Experimental Evaluation of a New Approach for a Two-Stage Hydrothermal Biomass Liquefaction Process

被引:4
|
作者
Klemm, Marco [1 ]
Kroeger, Michael [1 ]
Goersch, Kati [1 ]
Lange, Ruediger [2 ]
Hilpmann, Gerd [2 ]
Lali, Farzad [2 ]
Haase, Stefan [2 ]
Krusche, Michael [3 ]
Ullrich, Frank [3 ]
Chen, Zihao [4 ]
Wilde, Nicole [4 ]
Al-Naji, Majd [4 ]
Glaeser, Roger [4 ]
机构
[1] DBFZ Deutsch Biomasseforschungszentrum Gemeinnutz, D-04347 Leipzig, Germany
[2] Tech Univ Dresden, Chair Chem React Engn & Proc Plants, Fac Mech Sci & Engn, D-01069 Dresden, Germany
[3] Adv Machinery & Technol Chemnitz GmbH, D-09125 Chemnitz, Germany
[4] Univ Leipzig, Fac Chem & Mineral, Inst Chem Technol, D-04103 Leipzig, Germany
关键词
liquefaction; hydrothermal process; transfer hydrogenation; heterogeneously catalyzed reaction; hydrogen donor; wet biomass; CATALYTIC TRANSFER HYDROGENATION; GAMMA-VALEROLACTONE; LEVULINIC ACID; FORMIC-ACID; CONVERSION; WATER; GASIFICATION; GLUCOSE; PATHWAY; BIOFUEL;
D O I
10.3390/en13143692
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A new approach for biomass liquefaction was developed and evaluated in a joint research project. Focus of the project, called FEBio@H2O, lies on a two-step hydrothermal conversion. Within step 1, the input biomass is converted employing a hydrothermal degradation without added catalyst or by homogeneous catalysis. Within step 2, the hydrogen accepting products of step 1, e.g., levulinic acid (LA) are upgraded by a heterogeneously catalyzed hydrogenation with hydrogen donor substances, e.g., formic acid (FA). As a result, components with an even lower oxygen content in comparison to step 1 products are formed; as an example, gamma-valerolactone (GVL) can be named. Therefore, the products are more stable and contained less oxygen as requested for a possible application as liquid fuel. As a hydrothermal process, FEBio@H2O is especially suitable for highly water-containing feedstock. The evaluation involves hydrothermal conversion tests with model substances, degradation of real biomasses, transfer hydrogenation or hydrogenation with hydrogen donor of model substances and real products of step 1, catalyst selection and further development, investigation of the influence of reactor design, the experimental test of the whole process chain, and process assessment.
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页数:15
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