Chemical looping catalytic steam gasification (CLCSG) of algae over La1-Ba FeO3 perovskites for syngas production

2021 ◽  
Vol 151 ◽  
pp. 106154
Author(s):  
Jingchun Yan ◽  
Shouxi Jiang ◽  
Tao Song ◽  
Laihong Shen
2021 ◽  
Vol 35 (6) ◽  
pp. 4997-5005
Author(s):  
Xiaoxia Yang ◽  
Shengshen Gu ◽  
Amanj Kheradmand ◽  
Yijiao Jiang

Fuel ◽  
2021 ◽  
Vol 303 ◽  
pp. 121269
Author(s):  
Kun Zhao ◽  
Xiaojie Fang ◽  
Zhen Huang ◽  
Guoqiang Wei ◽  
Anqing Zheng ◽  
...  

2017 ◽  
Vol 31 (11) ◽  
pp. 12932-12941 ◽  
Author(s):  
Charlotte Lang ◽  
Xavier Sécordel ◽  
Claire Courson

Author(s):  
Nicolas Piatkowski ◽  
Christian Wieckert ◽  
Aldo Steinfeld

Gasification of coal, biomass, and other carbonaceous materials for high-quality syngas production is considered using concentrated solar energy as the source of high-temperature process heat. The solar reactor consists of two cavities separated by a SiC-coated graphite plate, with the upper one serving as the radiative absorber and the lower one containing the reacting packed bed that shrinks as the reaction progresses. A 5-kW prototype reactor with an 8 cm-depth, 14.3 cm-diameter cylindrical bed was fabricated and tested in the High-Flux Solar Simulator at PSI, subjected to solar flux concentrations up to 2300 suns. Beech charcoal was used as a model feedstock and converted into high-quality syngas (predominantly H2 and CO) with packed-bed temperatures up to 1500 K, an upgrade factor of the calorific value of 1.33, and an energy conversion efficiency of 29%. Pyrolysis was evident through the evolution of higher gaseous hydrocarbons during heating of the packed bed. The engineering design, fabrication, and testing of the solar reactor are described.


Fuel ◽  
2022 ◽  
Vol 309 ◽  
pp. 122100
Author(s):  
Ming Luo ◽  
Haiyan Zhang ◽  
Shuxiang Wang ◽  
Jianjun Cai ◽  
Yanjun Qin ◽  
...  

2022 ◽  
pp. 66-83
Author(s):  
Qingjiao Zhu ◽  
Xintong Guo ◽  
Yanan Guo ◽  
Jingjing Ma ◽  
Qingjie Guo

With the acceleration of industrialization and urbanization in China, wastewater treatment is increasing yearly. As a by-product of wastewater treatment, the gasification of sludge with coal in chemical looping process is a clean and efficient conversion technology. To explore the reaction behavior of cogasification of sludge and coal with iron-based oxygen carriers (OCs) for producing hydrogen-rich syngas, the experiment of cogasification using Fe2O3/Al2O3 as OC in a fluidized bed reactor was conducted. The result showed that the volume percentage of hydrogen (H2) and syngas yield is proportional to the amount of sludge added. The optimal operation conditions were: temperature at 900 °C, the mass ratio of OC to coal at 5.80 and mass ratio of sludge to coal at 0.2. Under this operating condition, the volume percentage of H2 and syngas yield in the flue gas was 75.6 vol% and 97.5 L·min-1·kg-1, respectively. Besides, the OC showed a stable reactivity in the sixth redox cycle with added sludge. However, the reactivity of OC significantly declined in the seventh and eighth redox cycles. It was recovered when the ash was separated. The decrease in the specific surface area of the OC caused by ash deposition is the main reason for the decline in its reactivity. The kinetic analysis showed that the random pore model describes the reaction mechanism of sludge/coal chemical looping gasification (CLG). The addition of sludge can reduce the activation energy of coal CLG reaction, accelerate the gasification reaction rate and increase the carbon conversion.


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