Determination of active sites during gasification of biomass char with CO2 using temperature-programmed desorption. Part 1: Methodology & desorption spectra

被引:21
|
作者
Schneider, Christoph [1 ]
Prat, Sonia Rincon [2 ]
Kolb, Thomas [1 ,3 ]
机构
[1] Karlsruhe Inst Technol, Engler Bunte Inst, EBI Ceb, Fuel Technol, Engler Bunte Ring 1, D-76131 Karlsruhe, Germany
[2] Univ Nacl Colombia, Dept Ingn Mecan & Mecatron, BIOT, Grp Invest Biomasa & Optimizac Term Proc, Carrera 30 45A-03, Bogota, Colombia
[3] Karlsruhe Inst Technol, Inst Tech Chem, ITC Vgt, Hermann von Helmholtz Pl 1, D-76344 Eggenstein Leopoldshafen, Germany
关键词
Biomass char; Gasification kinetics; Surface chemistry; Temperature-programmed desorption; Active sites; RANDOM PORE MODEL; THERMAL-DECOMPOSITION; TRANSIENT KINETICS; CARBON-DIOXIDE; COAL CHAR; EVOLUTION; REACTIVITY; PYROLYSIS; RATES;
D O I
10.1016/j.fuel.2019.116726
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Based on a carbon conversion mechanism for the gasification of carbon with CO2, a method for the determination of active sites during gasification of biomass char is presented. Beech wood char was partially gasified in CO2 followed by a temperature-programmed desorption (TPD) in order to determine total and stable surface complexes as a function of carbon conversion degree. The experiments were conducted in a temperature controlled quartz glass reactor coupled with a mass spectrometer for the detection of desorbed gas species (CO and CO2). Similar CO2 signals for total and stable surface complexes are observed for all carbon conversion degrees. Increased release of CO during the determination of total and stable surface complexes is detected for X-C = 0.9 carbon conversion degree. The desorption spectra of CO and CO2 during TPD cannot completely be explained by the underlying mechanistic model. The measured concentration profiles indicate that the gas species released during TPD may originate from decomposition of surface complexes but also from decomposition of ash components. CO and CO2 arising from of ash components or surface complexes must be differentiated in order to determine reactive surface area (RSA) as a function of carbon conversion degree which is then transferred into a kinetic rate expression for the specific conversion rate R-m. This paper describes the methodology applied for the determination of RSA and discusses the raw data obtained during TPD. In part 2, a detailed analysis concerning the origin of the released gases during TPD is conducted.
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页数:9
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