Continuous hydrothermal co-liquefaction of aspen wood and glycerol with water phase recirculation

被引:167
作者
Pedersen, T. H. [1 ]
Grigoras, I. F. [1 ]
Hoffmann, J. [1 ]
Toor, S. S. [1 ]
Daraban, I. M. [1 ]
Jensen, C. U. [2 ]
Iversen, S. B. [2 ]
Madsen, R. B. [3 ,4 ]
Glasius, M. [3 ,4 ]
Arturi, K. R. [5 ]
Nielsen, R. P. [5 ]
Sogaard, E. G. [5 ]
Rosendahl, L. A. [1 ]
机构
[1] Aalborg Univ, Dept Energy Technol, DK-9220 Aalborg, Denmark
[2] Steeper Energy Aps, DK-2970 Horsholm, Denmark
[3] Aarhus Univ, Dept Chem, DK-8000 Aarhus C, Denmark
[4] Aarhus Univ, iNANO, DK-8000 Aarhus C, Denmark
[5] Aalborg Univ, Dept Chem & Biosci, DK-6700 Esbjerg, Denmark
关键词
Biofuel; Continuous processing; Biocrude; Biomass; Hydrothermal liquefaction; Sustainability; HOT COMPRESSED WATER; PROMOTED H-DONATION; CRUDE BIO-OIL; ASSISTED LIQUEFACTION; DONOR MEDIA; CONVERSION; BIOMASS; ALCOHOLS; LIGNIN; TEMPERATURE;
D O I
10.1016/j.apenergy.2015.10.165
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
Hydrothermal liquefaction is a promising technology for the conversion of a wide range of bio-feedstock into a biocrude; a mixture of chemical compounds that holds the potential for a renewable production of chemicals and fuels. Most research in hydrothermal liquefaction is performed in batch type reactors, although a continuous and energy-efficient operation is paramount for such process to be feasible. In this work an experimental campaign in a continuous bench scale unit is presented. The campaign is based on glycerol-assisted hydrothermal liquefaction of aspen wood carried out with the presence of a homogeneous catalyst at supercritical water conditions, 400 degrees C and 300 bar. Furthermore, in the experimental campaign a water phase recirculation step is incorporated to evaluate the technical feasibility of such procedure. In total, four batches of approximately 100 kg of feed each were, processed successfully at steady state conditions without any observation of system malfunctioning. The biocrude obtained was characterized using several analytical methods to evaluate the feasibility of the process and the quality of the product. Results showed that a high quality biocrude was obtained having a higher heating value of 34.3 MJ/kg. The volatile fraction of the biocrude consisted mostly of compounds having number of carbon atoms in the C-6-C-12 range similar to gasoline. In terms of process feasibility, it was revealed that total organic carbon (TOC) and ash significantly accumulated in the water phase when such is recirculated for the proceeding batch. After four batches the TOC and the ash mass fraction of the water phase were 136.2 [g/L] and 12.6 [%], respectively. Water phase recirculation showed a slight increase in the biocrude quality in terms on an effective hydrogen-to-carbon ratio, but it showed no effects on the product gas composition or the pH of the water phase. The successful operation demonstrated the technical feasibility of a continuous production of high quality biocrude. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1034 / 1041
页数:8
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