Air-based coal gasification in a two-chamber gas reactor with circulating fluidized bed

2017 ◽  
Vol 64 (1) ◽  
pp. 46-52 ◽  
Author(s):  
A. M. Dubinin ◽  
V. G. Tuponogov ◽  
Y. A. Kagramanov
Fuel ◽  
2015 ◽  
Vol 152 ◽  
pp. 131-137 ◽  
Author(s):  
Adam Klimanek ◽  
Wojciech Adamczyk ◽  
Anna Katelbach-Woźniak ◽  
Gabriel Węcel ◽  
Andrzej Szlęk

2020 ◽  
Vol 194 ◽  
pp. 04044
Author(s):  
Shengxian Xian ◽  
Denghao Jiang ◽  
Yanqi Fan ◽  
Haixia Zhang ◽  
Zhen Chai ◽  
...  

The release behavior of sulfur during coal gasification was studied in a bench-scale self-heated circulating fluidized bed gasifier. With the increase of the O2/C molar ratio, gasification temperature increases, which promotes sulfur release rate and the formation of H2S. The conversion reaction between H2S and COS is far from equilibrium and the yield of COS is excessive. Under the same molar ratio of O2/C, the increase of coal feeding rate can elevate the gasification temperature, promote the release of sulfur and the transformation of gaseous sulfur to H2S.


2017 ◽  
Vol 10 (1) ◽  
pp. 48-67
Author(s):  
Martin Schurz ◽  
Alexander Laugwitz ◽  
Steffen Krzack ◽  
Bernd Meyer

Background:Coal gasification is the promising technology for syngas routes to produce chemicals or transportation fuels. Additionally, it enables clean power generation from coal in Integrated Gasification Combined Cycles (IGCC). So far, coal fines with high ash contents could not be feasibly used in such routes.In this regard, the Internal Circulation gasifier (INCI) is designed to gasify high-ash coal fines efficiently. The staged system is combining a moving bed, a fluidized bed and a jetting fluidized bed in one reaction chamber.Method:The present paper substantially describes the laboratory-scale prototype development in the COORVED-project (“CO2-reduction by innovative gasifier design”) based on the INCI gasification principle of about 50-125 kW thermal input. Information about the gasifiers compounding, especially the reaction chamber, peripheral components and applied measurement systems are given.Results:Experimental results are presented, confirming the targeted, typical flow pattern inside the reaction chamber. Furthermore technical and operational limits of the COORVED prefiguration are discussed. Based on these results a major design change of the reaction chamber is required and explained in detail. Additionally, results of the feedstock variation from coke to lignite are shown.Conclusion:Finally, the operability of the INCI gasification principle is proven by a stationary operating system with controlled ash agglomeration.


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