Hydrotreatment of straw bio-oil from ablative fast pyrolysis to produce suitable refinery intermediates

被引:58
作者
Auersvald, Milos [1 ]
Shumeiko, Bogdan [1 ]
Vrtiska, Dan [1 ]
Straka, Petr [1 ]
Stas, Martin [1 ]
Simacek, Pavel [1 ]
Blazek, Josef [1 ]
Kubicka, David [1 ]
机构
[1] Univ Chem & Technol Prague, Dept Petr Technol & Alternat Fuels, Tech 5, Prague 16628, Czech Republic
关键词
Hydrotreatment; Straw bio-oil; Ablative fast pyrolysis (AFP); Biofuels; Sulphided catalysts; CATALYTIC HYDRODEOXYGENATION; MODEL-COMPOUND; O-REMOVAL; BIOMASS; PHOSPHIDE; DEACTIVATION; PHENOL; METAL; NI;
D O I
10.1016/j.fuel.2018.10.090
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
To meet the expected requirements of the proposed EU Renewable Energy Directive for the next decade (RED II), it is necessary to increase the availability of second-generation biofuels. One promising way of doing this involves using ablative fast pyrolysis units to transform an agricultural by-product, for example straw, into bio-oil. To obtain straw bio-oil suitable for processing in a typical refinery, we optimized the key parameters of its hydrotreatment. For the upgrading, a continuous flow reactor with a fixed bed of a commercial sulphide NiMo/Al2O3 catalyst was used. The reaction temperature and pressure were tested at 240-360 degrees C and 2-8 MPa, respectively. The reaction off-gas was analysed by GC-FID/TCD. A detailed physicochemical analysis of the products was carried out. Under most conditions tested, the product was separated into an aqueous and an organic phase. For the best products, > 85% of the feed energy content remained in the organic phase and a significant decrease in viscosity and acidity was achieved. The product prepared at 360 degrees C and 8 MPa was the only one completely miscible with straight-run gas oil and, thus, appears to be the most suitable for co-processing in a refinery.
引用
收藏
页码:98 / 110
页数:13
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