Thermal and catalytic fast hydropyrolysis of lignin: Optimization for selective production of aromatics using high-pressure tandem μ-reactor - gas chromatography/mass spectrometry

被引:11
作者
Ma, Chuan [1 ]
Kumagai, Shogo [2 ,3 ]
Watanabe, Atsushi [2 ,4 ]
Watanabe, Chuichi [4 ]
Teramae, Norio [4 ,5 ]
Yoshioka, Toshiaki [2 ]
Kim, Young -Min [6 ]
机构
[1] Chongqing Univ, Sch Energy & Power Engn, Key Lab Low Grade Energy Utilizat Technol & Syst, Minist Educ, Chongqing 400044, Peoples R China
[2] Tohoku Univ, Grad Sch Environm Studies, 6o-07 Aoba,Aoba Ku, Sendai, Miyagi 9808579, Japan
[3] Tohoku Univ, Div Estab Frontier Sci Org Adv Studies, 2-1-1 Katahira,Aoba Ku, Sendai 9808577, Japan
[4] Frontier Labs Ltd, 4-16-02 Saikon, Koriyama, Fukushima 9638862, Japan
[5] Tohoku Univ, Grad Sch Sci, Dept Chem, Aoba Ku, Sendai, Miyagi 9808578, Japan
[6] Daegu Univ, Dept Environm Engn, Gyeongbuk 38453, South Korea
关键词
Lignin; Catalytic hydropyrolysis; Condition optimization; HZSM-5; BTX; FAST PYROLYSIS; IN-SITU; BIOMASS; HZSM-5; FUELS; VAPOR; WOOD;
D O I
10.1016/j.cej.2023.147524
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Hydropyrolysis is a promising route for converting biomass into valuable chemicals. A high-pressure tandem mu-reactor - gas chromatography/mass spectrometry was used to study the pyrolysis of lignin and probe the ef-fects of reaction atmosphere (H2 vs He), temperature, catalyst (HZSM-5) presence/absence, and pressure on product yields and distributions. Hydropyrolysis favored the demethoxylation and demethylation of guaiacyl-derived intermediates, generating catechol-and phenol-type compounds. The yields of guaiacyl-and catechol-type compounds decreased with increasing temperature and H2 pressure. The products formed at the highest examined temperature (700 degrees C) and H2 pressure (3.0 MPa) were dominated by phenol-type compounds, mon-oaromatic hydrocarbons (MAHs), and polycyclic aromatic hydrocarbons (PAHs). The substantial decrease in char yield with increasing H2 pressure at 700 degrees C indicated that active hydrogen radicals enhanced the cracking of lignin macromolecules and suppressed the condensation reactions to form char at high temperatures. HZSM-5 exhibited considerable hydrocracking activity for converting lignin pyrolysis vapor into aromatics, with an in-crease in H2 pressure further improving the formation of benzene, toluene, and xylenes (BTX) at the expense of phenolics. However, high catalytic upgrading temperatures favored the coupling reactions in the hydrocarbon pool, promoting the formation of PAHs. Evolved gas analysis showed that lignin hydropyrolysis involved two stages (at 250-500 and 500-800 degrees C), suggesting that the labile fraction of the nascent char underwent further hydrocracking at high pressure and temperature. The high production of BTX and naphthalenes through catalytic hydropyrolysis of lignin provides a promising route for the valorization of lignin-rich resources.
引用
收藏
页数:9
相关论文
共 45 条
[31]   Production of hydrocarbon fuels from biomass using catalytic pyrolysis under helium and hydrogen environments [J].
Thangalazhy-Gopakumar, Suchithra ;
Adhikari, Sushil ;
Gupta, Ram B. ;
Tu, Maobing ;
Taylor, Steven .
BIORESOURCE TECHNOLOGY, 2011, 102 (12) :6742-6749
[32]   Parametric effect of biomass partial hydropyrolysis process in a downer reactor to co-produce high-quality tar and syngas [J].
Tian, Yuanyu ;
Li, Jie ;
Wei, Wei ;
Zong, Peijie ;
Zhang, Di ;
Zhu, Yanan ;
Qiao, Yingyun .
BIORESOURCE TECHNOLOGY, 2021, 320
[33]   Influence of fast pyrolysis conditions on yield and structural transformation of biomass chars [J].
Trubetskaya, Anna ;
Jensen, Peter Arendt ;
Jensen, Anker Degn ;
Steibel, Markus ;
Spliethoff, Hartmut ;
Glarborg, Peter .
FUEL PROCESSING TECHNOLOGY, 2015, 140 :205-214
[34]   Valorization of Biomass: Deriving More Value from Waste [J].
Tuck, Christopher O. ;
Perez, Eduardo ;
Horvath, Istvan T. ;
Sheldon, Roger A. ;
Poliakoff, Martyn .
SCIENCE, 2012, 337 (6095) :695-699
[35]   Hydrodeoxygenation kinetics of syringol, guaiacol and phenol over H-ZSM-5 [J].
Venkatesan, Kavimonica ;
Krishna, J. V. Jayarama ;
Anjana, S. ;
Selvam, Parasuraman ;
Vinu, Ravikrishnan .
CATALYSIS COMMUNICATIONS, 2021, 148
[36]   Selective production of aromatic hydrocarbons from lignocellulosic biomass via catalytic fast-hydropyrolysis using W2C/γ-Al2O3 [J].
Venkatesan, Kavimonica ;
He, Songbo ;
Seshan, Kulathu ;
Selvam, Parasuraman ;
Vinu, Ravikrishnan .
CATALYSIS COMMUNICATIONS, 2018, 110 :68-73
[37]   Noncatalytic hydropyrolysis of lignin in a high pressure micro-pyrolyzer [J].
Wang, Huiyuan ;
Li, Tan ;
Su, Jing ;
Miao, Kai ;
Wang, Kaige .
FUEL PROCESSING TECHNOLOGY, 2022, 233
[38]   Comparison of in-situ and ex-situ catalytic pyrolysis in a micro-reactor system [J].
Wang, Kaige ;
Johnston, Patrick A. ;
Brown, Robert C. .
BIORESOURCE TECHNOLOGY, 2014, 173 :124-131
[39]   Catalytic pyrolysis of lignin in a cascade dual-catalyst system of modified red mud and HZSM-5 for aromatic hydrocarbon production [J].
Wang, Shaoqing ;
Li, Zhihe ;
Bai, Xueyuan ;
Yi, Weiming ;
Fu, Peng .
BIORESOURCE TECHNOLOGY, 2019, 278 :66-72
[40]   Downstream processing of lignin derived feedstock into end products [J].
Wong, Sie Shing ;
Shu, Riyang ;
Zhang, Jiaguang ;
Liu, Haichao ;
Yan, Ning .
CHEMICAL SOCIETY REVIEWS, 2020, 49 (15) :5510-5560