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Fuel Processing Technology
journal homepage: www.elsevier.com/locate/fuproc
Invited review article
Recent developments in lignocellulosic biomass catalytic fast pyrolysis:
Strategies for the optimization of bio-oil quality and yield
Xu Chen, Qingfeng Che, Shujuan Li, Zihao Liu, Haiping Yang
⁎
, Yingquan Chen, Xianhua Wang,
Jingai Shao, Hanping Chen
State Key Laboratory of Coal Combustion, Huazhong University of Science and Technology, 1037 Luoyu Road, 430074 Wuhan, PR China
ARTICLE INFO
Keywords:
Biomass
Catalytic fast pyrolysis
Bio-oil
High-quality
High-yield
ABSTRACT
Catalytic fast pyrolysis (CFP) is an attractive approach to convert biomass to high-quality bio-oil through the
deoxygenation of pyrolysis vapors in the form of H
2
O, CO, and CO
2
. However, the deoxygenation process comes
at the expense of bio-oil yield. This review begins with recent progress on lignocellulosic biomass pyrolysis
chemistry and techniques, and then focuses on the latest improvements to the design of advanced catalysts and
novel CFP processes. It was found that basic metal oxides (e.g., MgO and CaO) are promising alternative catalysts
to zeolites (such as ZSM-5) with respect to the preferred decarboxylation reaction, which merits additional
investigation on their structure-function relationships in the future. Additionally, catalytic co-pyrolysis of bio-
mass with waste plastics or waste tires over zeolites is an attractive approach from the viewpoint of preferred
dehydration reactions and the high-value utilization of solid wastes. However, the physicochemical properties of
the catalysts should be further adjusted. Furthermore, in spite of many interesting results reported in the lit-
erature, quantitatively analysis and uniform data presentation format is necessary for the further development of
CFP techniques.
1. Introduction
With the increasing concerns of the environmental pollution and the
energy crisis caused by fossil fuels overuse, the development of clean
and renewable energy alternatives is extremely urgent. Lignocellulosic
biomass, the only one carbon-containing renewable energy resource,
has been identified as an attractive feedstock for producing renewable
fuels and chemicals due to the potential of zero CO
2
emission, abundant
availability and low cost [1]. According to the International Energy
Agency, bioenergy would account for 10% of the world's primary en-
ergy supply by 2035 [2].
To cleanly and efficiently utilize the lignocellulosic biomass re-
sources, the development of suitable conversion techniques is particu-
larly important [3]. Fast pyrolysis is a promising approach as it can
convert lignocellulosic biomass into liquid products in a short period,
and the resulting pyrolysis liquid, called bio-oil, can reach yields of up
to 65–75 wt% [4]. For a better understanding of biomass pyrolysis
technology and guiding bio-oil production, extensive research efforts
have been conducted over the past years with focus on biomass pyr-
olysis mechanism [5–7], and meanwhile, novel pyrolysis techniques,
such as grinding pyrolysis, microwave pyrolysis, solar pyrolysis, and
stepwise pyrolysis, etc., have also been developed [8–11]. Hence, there
is a need for a comprehensive study to summarize the state-of-the-art
advances in the aspects of biomass pyrolysis mechanism and technique.
In spite of these achievements on biomass pyrolysis chemistry and
technique, the crude bio-oil from biomass fast pyrolysis still remains a
high oxygen content, which contributes to instability, low heating va-
lues, high viscosities and high acidity; and it is unsuitable for direct use
in the existing petroleum-based infrastructure [12]. Therefore, the
crude bio-oil must be further upgraded to reduce the undesirable
components and increase the content of useful compounds. Hydro-
deoxygenation (HDO) of bio-oil [13] or pyrolysis vapors [14,15] is an
effective bio-oil upgrading process. However, the harsh reaction con-
ditions (high pressure), the use of high-cost noble catalysts or bifunc-
tional metal-acid catalysts (such as transition metal carbides, nitrides,
and phosphide catalysts), and the considerable consumption of hy-
drogen blocked the development and utilization of HDO for bio-oil
upgrading [16]. Alternatively, catalytic upgrading of the pyrolysis va-
pors under inert atmosphere and atmospheric pressure, or catalytic fast
pyrolysis process (CFP), is the other one promising approach to bio-oil
upgrading [17,18].
With directly upgrading of uncondensed vapors using suitable
https://doi.org/10.1016/j.fuproc.2019.106180
Received 1 May 2019; Received in revised form 5 August 2019; Accepted 5 August 2019
⁎
Corresponding author.
E-mail address: yhping2002@163.com (H. Yang).
Fuel Processing Technology 196 (2019) 106180
0378-3820/ © 2019 Elsevier B.V. All rights reserved.
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