Effect of process parameters on supercritical liquefaction of Xanthium strumarium for bio-oil production

被引:12
|
作者
Genel, Yasar [1 ]
Durak, Halil [2 ]
Aysu, Tevfik [3 ]
Genel, Ilyas [1 ]
机构
[1] Yuzuncu Yil Univ, Fac Educ, Dept Chem, TR-65080 Van, Turkey
[2] Yuzuncu Yil Univ, Vocat Sch Hlth Serv, TR-65080 Van, Turkey
[3] Yuzuncu Yil Univ, Fac Sci, Dept Chem, TR-65080 Van, Turkey
来源
关键词
Energy; Biomass; Bio-oil; Supercritical fluid; DIRECT THERMOCHEMICAL LIQUEFACTION; HYDROTHERMAL LIQUEFACTION; STRUCTURAL-ANALYSIS; BIOMASS; PYROLYSIS; ETHANOL; WATER; TEMPERATURE; CELLULOSE; EXTRACTION;
D O I
10.1016/j.supflu.2016.04.009
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Supercritical liquefaction process is used for producing energy from biomass. The common reaction conditions for supercritical liquefaction process are the 240-380 degrees C temperature range and 5-20 MPa pressure values range. Xanthium strumarium liquefaction experiments were performed in a cylindrical reactor (75 mL) in organic solvents (acetone, ethanol, methanol) under supercritical conditions with (zinc oxide, calcium hydroxide) and without catalyst at the temperatures of 250, 275 and 300 degrees C. The produced liquids at 300 degrees C in liquefaction were analyzed and characterized by Elemental, GC-MS and FT-IR. 36, 37 and 50 different types of compounds were identified by GC-MS obtained in acetone, ethanol and methanol respectively. The liquid product efficiency has been obtained at 300 degrees C in acetone with zinc oxide catalyst (74.80%). The highest HHV value has been calculated as 32.16 MJ/kg with calcium hydroxide catalyst in acetone. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:42 / 53
页数:12
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