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Energy Conversion and Management
journal homepage: www.elsevier.com/locate/enconman
Optimization of bio-oil production from solid digestate by microwave-
assisted liquefaction
M. Barbanera
a,b,
⁎
, C. Pelosi
c
, A.R. Taddei
d
, F. Cotana
b
a
Department of Economics, Engineering, Society and Business Organization, University of Tuscia, 01100 Viterbo, Italy
b
CIRIAF – Biomass Research Centre – Department of Engineering, Via G. Duranti 67, 06125 Perugia, Italy
c
Department of Economics, Engineering, Society and Business Organization, Laboratory of Diagnostics and Materials Science, University of Tuscia, 01100 Viterbo, Italy
d
Interdepartmental Centre of Electron Microscopy (C.I.M.E.), and Department of Environmental Sciences, University of Tuscia, 01100 Viterbo, Italy
ARTICLE INFO
Keywords:
Microwave
Liquefaction
Solid digestate
Bio-oil
Response Surface Methodology
ABSTRACT
Microwave-assisted direct liquefaction of solid digestate was carried out in polyethylene glycol and glycerol
employing sulfuric acid as catalyst, in order to convert it into a biofuel. Response Surface Methodology (RSM)
coupled with Box-Behnken Design (BBD) with a total of 15 individual experiments was used to optimize the
conditions of three independent variables (temperature, reaction time and solvent-to-biomass ratio) related to
the bio-oil yield, the higher heating value (HHV) of bio-oil and the energy use of microwave treatment.
Desirability function was employed to determine the optimal reaction conditions of the liquefaction process. The
results showed that at the optimal conditions the bio-oil yield, the HHV of bio-oil and energy use were re-
spectively 59.38%, 28.48 MJ/kg, and 115.93 Wh. The predicted responses showed a good compliance to the
obtained experimental data. The optimized bio-oil was further characterized using FTIR analysis while the
properties of the solid digestate and the liquefaction residue were analyzed by means of SEM analysis.
1. Introduction
Nowadays, global challenges related to resources depletion, air
pollution, and cost of oil require significant improvements in the search
of alternative renewable energy resources. Furthermore, since it is ex-
pected that the world energy demand will double by 2050 [1], the
research on biomass-based fuels is one of the trending strategies to
fulfill energy requirements. Currently, the significant increase of ex-
ploitation of anaerobic digestion plants for biogas or biomethane pro-
duction is leading to the development of a significant environmental
issue related to the digestate disposal [2]. Up to now, the solid fraction
of digestate has been mostly used as a biofertilizer without any further
processing because its contains high content of nutrients (N, P, K) and
organic matter [3]. However, its overuse can cause significant en-
vironmental threats to the soil matrix and to human beings [4] due to
ammonia emissions and nitrate and heavy metals leaching as well as
the presence of pathogens and land usage [5] Therefore, in order to
overcome these drawbacks it is necessary to develop new strategies for
sustainable recovery of solid digestate. Whereas the energy efficiency of
the anaerobic digestion process is rather low (33–50%) [5], digestate
could be conveniently employed for energy purposes. In most biogas
plants, digestate is separated into two fractions, liquid (rich in nitrogen)
and solid (rich in lignin), being the latter suitable for thermo-chemical
processes, such as pyrolysis, gasification and direct liquefaction, in
order to convert it into biofuels (e.g. bio-oil) or gas fuels (e.g. H
2
) [6].
However, pyrolysis process shows certain disadvantages, due to the
high operating temperature which could lead to cross-linking reactions
between hydrocarbons and aromatics, decreasing the bio-oil yield [7].
Besides the digestate remarkable ash content in digestate can cause
significant slagging and fouling problems during the gasification reac-
tions [8]. On the other hand, direct liquefaction of biomass has at-
tracted wide research interests since biomass can be successfully con-
verted into multifunctional bio-oil at milder temperatures and in
presence of solvents, such as phenol, monohydric alcohols and poly-
hydric alcohols, and acid or basic catalysts [9,10]. In the liquefaction
process, cellulose, hemicellulose and lignin are reduced into fragments
of smaller molecules but the effective reaction pathways are scarcely
detectable; it is assumed that polysaccharides are firstly degraded into
glycosides and then hydrolysed to form levulinic glycosides. Instead
lignin affects the recondensation reactions after the liquefaction step
leading to the formation of insoluble precipitates [11].
Microwave (MW) assisted liquefaction has been proven to be an
interesting alternative to conventional heating, because it allows to
obtain a uniform fast internal heating, to accelerate the kinetic reaction
https://doi.org/10.1016/j.enconman.2018.06.066
Received 11 April 2018; Received in revised form 28 May 2018; Accepted 18 June 2018
⁎
Corresponding author at: Department of Economics, Engineering, Society and Business Organization, University of Tuscia, 01100 Viterbo, Italy.
E-mail address: m.barbanera@unitus.it (M. Barbanera).
Energy Conversion and Management 171 (2018) 1263–1272
0196-8904/ © 2018 Elsevier Ltd. All rights reserved.
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