2021
DOI: 10.1016/j.jaap.2021.105270
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Effect of fractional condensation system coupled with an auger pyrolizer on bio-oil composition and properties

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Cited by 4 publications
(1 citation statement)
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“…Fine particles were separated from the pyrolysis gas by an internal deflector 10.2 cm in diameter and 10.5 cm long placed at the reactor exit. The gas was evacuated through an opening in the top part of the tank and directed towards the countercurrent condensation system composed of three condensers as described by Álvarez-Chávez et al [17], one at 120 • C to recover the oily phase of bio-oil, another for the recovery of the aqueous phase, and the last at 4 • C for the recovery of the remaining aqueous phase. The reported yields (Y) are calculated on wet basis according to Equations ( 4)-( 6) as follows: Y% biochar = mass of char/mass of biomass,…”
Section: Pyrolysis Operating Conditionsmentioning
confidence: 99%
“…Fine particles were separated from the pyrolysis gas by an internal deflector 10.2 cm in diameter and 10.5 cm long placed at the reactor exit. The gas was evacuated through an opening in the top part of the tank and directed towards the countercurrent condensation system composed of three condensers as described by Álvarez-Chávez et al [17], one at 120 • C to recover the oily phase of bio-oil, another for the recovery of the aqueous phase, and the last at 4 • C for the recovery of the remaining aqueous phase. The reported yields (Y) are calculated on wet basis according to Equations ( 4)-( 6) as follows: Y% biochar = mass of char/mass of biomass,…”
Section: Pyrolysis Operating Conditionsmentioning
confidence: 99%