Effect of low temperature hydrothermal liquefaction on catalytic hydrodenitrogenation of algae biocrude and model macromolecules

被引:64
作者
Costanzo, William [1 ]
Hilten, Roger [1 ]
Jena, Umakanta [1 ]
Das, K. C. [1 ]
Kastner, James R. [1 ]
机构
[1] Univ Georgia, Coll Engn, Biochem Engn, Athens, GA 30602 USA
来源
ALGAL RESEARCH-BIOMASS BIOFUELS AND BIOPRODUCTS | 2016年 / 13卷
关键词
Algae; Fuels; Heteroatoms; Hydrothermal liquefaction; Catalyst; Hydrodenitrogenation; Hydrodeoxygenation; THERMOCHEMICAL LIQUEFACTION; MICROALGAE CULTIVATION; OIL; BIOMASS; HYDRODEOXYGENATION; NITROGEN; ACIDS; PETROLEUM; REACTOR; WATER;
D O I
10.1016/j.algal.2015.11.009
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Staged, low and high-temperature subcritical liquefaction were used to pretreat algae and generate a biocrude primarily characterized by free fatty acids and unsaturated hydrocarbons with reduced nitrogen heteroatom levels. Subsequently, catalytic hydrodenitrogenation and deoxygenation (HDN/HDO) was conducted using ruthenium (5% Ru/carbon) and cobalt molybdenum catalysts. Ru on carbon was the most effective HDO catalyst and generated the lowest level of nitrogen and heteroatoms in the resulting oil. A CoMo-S catalyst generated higher nitrogen and heteroatom levels, and resulted in a higher TAN value and lower heating value, probably due to the low sulfur levels in the biocrude. The highest quality oil was generated from a raceway strain using Ru/C and HTL pretreatment (225 degrees C, 15 min) with a repeated batch HDN/HDO step (3.24% N, 8.2% O, TAN of 12, 1.25% water, HHV 40 MJ/kg) and had a boiling point range of similar to 20% kerosene, similar to 30% distillate fuel oil, and similar to 50% gas oil. A 57% reduction in nitrogen content of the oil was realized when repeated HDN/HDO was coupled with HTL pretreatment using Ru/C (4.3 wt.%N), relative to 7.5%N for single stage HTL/HDO. Final yields for the highest quality oil generated via the coupled HTL/HDO process ranged from 15 to 22%. Recovery and reuse of the catalyst (Ru/C) resulted in a significant decline in activity potentially caused by coking and metals deposition. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:53 / 68
页数:16
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