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Featured researches published by Melisa Bertero.


Bioresource Technology | 2013

Conversion of pine sawdust bio-oil (raw and thermally processed) over equilibrium FCC catalysts

Melisa Bertero; Ulises Sedran

A raw bio-oil from pine sawdust, the liquid product from its thermal conditioning and a synthetic bio-oil composed by eight model compounds representing the main chemical groups in bio-oils, were converted thermally and over a commercial equilibrium FCC catalyst. The experiments were performed in a fixed bed reactor at 500 °C. The highest hydrocarbon yield (53.5 wt.%) was obtained with the conditioned liquid. The coke yields were significant in all the cases, from 9 to 14 wt.%. The synthetic bio-oil produced lesser hydrocarbons and more oxygenated compounds and coke than the authentic feedstocks from biomass. The previous thermal treatment of the raw bio-oil had the positive effects of increasing 25% the yield of hydrocarbons, decreasing 55% the yield of oxygenated compounds and decreasing 20% the yield of coke, particularly the more condensed coke.


Archive | 2018

Pyrolysis Products from Residues of Palm Oil Industry

Melisa Bertero; Juan Rafael García; Marisa Falco; Ulises Sedran; Khoirun Nisa Mahmud; Suzami Junaidah Ariffin; Ani Idris; Zainul Akmar Zakaria

Palm kernel shell (PKS) and empty fruit bunches, both raw (EFB-R) and pretreated by means of autoclaving (EFB-A) and microwave (EFB-M), were pyrolyzed in a fixed-bed stainless steel reactor at 550 °C. The yield of the water-soluble liquid fraction (pyroligneous acid, PA) in the pyrolysis of PKS was 26%wt. (dry basis) and in the range of 16–46%wt. when different EFB were used. The yield of insoluble liquid fraction (bio-oil, BO) was 9.1%wt. for PKS and up to 25%wt. in the case of EFB. Liquid and gaseous products were analyzed by conventional capillary gas chromatography. The PA from the PKS had 30%wt. of total phenolic compounds (up to 24%wt. phenol) and 46%wt. acetic acid. On the other hand, the bio-oil from PKS had 43%wt. of total phenolic compounds (up to 26%wt. phenol) and 17%wt. acetic acid. The PA from EFB contained mainly acetic acid (65.5%wt.), furfural (7.7%wt.), methanol (8.0%wt.), and phenol (15.2%wt.). When EFB was pretreated, the concentration of acetic acid in PA decreased dramatically, while the concentration of furfural increased up to ten times, this effect being more noticeable in the case of microwave pretreatment. The yields of by-products were of significance in all cases (13–23%wt. of gases and 33–52%wt. of char). These results show that the liquid products obtained from the pyrolysis of palm oil industrial wastes could be used in order to obtain chemical raw materials of worldwide extended use, while the by-products (gases and char) can be used as renewable energy sources.


Fuel | 2012

Fuels from bio-oils: Bio-oil production from different residual sources, characterization and thermal conditioning

Melisa Bertero; Gabriela de la Puente; Ulises Sedran


Fuel | 2014

Characterization of the liquid products in the pyrolysis of residual chañar and palm fruit biomasses

Melisa Bertero; Horacio Gorostegui; Camilo J. Orrabalis; Carlos A. Guzmán; Edgardo L. Calandri; Ulises Sedran


Energy & Fuels | 2011

Effect of Pyrolysis Temperature and Thermal Conditioning on the Coke-Forming Potential of Bio-oils

Melisa Bertero; Gabriela de la Puente; Ulises Sedran


Applied Catalysis A-general | 2015

Catalytic cracking of bio-oils improved by the formation of mesopores by means of Y zeolite desilication

Juan Rafael García; Melisa Bertero; Marisa Falco; Ulises Sedran


Renewable Energy | 2013

Products and coke from the conversion of bio-oil acids, esters, aldehydes and ketones over equilibrium FCC catalysts.

Melisa Bertero; Gabriela de la Puente; Ulises Sedran


Catalysis Today | 2013

Upgrading of bio-oils over equilibrium FCC catalysts. Contribution from alcohols, phenols and aromatic ethers

Melisa Bertero; Ulises Sedran


Energy | 2016

Immediate catalytic upgrading of soybean shell bio-oil

Melisa Bertero; Ulises Sedran


Recent Advances in Thermo-Chemical Conversion of Biomass | 2015

Coprocessing of Bio-oil in Fluid Catalytic Cracking

Melisa Bertero; Ulises Sedran

Collaboration


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Ulises Sedran

National Scientific and Technical Research Council

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Gabriela de la Puente

National Scientific and Technical Research Council

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Juan Rafael García

National Scientific and Technical Research Council

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Marisa Falco

National Scientific and Technical Research Council

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Camilo J. Orrabalis

National Scientific and Technical Research Council

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Carlos A. Guzmán

National Scientific and Technical Research Council

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Edgardo L. Calandri

National Scientific and Technical Research Council

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Horacio Gorostegui

National Scientific and Technical Research Council

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Ani Idris

Universiti Teknologi Malaysia

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Khoirun Nisa Mahmud

Universiti Teknologi Malaysia

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