CO2 gasification of biomass: The effect of lime concentration in a fluidized bed
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F44555601%3A13520%2F18%3A43893688" target="_blank" >RIV/44555601:13520/18:43893688 - isvavai.cz</a>
Výsledek na webu
<a href="http://dx.doi.org/10.1016/j.apenergy.2018.02.151" target="_blank" >http://dx.doi.org/10.1016/j.apenergy.2018.02.151</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.1016/j.apenergy.2018.02.151" target="_blank" >10.1016/j.apenergy.2018.02.151</a>
Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
CO2 gasification of biomass: The effect of lime concentration in a fluidized bed
Popis výsledku v původním jazyce
Calcined limestone or dolomite can be directly used in the fluidized bed (FB) gasification to reform tar compounds in situ, to enhance carbon conversion and cold gas efficiency of the gasification process. Unfortunately, such materials exhibit poorer mechanical properties, attrition, sintering and entrainment. Therefore they have to be replenished continuously or periodically. In this paper the effects of the ratio of calcined dolomitic limestone and silica sand in the FB (0 %, 25 %, 50 % and 100 %vol. of dolomitic limestone) for CO2 + O2 gasification of biomass and comparison with steam + O2 gasification was studied at temperature of 850 oC. The experiments were performed in a semi-auto-thermal spouting FB reactor gasifying 1.4 kg/h of woody biomass. In gasification by steam + O2 optimal results were found with 50 vol. % (35 mass %) lime in the FB (tar dew point 79 oC). At CO2 + O2 gasification the best results have been found for undiluted lime particles (tar dew point 71 oC).
Název v anglickém jazyce
CO2 gasification of biomass: The effect of lime concentration in a fluidized bed
Popis výsledku anglicky
Calcined limestone or dolomite can be directly used in the fluidized bed (FB) gasification to reform tar compounds in situ, to enhance carbon conversion and cold gas efficiency of the gasification process. Unfortunately, such materials exhibit poorer mechanical properties, attrition, sintering and entrainment. Therefore they have to be replenished continuously or periodically. In this paper the effects of the ratio of calcined dolomitic limestone and silica sand in the FB (0 %, 25 %, 50 % and 100 %vol. of dolomitic limestone) for CO2 + O2 gasification of biomass and comparison with steam + O2 gasification was studied at temperature of 850 oC. The experiments were performed in a semi-auto-thermal spouting FB reactor gasifying 1.4 kg/h of woody biomass. In gasification by steam + O2 optimal results were found with 50 vol. % (35 mass %) lime in the FB (tar dew point 79 oC). At CO2 + O2 gasification the best results have been found for undiluted lime particles (tar dew point 71 oC).
Klasifikace
Druh
J<sub>imp</sub> - Článek v periodiku v databázi Web of Science
CEP obor
—
OECD FORD obor
20402 - Chemical process engineering
Návaznosti výsledku
Projekt
—
Návaznosti
I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace
Ostatní
Rok uplatnění
2018
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Údaje specifické pro druh výsledku
Název periodika
Applied Energy
ISSN
0306-2619
e-ISSN
—
Svazek periodika
2018
Číslo periodika v rámci svazku
217
Stát vydavatele periodika
NL - Nizozemsko
Počet stran výsledku
8
Strana od-do
361-368
Kód UT WoS článku
000430030400032
EID výsledku v databázi Scopus
2-s2.0-85042856984