Hydrothermal liquefaction of lignin in near-critical water in a new batch reactor: Influence of phenol and temperature

被引:74
|
作者
Arturi, Katarzyna R. [1 ]
Strandgaard, Morten [1 ]
Nielsen, Rudi P. [1 ]
Sogaard, Erik G. [1 ]
Maschietti, Marco [1 ]
机构
[1] Aalborg Univ, Fac Sci & Engn, Sect Chem Engn, Dept Chem & Biosci, Niels Bohrs Vej 8, DK-6700 Esbjerg, Denmark
来源
关键词
Kraft lignin; Hydrothermal conversion; Aromatic monomers; Biocrude; Co-solvent; Injection; SUPERCRITICAL WATER; ELEVATED-TEMPERATURE; MODEL-COMPOUND; WOOD BIOMASS; KRAFT LIGNIN; CONVERSION; DEPOLYMERIZATION; GASIFICATION; CHEMICALS; CATALYSTS;
D O I
10.1016/j.supflu.2016.12.015
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The hydrothermal conversion of Kraft lignin (6 wt.%) in the presence of K2CO3 (1.7 wt.%) was studied as a function of temperature (T = 280-350 degrees C) and phenol mass fraction. (w(ph) = 0.0-9.7 wt.%). The process was carried out in a new batch reactor with injection of lignin slurry enabling fast heating of the biomass, effective control of reaction pressure, and withdrawal/quenching of the products. An aqueous phase and biocrude were obtained, both containing a broad spectrum of aromatic monomers and dimers. The former group consisted mostly of methoxybenzenes, guaiacols, catechols, and alkylphenols, while the latter included anisolic/phenolic dimers. For a given wph (3.4 wt.%), the total yield of monomeric aromatics (Y-T) was maximized at 320 degrees C. At T =300 degrees C and without phenol, YT was low, whereas it increased steeply up to w(ph) = 6.5 wt.%. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:28 / 39
页数:12
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