AJUNTAMENT D'ALCOI
Website
Generalitat Valenciana
Website
Ayuntamiento de Valencia
Website
Cicloplast
Website
Ayuntamiento de Onil
Website
Anarpla
Website
Ayuntamiento de Mislata
Website
nlWA, North London Waste Authority
Website
Ayuntamiento de Salinas
Website
Zicla
Website
Fondazione Ecosistemi
Website
PEFC
Website
ALQUIENVAS
Website
DIPUTACI� DE VAL�NCIA
Website
AYUNTAMIENTO DE REQUENA
Website
UNIVERSIDAD DE ZARAGOZA
Website
OBSERVATORIO CONTRATACIÓN PÚBLICA
Website
AYUNTAMIENTO DE PAIPORTA
Website
AYUNTAMIENTO DE CUENCA
Website
BERL� S.A.
Website
CM PLASTIK
Website
TRANSFORMADORES INDUSTRIALES ECOL�GICOS
INDUSTRIAS AGAPITO
Website
RUBI KANGURO
Website
If you want to support our LIFE project as a STAKEHOLDER, please contact with us: life-future-project@aimplas.es
In this section, you can access to the latest technical information related to the FUTURE project topic.
Comprehensive optimization of coal chemical looping gasification process for low CO2 emission based on multi-scale simulation coupled experiment
Carbon dioxide (CO2) emission reduction has become an urgent topic to be studied and solved with the in-depth understanding of global warming and frequent occurrence of extreme climate. At present, the application of chemical looping technology in coal gasification to produce high purity synthesis gas is an important way to achieve CO2 emission reduction, ensure energy security, and promote ecological civilization. In this paper, a new fusion research method combining multi-scale modeling and experimental testing is adopted to comprehensively optimize the coal chemical looping gasification (CCLG) process, aiming at ruducing CO2 emissions in the synthesis gas production of CCLG. In order to investigate the effect of main reaction conditions on CCLG process, the pyrolysis and gasification experiments of Meihuajing coal are carried out in a tubular furnace reactor with Fe2O3 and CuO as oxygen carriers respectively. Subsequently, the multi-scale simulation of CCLG process including molecular dynamics (MD) and computational fluid dynamics (CFD) simulations is performed to validate the experimental results and supplement important reaction kinetics data. Both of multi-scale modeling and experimental testing suggest that the optimum pyrolysis temperature range, gasification temperature range, char/oxygen carrier mass ratio (C/O), and steam flow are below 900 ?, 900?950 ?, 1:1.5, and 0.15?g/min respectively, providing an effective guidance for the optimal design of practical CCLG pilot plant.
» Author: Zhe Cui, Suli Sun, Haoran Zhang, Bin Liu, Wende Tian, Qingjie Guo
» Publication Date: 15/09/2022
C/ Gustave Eiffel, 4
(València Parc Tecnològic) - 46980
PATERNA (Valencia) - SPAIN
(+34) 96 136 60 40
Project Management department - Sustainability and Industrial Recovery
life-future-project@aimplas.es