Enhancement of the production of light aromatics from poplar wood by combined approach of wet torrefaction pretreatment and catalytic fast pyrolysis using metal modified hierarchical zeolite

被引:0
|
作者
Cai W. [1 ]
Huang M. [1 ]
Zhu L. [1 ]
Zheng Y.-B. [1 ]
Cai B. [1 ]
Ma Z.-Q. [1 ]
机构
[1] College of Chemistry and Materials Engineering, National Engineering Research Center of Wood-based Resources Comprehensive Utilization, Zhejiang A & F University, Hangzhou
关键词
aromatics; biomass; catalytic fast pyrolysis; synergetic deoxygenation and demineralization; wet torrefaction; zeolite;
D O I
10.19906/j.cnki.JFCT.2023004
中图分类号
学科分类号
摘要
Light aromatics are extremely important building blocks in the chemical industry which can be produced from the catalytic fast pyrolysis (CFP) of biomass. In this work, wet torrefaction pretreatment (WTP) was employed to improve the quality of poplar wood (PW) in terms of the synergetic deoxygenation and demineralization. Then, metal-modified hierarchical HZSM-5 was prepared by the combined approach of NaOH desilication pretreatment and metal (Zn, Ga, and Fe) modification. At last, the CFP of torrefied PW was carried out by using the metalmodified hierarchical HZSM-5 as catalyst to produce light aromatics. Results showed that the deoxygenation and demineralization rates gradually increased with the increase of WTP temperature from 180 to 260 ℃, the maximum removal rates of oxygen, K, Mg, Ca, and Na were 47.96%, 90.99%, 86.65%, 66.09%, and 36.29%, respectively. NaOH desilication pretreatment and metal modification on HZSM-5 promoted the formation of light aromatics. The Zn-modified hierarchical HZSM-5 presented the highest yield of light aromatics. The yield of aromatics increased first with the raise of catalyst-to-torrefied PW ratio from 1:1 to 1∶3, then decreased slightly at the highest catalyst-to-torrefied PW ratio of 1∶5. At last, the operation parameter of WTP and CFP was optimized which the maximum yield of light aromatics was 7.83 × 107 p.a./mg at WTP temperature of 220 ℃, catalyst-to-biomass ratio of 3∶1, and CFP temperature of 850 ℃. © 2023 Science Press. All rights reserved.
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页码:1126 / 1136
页数:10
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共 33 条
  • [1] HUANG Ming, ZHU Liang, MA Zhong-qing, ZHOU Bing-liang, LIU Xiao-huan, YE Jie-wang, ZHAO Chao, Production of light aromatics from the fast pyrolysis of lignin catalyzed by metalmodified H-ZSM-5 zeolites[J], J Fuel Chem Technol, 49, 3, pp. 292-302, (2021)
  • [2] MA Zhong-qing, WANG Jun-hao, HUANG Ming, CAI Wei, XU Jia-long, YANG You-you, Effects of lignin species and catalyst addition on pyrolysis products[J], Trans CSAE, 36, 1, pp. 274-282, (2020)
  • [3] MA Hui-xia, ZHOU Feng, WU Guang, FU Jie, QIAO Kai, Catalytic fast pyrolysis of biomass to aromatics over hierarchical HZSM-5[J], J Chem Ind Eng, 71, 11, pp. 5200-5207, (2020)
  • [4] CEN K H, ZHUANG X H, GAN Z Y, MA Z Q, LI M, CHEN D Y., Effect of the combined pretreatment of leaching and torrefaction on the production of bio-aromatics from rice straw via the shape selective catalytic fast pyrolysis[J], Energy Reports, 7, pp. 732-739, (2021)
  • [5] ZHU Liang, HUANG Ming, DING Zi-xia, MA Zhong-qing, Production of light bio-aromatics from co-catalytic fast pyrolysis of torrefied bamboo and high-density polyethylene[J], J Fuel Chem Technol, 50, 8, pp. 993-1003, (2022)
  • [6] ZHANG Yu, XU Jia-jia, MA Zhong-qing, WANG Jun-hao, LI Wen-zhu, ZHANG Wen-biao, Pretreatment on characteristics of pyrolysis products for small diameter sympodial bamboo with torrefaction[J], J Zhejiang A & F Univ, 36, 5, pp. 981-989, (2019)
  • [7] ZHANG S P, SU Y H, XU D, ZHU S G, ZHANG H L, LIU X Z., Assessment of hydrothermal carbonization and coupling washing with torrefaction of bamboo sawdust for biofuels production[J], Bioresour Technol, 258, (2018)
  • [8] SMITH A M, SINGH S, ROSS A B., Fate of inorganic material during hydrothermal carbonization of biomass: Influence of feedstock on combustion behavior of hydrocar[J], Fuel, 169, (2016)
  • [9] HOEKMAN S K, BROCH A, FELIX L, FARTHING W., Hydrothermal carbonization (HTC) of loblolly pine using a continuous, reactive twin-screw extruder[J], Energy Convers Manage, 134, (2017)
  • [10] NAKASON K, PANYAPINYOPOL B, KANOKKANTAPONG V, VIRIYA-EMPIKUL N, KRAITHONG W, PAVASANT P., Hydrothermal carbonization of unwanted biomass materials: Effect of process temperature and retention time on hydrochar and liquid fraction[J], J Energy Inst, 91, 5, (2018)