Optimization of Slag Mobility of Biomass Fuels in a Pilot-scale Entrained-Flow Gasifier

被引:0
|
作者
Mielke, Konrad [1 ]
Wu, Guixuan [1 ,2 ]
Eberhard, Mark [3 ]
Kolb, Thomas [4 ]
Mueller, Michael [1 ]
机构
[1] Forschungszentrum Julich, Inst Energy & Climate Res IEK 2, Wilhelm Johnen Str, D-52425 Julich, Germany
[2] GTT Technol, Kaiserstr 103, D-52134 Herzogenrath, Germany
[3] Karlsruhe Inst Technol, Inst Tech Chem ITC, POB 3640, D-76021 Karlsruhe, Germany
[4] Karlsruhe Inst Technol, Engler Bunte Inst, Engler Bunte Ring 9a, D-76131 Karlsruhe, Germany
关键词
Biomass fuels; Entrained‐ flow gasification; Oxide melts; Slag mobility; Viscosity; OXIDE MELTS RELEVANT; FULLY LIQUID SLAGS; VISCOSITY MODEL; PART; IRON-OXIDE; SYSTEMS; GASIFICATION;
D O I
10.1002/ceat.202000531
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The bioliq (R) process, developed at the Karlsruhe Institute for Technology, aims at the production of synthetic fuels and chemicals from biomass. The bioliq (R) technology is based on a two-step process with decentral pyrolysis for the production of a transportable slurry from residual biomass and the central entrained-flow gasification of the slurry by using biomass-to-liquid technology. This study is focused on the slag, which is formed by melting the inorganic ash components during gasification. To operate the gasifier smoothly, a range of desired viscosity has to be defined. A structure-based viscosity model was used to predict the viscosity of the slags at the gasifier outlet. A good agreement between experimental and calculated viscosities is achieved for fully liquid slag systems.
引用
收藏
页码:1302 / 1310
页数:9
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