Spirulina (Arthrospira platensis) was cultivated in a 70 L indoor vertical photobioreactor and harvested at concentrations of 1.0 g L-1 dry biomass. Lyophilised algal biomass was pyrolysed at 500 degrees C under nitrogen and vapours were passed over pelletised HZSM5- zeolite (SiO2/Al2O3 38). An organic fraction (bio-oil) overlaying an aqueous phase was obtained by cold trapping, while non-condensed bio-oil components (XAD fraction) were adsorbed onto a poly(styrene-co-divinylbenzene) resin. About 20% of the original algal carbon was converted into inorganic carbon in the aqueous (HCO3-/CO32-) and gas phase (composed of 70% CO2, 20% CO). Most of spirulina carbon ended up in char (30%) and coke (30%). Bio-oil and XAD fraction represented approximately 10% mass, 20% carbon and 20% energy of algal biomass. Bio-oil composition was dominated by alkylated monoaromatic hydrocarbons, with benzene concentrations below 10 g kg(-1). Large part of original nitrogen was dissolved in the aqueous phase (40%) and incorporated into char/coke (37%). A minor fraction (6%) of nitrogen ended up in bio-oil in the form of indoles, pyrroles, carbazoles, anilines. While deoxygenation was effective, denitrogenation was incomplete and probably counteracted by zeolite ammonisation. Microcombustion experiments showed that the bio-oil burnt efficiently, but with a sooting flame, and a tendency to form small solid carbonaceous residues probably associated with the presence of heavy compounds.

Pyrolysis of spirulina and zeolite cracking over HZSM-5. An analytical investigation on the chemical route of bio-oil from cultivation to combustion

Calabria Raffaela;Massoli Patrizio
2017

Abstract

Spirulina (Arthrospira platensis) was cultivated in a 70 L indoor vertical photobioreactor and harvested at concentrations of 1.0 g L-1 dry biomass. Lyophilised algal biomass was pyrolysed at 500 degrees C under nitrogen and vapours were passed over pelletised HZSM5- zeolite (SiO2/Al2O3 38). An organic fraction (bio-oil) overlaying an aqueous phase was obtained by cold trapping, while non-condensed bio-oil components (XAD fraction) were adsorbed onto a poly(styrene-co-divinylbenzene) resin. About 20% of the original algal carbon was converted into inorganic carbon in the aqueous (HCO3-/CO32-) and gas phase (composed of 70% CO2, 20% CO). Most of spirulina carbon ended up in char (30%) and coke (30%). Bio-oil and XAD fraction represented approximately 10% mass, 20% carbon and 20% energy of algal biomass. Bio-oil composition was dominated by alkylated monoaromatic hydrocarbons, with benzene concentrations below 10 g kg(-1). Large part of original nitrogen was dissolved in the aqueous phase (40%) and incorporated into char/coke (37%). A minor fraction (6%) of nitrogen ended up in bio-oil in the form of indoles, pyrroles, carbazoles, anilines. While deoxygenation was effective, denitrogenation was incomplete and probably counteracted by zeolite ammonisation. Microcombustion experiments showed that the bio-oil burnt efficiently, but with a sooting flame, and a tendency to form small solid carbonaceous residues probably associated with the presence of heavy compounds.
2017
Istituto Motori - IM - Sede Napoli
Microalgae
Cyanobacteria
Biofuels
Calatytic pyrolysis
Gas chromatography-mass spectrometry
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/348712
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