Controllable production of liquid and solid biofuels by doping-free, microwave-assisted, pressurised pyrolysis of hemicellulose

被引:39
|
作者
Li, T. [1 ]
Remon, J. [1 ]
Shuttleworth, P. S. [2 ]
Jiang, Z. [3 ]
Fan, J. [1 ]
Clark, J. H. [1 ]
Budarin, V. L. [1 ]
机构
[1] Univ York, Dept Chem, Green Chem Ctr Excellence, York YO10 5DD, N Yorkshire, England
[2] CSIC, Inst Ciencia & Tecnol Polimeros, Dept Fis Polimeros Elastomeros & Aplicac Energet, C Juan de la Cierva 3, E-28006 Madrid, Spain
[3] Sichuan Univ, Coll Chem, Minist Educ, Key Lab Green Chem & Technol, Chengdu 610064, Sichuan, Peoples R China
基金
英国工程与自然科学研究理事会; 英国生物技术与生命科学研究理事会; “创新英国”项目;
关键词
Microwave; Pyrolysis; Hemicellulose; Bio-oil; Bio-char; BIO-OIL; 2ND-GENERATION BIOREFINERY; CORNCOB RESIDUE; BIOMASS; CONVERSION; CELLULOSE; ENERGY; LIGNIN; GASIFICATION; TEMPERATURE;
D O I
10.1016/j.enconman.2017.04.055
中图分类号
O414.1 [热力学];
学科分类号
摘要
Batch, pressurised microwave-assisted pyrolysis of hemicellulose in the absence of any external microwave absorber was found to be a promising route for the production of bio-based chemicals and biofuels. The experiments were conducted in a 10 mL batch reactor using a fixed power of 200 W employing different initial masses of xylan (0.1-0.7 g) for a maximum time, temperature and pressure of 10 min, 250 degrees C and 200 psi, respectively. The gas, bio-oil and solid (char) yields varied by 16-40%, 2-21% and 40-82%, respectively. Char production is preferential using a low amount of xylan (<0.25 g), while bio-oil production is favoured using a high amount of xylan (0.25-0.7 g). The effect of the sample mass is accounted for by the different physical state of the volatiles released during pyrolysis depending on the pressure attained during the experiment. This permits the process to be easily customised for the selective production of liquid (bio-oil) or solid (bio-char). Regarding the bio-oil, it is composed of a mixture of platform chemicals such as aldehydes, alkenes, phenols, polyaromatic hydrocarbons (PAHC), cyclic ketones and furans, with the composition varying depending on the initial mass of xylan. The char had a higher proportion of C together with a lower proportion of 0 than the original feedstock. Energy efficiencies of 100 and 26% were achieved for char and bio-oil production, respectively; thus leading to an increase in the HHV of the products (with respect to the original feedstock) of 52% for char and 19% for bio-oil. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:104 / 113
页数:10
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