Using Isopropanol as a Capping Agent in the Hydrothermal Liquefaction of Kraft Lignin in Near-Critical Water

被引:8
作者
Ahlbom, Anders [1 ]
Maschietti, Marco [2 ]
Nielsen, Rudi [2 ]
Lyckeskog, Huyen [1 ]
Hasani, Merima [1 ]
Theliander, Hans [1 ]
机构
[1] Chalmers Univ Technol, Dept Chem & Chem Engn, SE-41296 Gothenburg, Sweden
[2] Aalborg Univ, Dept Chem & Biosci, Niels Bohrs Vej 8, DK-6700 Esbjerg, Denmark
关键词
hydrothermal liquefaction; Kraft lignin; isopropanol; alkaline catalyst; ACID-CATALYZED DEPOLYMERIZATION; SUPERCRITICAL WATER; SUBCRITICAL WATER; ALKALI LIGNIN; CONVERSION; DEGRADATION; BIOMASS; PHENOL; ALKYLATION; CHEMICALS;
D O I
10.3390/en14040932
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
In this study, Kraft lignin was depolymerised by hydrothermal liquefaction in near-critical water (290-335 degrees C, 250 bar) using Na2CO3 as an alkaline catalyst. Isopropanol was used as a co-solvent with the objective of investigating its capping effect and capability of reducing char formation. The resulting product, which was a mixture of an aqueous liquid, containing water-soluble organic compounds, and char, had a lower sulphur content than the Kraft lignin. Two-dimensional nuclear magnetic resonance studies of the organic precipitates of the aqueous phase and the char indicated that the major lignin bonds were broken. The high molar masses of the char and the water-soluble organics, nevertheless, indicate extensive repolymerisation of the organic constituents once they have been depolymerised from the lignin. With increasing temperature, the yield of char increased, although its molar mass decreased. The addition of isopropanol increased the yield of the water-soluble organic products and decreased the yield of the char as well as the molar masses of the products, which is indicative of a capping effect.
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页数:16
相关论文
共 46 条
[1]   Continuous catalytic depolymerisation and conversion of industrial kraft lignin into low-molecular-weight aromatics [J].
Abdelaziz, Omar Y. ;
Li, Kena ;
Tuna, Per ;
Hulteberg, Christian P. .
BIOMASS CONVERSION AND BIOREFINERY, 2018, 8 (02) :455-470
[2]   A review on process conditions for optimum bio-oil yield in hydrothermal liquefaction of biomass [J].
Akhtar, Javaid ;
Amin, Nor Aishah Saidina .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2011, 15 (03) :1615-1624
[3]   Hydrothermal liquefaction of lignin in near-critical water in a new batch reactor: Influence of phenol and temperature [J].
Arturi, Katarzyna R. ;
Strandgaard, Morten ;
Nielsen, Rudi P. ;
Sogaard, Erik G. ;
Maschietti, Marco .
JOURNAL OF SUPERCRITICAL FLUIDS, 2017, 123 :28-39
[4]   Hydrothermal liquefaction of kraft lignin in sub-critical water: the influence of the sodium and potassium fraction [J].
Belkheiri, Tallal ;
Andersson, Sven-Ingvar ;
Mattsson, Cecilia ;
Olausson, Lars ;
Theliander, Hans ;
Vamling, Lennart .
BIOMASS CONVERSION AND BIOREFINERY, 2018, 8 (03) :585-595
[5]   Hydrothermal Liquefaction of Kraft Lignin in Subcritical Water: Influence of Phenol as Capping Agent [J].
Belkheiri, Tallal ;
Andersson, Sven-Ingvar ;
Mattsson, Cecilia ;
Olausson, Lars ;
Theliander, Hans ;
Vamling, Lennart .
ENERGY & FUELS, 2018, 32 (05) :5923-5932
[6]  
Belkheiri T, 2014, CELL CHEM TECHNOL, V48, P813
[7]  
Berlin A., 2014, Bioenergy Research: Advances and Applications, P315, DOI DOI 10.1016/B978-0-444-59561-4.00018-8
[8]  
Bobleter O., 1979, Cellul. Chem. Technol, V13, P583
[9]   Alkylation reactions in near-critical water in the absence of acid catalysts [J].
Chandler, K ;
Deng, FH ;
Dillow, AK ;
Liotta, CL ;
Eckert, CA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (12) :5175-5179
[10]   Hydrothermal degradation of alkali lignin to bio-phenolic compounds in sub/supercritical ethanol and water-ethanol co-solvent [J].
Cheng, Shuna ;
Wilks, Carolynne ;
Yuan, Zhongshun ;
Leitch, Mathew ;
Xu, Chunbao .
POLYMER DEGRADATION AND STABILITY, 2012, 97 (06) :839-848