Syngas Composition: Gasification of Wood Pellet with Water Steam through a Reactor with Continuous Biomass Feed System
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F61989100%3A27730%2F20%3A10245318" target="_blank" >RIV/61989100:27730/20:10245318 - isvavai.cz</a>
Výsledek na webu
<a href="https://www.mdpi.com/1996-1073/13/17/4376/htm#B2-energies-13-04376" target="_blank" >https://www.mdpi.com/1996-1073/13/17/4376/htm#B2-energies-13-04376</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.3390/en13174376" target="_blank" >10.3390/en13174376</a>
Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
Syngas Composition: Gasification of Wood Pellet with Water Steam through a Reactor with Continuous Biomass Feed System
Popis výsledku v původním jazyce
Investigations were performed in relation to the thermal gasification of wood granulate using steam in an allothermal reactor with electric heaters. They studied the impact of the temperature inside the reactor and the steam flow rate on the percentage shares of H2, CH4, CO and CO2 in synthesis gas and on the calorific value of syngas. The tests were conducted at temperatures inside the reactor equal to 750, 800 and 850 oC and with a steam flow rate equal to 10.0 15.0 and 20.0 kg/h. The intensity of gasified biomass was 20 kg/h A significant impact of the temperature on the percentages of all the components of synthesis gas and a significant impact of the steam flow rate on the content of hydrogen and carbon dioxide in syngas were found. The highest percentage of hydrogen obtained was 43.3%. The calorific value of the gas depended significantly on the temperature inside the reactor and the correlation between the temperature and the steam flow rate. Its maximum value was 13.3 MJ//m^3 at 800 oC. This paper also includes an assessment of the mutual correlations of the percentage shares of the individual synthesis gas components.
Název v anglickém jazyce
Syngas Composition: Gasification of Wood Pellet with Water Steam through a Reactor with Continuous Biomass Feed System
Popis výsledku anglicky
Investigations were performed in relation to the thermal gasification of wood granulate using steam in an allothermal reactor with electric heaters. They studied the impact of the temperature inside the reactor and the steam flow rate on the percentage shares of H2, CH4, CO and CO2 in synthesis gas and on the calorific value of syngas. The tests were conducted at temperatures inside the reactor equal to 750, 800 and 850 oC and with a steam flow rate equal to 10.0 15.0 and 20.0 kg/h. The intensity of gasified biomass was 20 kg/h A significant impact of the temperature on the percentages of all the components of synthesis gas and a significant impact of the steam flow rate on the content of hydrogen and carbon dioxide in syngas were found. The highest percentage of hydrogen obtained was 43.3%. The calorific value of the gas depended significantly on the temperature inside the reactor and the correlation between the temperature and the steam flow rate. Its maximum value was 13.3 MJ//m^3 at 800 oC. This paper also includes an assessment of the mutual correlations of the percentage shares of the individual synthesis gas components.
Klasifikace
Druh
J<sub>imp</sub> - Článek v periodiku v databázi Web of Science
CEP obor
—
OECD FORD obor
20300 - Mechanical engineering
Návaznosti výsledku
Projekt
<a href="/cs/project/EF16_019%2F0000753" target="_blank" >EF16_019/0000753: Centrum výzkumu nízkouhlíkových energetických technologií</a><br>
Návaznosti
P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)
Ostatní
Rok uplatnění
2020
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Údaje specifické pro druh výsledku
Název periodika
Energies
ISSN
1996-1073
e-ISSN
—
Svazek periodika
13
Číslo periodika v rámci svazku
17
Stát vydavatele periodika
CH - Švýcarská konfederace
Počet stran výsledku
14
Strana od-do
1-14
Kód UT WoS článku
000569939500001
EID výsledku v databázi Scopus
—