Investigation of In-Situ and Ex-Situ Catalytic Pyrolysis Upgrading of Pine Using Thermo-Gravimetric Analysis and a Fixed-Bed Reactor System

被引:8
作者
Zheng, Yunwu [1 ,2 ]
Wang, Fei [1 ]
Yang, Xiaoqing [1 ]
Liu, Can [1 ]
Huang, Yuanbo [1 ]
Gu, Jiyou [2 ]
Zheng, Zhifeng [1 ]
机构
[1] Southwest Forestry Univ, Coll Mat Engn, Univ Key Lab Biomass Chem Refinery & Synth, Kunming 650224, Yunnan, Peoples R China
[2] Northeast Forestry Univ, Coll Mat Sci & Engn, Minist Educ, Key Lab Biobased Mat Sci & Technol, Harbin 150040, Heilongjiang, Peoples R China
关键词
Catalytic Pyrolysis Upgrading; In-Situ versus Ex-Situ; Aromatic; HZSM-5; Catalyst; Kinetics; AROMATIC-HYDROCARBONS; ZSM-5; BIOMASS; VAPORS; MICROWAVE;
D O I
10.1166/jbmb.2017.1689
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
To determine the influence of process parameters on the preparation of aromatic compounds from biomass by catalytic pyrolysis, in situ and ex situ catalytic pyrolysis processes were compared using TGA and a fixed-bed reactor. At the same time, BET, TEM and XRD were used to analyze the characteristic of HZSM-5 catalyst, and GC-MS, FTIR and elemental analysis were used to analyze the composition and selectivity of bio-oil. The results showed the following: catalyst addition can clearly promote the dehydration reaction of the initial stage, which can effectively reduce the activation energy and the steric hindrance effect, accelerate the reaction rate, increase the conversion of wood powder (the conversion rate increased from 70.39% to 94.07%), and reduce the amount of residual carbon; for different catalytic pyrolysis processes, the composition and selectivity of the bio-oil vary: higher permanent gas yields, higher aromatic contents and a higher selectivity to benzene and toluene in the bio-oil were observed from the ex situ catalytic pyrolysis upgrading, and the deoxidation effect was better, however, higher yields of the bio-oil and a higher selectivity to C10+ polycyclic aromatic hydrocarbon were recorded during in situ catalytic pyrolysis; moreover, a higher temperature is conducive to the dealkylation reaction, and it increased the selectivity of non-substituted aromatics, while a low temperature caused the alkylation reaction to increase, which increased the selectivity of the substituted aromatics; at a pyrolysis temperature of 450 degrees C and a catalytic temperature of 500 degrees C, the ratio of the biomass to catalyst was 1: 2, the contents of single ring aromatics and residues reached 69% and 28.95%, respectively, and the calorific value reached 31.74 MJ/Kg; in comparison, at a pyrolysis temperature of 450 degrees C, the in situ catalytic pyrolysis of biomass only produces 27.51% and 30.01% light aromatic and residues, respectively.
引用
收藏
页码:400 / 413
页数:14
相关论文
共 45 条
[1]   THE PYROLYSIS KINETICS OF BAGASSE AT LOW HEATING RATES [J].
AIMAN, S ;
STUBINGTON, JF .
BIOMASS & BIOENERGY, 1993, 5 (02) :113-120
[2]  
Biddy M., 2013, PNNL22317 NAT REN EN, P717
[3]  
Caicedo-Realpe R., 2010, MICROPOR MESOPOR MAT, V128, P1
[4]   Catalytic fast pyrolysis of glucose with HZSM-5: The combined homogeneous and heterogeneous reactions [J].
Carlson, Torren R. ;
Jae, Jungho ;
Lin, Yu-Chuan ;
Tompsett, Geoffrey A. ;
Huber, George W. .
JOURNAL OF CATALYSIS, 2010, 270 (01) :110-124
[5]   A unified correlation for estimating HHV of solid, liquid and gaseous fuels [J].
Channiwala, SA ;
Parikh, PP .
FUEL, 2002, 81 (08) :1051-1063
[6]   Degradation and Redeposition of the Chemical Components of Aspen Wood during Hot Water Extraction [J].
Chen, Haiyan ;
Fu, Yingjuan ;
Wang, Zhaojiang ;
Qin, Menghua .
BIORESOURCES, 2015, 10 (02) :3005-3016
[7]  
Cheng Y. T., 2012, ANGEW CHEM, V124, P6
[8]  
Cheng Y. T., 2012, ANGEW CHEM INT EDIT, V51, P44
[9]   Production of targeted aromatics by using Diels-Alder classes of reactions with furans and olefins over ZSM-5 [J].
Cheng, Yu-Ting ;
Huber, George W. .
GREEN CHEMISTRY, 2012, 14 (11) :3114-3125
[10]   Chemistry of Furan Conversion into Aromatics and Olefins over HZSM-5: A Model Biomass Conversion Reaction [J].
Cheng, Yu-Ting ;
Huber, George W. .
ACS CATALYSIS, 2011, 1 (06) :611-628