Chemical fractionation of inorganic constituents in entrained flow gasification of slurry from straw pyrolysis

被引:6
作者
Mielke, Konrad [1 ]
Kolb, Thomas [2 ]
Mueller, Michael [1 ]
机构
[1] Forschungszentrum Julich, Inst Energy & Climate Res IEK 2, Wilhelm Johnen Str, D-52425 Julich, Germany
[2] Karlsruhe Inst Technol, Engler Bunte Inst, Engler Bunte Ring 1, D-76131 Karlsruhe, Germany
关键词
Gasification; Ash fractionation; Slag; Viscosity; Biochar; Straw; VICTORIAN BROWN-COAL; GAS-PHASE; PART; RELEASE; ALKALI; ELEMENTS; BIOMASS; TRANSFORMATION; COMBUSTION; POTASSIUM;
D O I
10.1016/j.biombioe.2020.105732
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Pressurized entrained-flow gasification (PEFG) of straw biomass is currently being studied as a potentially sustainable and economically viable process to produce fuels and other vital chemicals. In the process chain the gasification is integrated and straw is converted via pyrolysis into a bioslurry consisting of a liquid, tar-rich phase and char. Afterwards, the slurry is gasified into a tar-free, low-methane syngas which is a basic reactant for the synthesis of biofuels. At the high temperatures over 1200 degrees C the ash constituents of the char in the bioslurry melt and flow down the inner wall as slag. The slag viscosity has to be in a certain range to form a protective layer at the reactor wall and to guarantee a continuous removing. For this reason, the composition of the molten ash at the reactor wall has to be well known. Due to several fractionation processes in the gasifier the composition of the slag at the reactor wall does not correspond directly with the slurry ash. Therefore, experiments were conducted to identify depletion and enrichment processes in the gasifier. Finally, the composition of the slag at the reactor wall is obtained and can be used for the adjustment of the viscosity.
引用
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页数:11
相关论文
共 48 条
[1]   Viscosity of ashes from energy production and municipal solid waste handling: A comparative study between two different experimental setups [J].
Arvelakis, S. ;
Frandsen, F. J. ;
Folkedahl, B. ;
Hurley, J. .
ENERGY & FUELS, 2008, 22 (05) :2948-2954
[2]  
Arvelakis S., 2005, P 30 INT TECHN C COA, P1215
[3]   Release of Inorganic Elements from Gasification and Co-Gasification of Coal with Miscanthus, Straw, and Wood at High Temperature [J].
Blaesing, Marc ;
Hasir, Nurul Baity Ahmad ;
Mueller, Michael .
ENERGY & FUELS, 2015, 29 (11) :7386-7394
[4]   Release of alkali metal, sulphur, and chlorine species from high temperature gasification of high- and low-rank coals [J].
Blaesing, Marc ;
Mueller, Michael .
FUEL PROCESSING TECHNOLOGY, 2013, 106 :289-294
[5]   The bioliq process for producing synthetic transportation fuels [J].
Dahmen, Nicolaus ;
Abeln, Johannes ;
Eberhard, Mark ;
Kolb, Thomas ;
Leibold, Hans ;
Sauer, Joerg ;
Stapf, Dieter ;
Zimmerlin, Bernd .
WILEY INTERDISCIPLINARY REVIEWS-ENERGY AND ENVIRONMENT, 2017, 6 (03)
[6]   Synthetic chemical product and fuels from biomass [J].
Dahmen, Nicolaus ;
Dinjus, Eckhard .
CHEMIE INGENIEUR TECHNIK, 2010, 82 (08) :1147-1152
[7]   Alkali emission from birchwood particles during rapid pyrolysis [J].
Davidsson, KO ;
Stojkova, BJ ;
Pettersson, JBC .
ENERGY & FUELS, 2002, 16 (05) :1033-1039
[8]   Release of inorganic constituents from leached biomass during thermal conversion [J].
Dayton, DC ;
Jenkins, BM ;
Turn, SQ ;
Bakker, RR ;
Williams, RB ;
Belle-Oudry, D ;
Hill, LM .
ENERGY & FUELS, 1999, 13 (04) :860-870
[9]   DIRECT OBSERVATION OF ALKALI VAPOR RELEASE DURING BIOMASS COMBUSTION AND GASIFICATION .1. APPLICATION OF MOLECULAR-BEAM MASS-SPECTROMETRY TO SWITCHGRASS COMBUSTION [J].
DAYTON, DC ;
FRENCH, RJ ;
MILNE, TA .
ENERGY & FUELS, 1995, 9 (05) :855-865
[10]   How inorganic elements of biomass influence char steam gasification kinetics [J].
Dupont, Capucine ;
Jacob, Sylvain ;
Marrakchy, Khalil Ould ;
Hognon, Celine ;
Grateau, Maguelone ;
Labalette, Francoise ;
Perez, Denilson Da Silva .
ENERGY, 2016, 109 :430-435