakos Panopoulos ◽  
Lydia Fryda ◽  
Emmanuel Kakaras

Three promising biomass fuels from southern European regions were gasified atmospherically with air in a lab-scale fluidized bed reactor with quartz or olivine as bed material. The fuels used were an agro-industrial residue (olive bagasse) and the energy crops giant reed and sweet sorghum bagasse. Varying air ratios and temperatures were tested to study the impact on the product gas composition and tar load. Tars were higher in the case of olive bagasse, attributed to its higher lignin content compared to the other two biomasses with higher cellulose. Giant reed gasification causes agglomeration and defluidisation problems at 790?C while olive bagasse shows the least agglomeration tendency. The particular olivine material promoted the destruction of tars, but to a lesser level than other reported works; this was attributed to its limited iron content. It also promoted the H2 and CO2 production while CO content decreased. Methane yield was slightly affected (decreased) with olivine, higher temperatures, and air ratios. Air ratio increase decreased the tar load but at the same time the gas quality deteriorated. .


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