2015
DOI: 10.1016/j.biortech.2014.10.163
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Pressurized pyrolysis of dried distillers grains with solubles and canola seed press cake in a fixed-bed reactor

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Cited by 36 publications
(8 citation statements)
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“…In this sense, an increase in the mass flow rate of N2 for pressurized pyrolysis runs led to a reduction of the concentration of volatiles within the reactor, possibly resulting in a lower extent of secondary charring reactions. The decrease in the yield of biochar with pressure is in disagreement with some previous studies, which have reported on a higher production of biochar when the pressure was increased [9][10][11][12][13] as a consequence of an enhancement of the secondary charring reactions. However, it should be noted that these previous studies were carried out at a constant mass flow rate of inert gas (at NTP conditions) and, thus, the gas residence time increased as the pressure rose.…”
Section: Carbonization Efficiency and Distribution Of The Pyrolysis Pcontrasting
confidence: 96%
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“…In this sense, an increase in the mass flow rate of N2 for pressurized pyrolysis runs led to a reduction of the concentration of volatiles within the reactor, possibly resulting in a lower extent of secondary charring reactions. The decrease in the yield of biochar with pressure is in disagreement with some previous studies, which have reported on a higher production of biochar when the pressure was increased [9][10][11][12][13] as a consequence of an enhancement of the secondary charring reactions. However, it should be noted that these previous studies were carried out at a constant mass flow rate of inert gas (at NTP conditions) and, thus, the gas residence time increased as the pressure rose.…”
Section: Carbonization Efficiency and Distribution Of The Pyrolysis Pcontrasting
confidence: 96%
“…In other words, the gas residence time within the reactor was increased when the pyrolysis system was pressurized. Thus, most of the earlier studies have reported on an increment of the char and gas yields, at the expense of tar (i.e., organic condensable fraction), when both the pressure and gas residence time had been increased [9][10][11][12][13]. Particularly interesting are the results obtained at the Hawaii Natural Energy Institute (University of Hawaii at Manoa, USA), where a Flash Carbonization (FC) system was used to carbonize a number of agricultural residues.…”
Section: Introductionmentioning
confidence: 99%
“…Ates et al [38] for the pressurized pyrolysis of two biomass sources, seems to be contradictory with the higher extent of the secondary reactions of the primary volatile species, since both thermal cracking and dehydration processes can notably increase the production of water [19]. However, a higher consumption of water can also be promoted by pressure by means of an enhancement of several reactions: (1) steam reforming of volatile organic compounds and/or light hydrocarbons, (2) watergas-shift reaction (reaction #1 in Table 2), and (3) steam gasification (reaction #5 in Table 2).…”
Section: Pure N2 Atmospherementioning
confidence: 99%
“…De-oiled seedcake is a major by-product of the biodiesel industry that is usually obtained after the oil extraction from the Jatropha curcas, canola, and pennycress. The residual oil in seedcakes gives them a higher energy content than lignocellulosic materials [76]. Typical de-oiled seedcake contains lipids (2-20%), a good protein amount (10-40%), very high volatile matter (70-90%), and lower ash content (0.5-10%).…”
Section: Biomass Feedstock Availability and Economic Analysismentioning
confidence: 99%