Abstract:Catalytic fast pyrolysis (CFP) of beech wood chips was undertaken in a laboratory-scale fixed bed reactor equipped with a biomass semi-continuous dispenser. During pyrolysis, chars are retained on a quartz frit and the pyrolytic vapors are entrained through a fixed-bed catalyst to be converted. Several acidic catalysts such as zeolites H-Beta, zeolite HMFI and 5% Ni supported on HMFI were screened in this equipment. The Ni/HMFI catalyst was also tested in the presence of 1 vol.% of hydrogen in the feed stream.… Show more
“…The use of all three ZSM-5 zeolite catalysts induced the production of ethane, ethylene, propane and propylene which were not produced by the non-catalytic pyrolysis. The production of these gases is indicative of enhanced cracking and dealkylation reactions catalyzed by ZSM-5 in accordance with its performance in biomass fast pyrolysis (Mullen and Boateng, 2010 ; Stephanidis et al, 2011 ; Wang et al, 2014 ; Margeriat et al, 2018 ). As discussed below, ethylene and propylene serve as precursors for the production of aromatics in the channels of ZSM-5.…”
The valorization of lignin that derives as by product in various biomass conversion processes has become a major research and technological objective. The potential of the production of valuable mono-aromatics (BTX and others) and (alkyl)phenols by catalytic fast pyrolysis of lignin is investigated in this work by the use of ZSM-5 zeolites with different acidic and porosity characteristics. More specifically, conventional microporous ZSM-5 (Si/Al = 11.5, 25, 40), nano-sized (≤20 nm, by direct synthesis) and mesoporous (9 nm, by mild alkaline treatment) ZSM-5 zeolites were tested in the fast pyrolysis of a softwood kraft lignin at 400–600°C on a Py/GC-MS system and a fixed-bed reactor unit. The composition of lignin (FT-IR, 2D HSQC NMR) was correlated with the composition of the thermal (non-catalytic) pyrolysis oil, while the effect of pyrolysis temperature and catalyst-to-lignin (C/L) ratio, as well as of the Si/Al ratio, acidity, micro/mesoporosity and nano-size of ZSM-5, on bio-oil composition was thoroughly investigated. It was shown that the conventional microporous ZSM-5 zeolites are more selective toward mono-aromatics while the nano-sized and mesoporous ZSM-5 exhibited also high selectivity for (alkyl)phenols. However, the nano-sized ZSM-5 zeolite exhibited the lowest yield of organic bio-oil and highest production of water, coke and non-condensable gases compared to the conventional microporous and mesoporous ZSM-5 zeolites.
“…The use of all three ZSM-5 zeolite catalysts induced the production of ethane, ethylene, propane and propylene which were not produced by the non-catalytic pyrolysis. The production of these gases is indicative of enhanced cracking and dealkylation reactions catalyzed by ZSM-5 in accordance with its performance in biomass fast pyrolysis (Mullen and Boateng, 2010 ; Stephanidis et al, 2011 ; Wang et al, 2014 ; Margeriat et al, 2018 ). As discussed below, ethylene and propylene serve as precursors for the production of aromatics in the channels of ZSM-5.…”
The valorization of lignin that derives as by product in various biomass conversion processes has become a major research and technological objective. The potential of the production of valuable mono-aromatics (BTX and others) and (alkyl)phenols by catalytic fast pyrolysis of lignin is investigated in this work by the use of ZSM-5 zeolites with different acidic and porosity characteristics. More specifically, conventional microporous ZSM-5 (Si/Al = 11.5, 25, 40), nano-sized (≤20 nm, by direct synthesis) and mesoporous (9 nm, by mild alkaline treatment) ZSM-5 zeolites were tested in the fast pyrolysis of a softwood kraft lignin at 400–600°C on a Py/GC-MS system and a fixed-bed reactor unit. The composition of lignin (FT-IR, 2D HSQC NMR) was correlated with the composition of the thermal (non-catalytic) pyrolysis oil, while the effect of pyrolysis temperature and catalyst-to-lignin (C/L) ratio, as well as of the Si/Al ratio, acidity, micro/mesoporosity and nano-size of ZSM-5, on bio-oil composition was thoroughly investigated. It was shown that the conventional microporous ZSM-5 zeolites are more selective toward mono-aromatics while the nano-sized and mesoporous ZSM-5 exhibited also high selectivity for (alkyl)phenols. However, the nano-sized ZSM-5 zeolite exhibited the lowest yield of organic bio-oil and highest production of water, coke and non-condensable gases compared to the conventional microporous and mesoporous ZSM-5 zeolites.
“…Energy & Fuels A labscale pyrolytic setup already described previously 10 was used. The wood chips were dried at 110 °C for 1.5 h before being placed in a gastight hopper and kept under N 2 .…”
Section: Methodsmentioning
confidence: 99%
“…Numerous studies investigated the effect of different parameters of pyrolysis, such as the temperature, heating rate, particle size, reactor configuration, residence time, and presence and properties of catalysts; − other works reported the impact of mixing the wood with different materials, such as plastics, agricultural residues, and municipal solid waste. − The pyrolysis of demolition wood in a fluidized bed reactor has been mentioned as early as 2005, but the authors reported mostly experiments using pristine woods (pine, beech, and bamboo) and only experiment using demolition wood, which was simply compared in terms of liquid and char yields. Hwang et al carried out the pyrolysis of different municipal solid wastes, including wood chips (obtained from construction and demolition waste) and mixtures of paper/wood/plastics, at 500, 700, and 900 °C, the highest temperatures more closely related to gasification conditions.…”
The use of pyrolysis oils from demolition woods is an interesting option to produce fuels or chemicals from waste wood. This work investigated the effect of paints and varnish that contain various potential contaminants on the properties of bio-oils obtained by thermal pyrolysis of wood or after ex situ catalysis of the pyrolysis vapors using a HZSM-5 catalyst. The paints and varnish were analyzed, and their main components were identified. Clean beech wood samples were impregnated with commercial paints and varnish and also individually with the main inorganic compounds (TiO 2 , CaCO 3 , and BaSO 4 ) found in the paints and varnish. These contaminated wood samples were pyrolyzed, and the gas, liquid, and solid products formed were thoroughly characterized and compared to the products obtained from clean wood. The results show that the mineral contaminants remained in the chars and that the pyrolysis oils obtained by thermal pyrolysis were not significantly modified by the presence of contaminants on the wood. In ex-situ-catalyzed pyrolysis experiments, the HZSM-5 catalyst promoted the formation of some fully deoxygenated aromatic compounds, which were not obtained without a catalyst. However, the bio-oil produced from wood impregnated with commercial paints and varnish contained less fully deoxygenated compounds. This effect was not related to the mineral compounds present in the paints and varnish and could originate from the polymeric organic components present in their formulations.
Raw
pyrolysis bio-oils can be used as liquid biofuels for district
heating or as raw materials for producing O-containing substances.
Additionally, they can be upgraded using different processes to obtain
products with promising potential to be used as advanced liquid transportation
biofuels. The more widespread use of the raw and upgraded bio-oils
is associated with the detailed knowledge of their chemical composition.
The chemical characterization of both the raw and upgraded bio-oils
is challenging as bio-oils contain thousands of different, mostly
O-containing, chemicals. One of the most critical problems in bio-oil
analytics is identifying currently unknown bio-oil compounds, which
can be achieved using powerful techniques such as two-dimensional
gas chromatography (2D-GC). 2D-GC allows one to analyze volatile and
semivolatile bio-oil compounds and provides much more detailed analytical
information due to its higher chromatographic resolution than conventional
one-dimensional GC. This review aims to summarize and critically evaluate
the studies devoted to the 2D-GC characterization of pyrolysis bio-oils.
Thermal and catalytic raw pyrolysis bio-oils and hydrotreated bio-oils
are of interest to this review. Additionally, the strategies and goals
for further research are outlined.
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