Federico Liuzzi

Dr. Federico Liuzzi

orcid

Research Focus & Metrics

Academic Career Length

14Years (2013-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 February 2013 in Applied Energy
Verified
Journal Article
Closed access
IBIsabella De Bari
Isabella De Bari
Federico LiuzziFederico Liuzzi
Federico Liuzzi
AVAntonio Villone
Antonio Villone
GBGiacobbe Braccio
Giacobbe Braccio

1 September 2013 in New Biotechnology
Verified
Journal Article
Closed access
IBIsabella De Bari
Isabella De Bari
PCPaola De Canio
Paola De Canio
DCDaniela Cuna
Daniela Cuna
Federico LiuzziFederico Liuzzi
Federico Liuzzi
ACAngela Capece
Angela Capece
PRPatrizia Romano
Patrizia Romano

28 February 2019 in Journal of Microbiology and Biotechnology
Verified
Journal Article
Closed access
Nicola Di FidioNicola Di Fidio
Nicola Di Fidio
Federico LiuzziFederico Liuzzi
Federico Liuzzi
SMSilvio Mastrolitti
Silvio Mastrolitti
Roberto AlbergoRoberto Albergo
Roberto Albergo
IBIsabella De Bari
Isabella De Bari
The use of low-cost substrates represents one key issue to make single cell oil production sustainable. Among low-input crops, Arundo donax L. is a perennial herbaceous rhizomatous grass containing both C5 and C6 carbohydrates. The scope of the present work was to investigate and optimize the production of lipids by the oleaginous yeast Cutaneotrichosporon curvatus from undetoxified lignocellulosic hydrolysates of steam-pretreated A. donax. The growth of C. curvatus was first optimized in synthetic media, similar in terms of sugar concentration to hydrolysates, by applying the response surface methodology (RSM) analysis. Then the bioconversion of undetoxified hydrolysates was investigated. A fed-batch process for the fermentation of A. donax hydrolysates was finally implemented in a 2-L bioreactor. Under optimized conditions, the total lipid content was 64% of the dry cell weight and the lipid yield was 63% of the theoretical. The fatty acid profile of C. curvatus triglycerides contained 27% palmitic acid, 33% oleic acid and 32% linoleic acid. These results proved the potential of lipid production from A. donax, which is particularly important for their consideration as substitutes for vegetable oils in many applications such as biodiesel or bioplastics.

5 January 2020 in Catalysts
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Journal Article
Open access
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Nicola Di FidioNicola Di Fidio
Nicola Di Fidio
ANNA RASPOLLIANNA RASPOLLI
ANNA RASPOLLI
Sara FulignatiSara Fulignati
Sara Fulignati
Domenico LicursiDomenico Licursi
Domenico Licursi
Federico LiuzziFederico Liuzzi
Federico Liuzzi
Claudia AntonettiClaudia Antonetti
Claudia Antonetti
Lignocellulosic biomass represents one of the most important feedstocks for future biorefineries, being a precursor of valuable bio-products, obtainable through both chemical and biological conversion routes. Lignocellulosic biomass has a complex matrix, which requires the careful development of multi-step approaches for its complete exploitation to value-added compounds. Based on this perspective, the present work focuses on the valorization of hemicellulose and cellulose fractionsof giant reed (Arundo donax L.) to give second-generation sugars, minimizing the formation of reaction by-products. The conversion of hemicellulose to xylose was undertaken in the presence of the heterogeneous acid catalyst Amberlyst-70 under microwave irradiation. The effect of the main reaction parameters, such as temperature, reaction time, catalyst, and biomass loadings on sugars yield was studied, developing a high gravity approach. Under the optimised reaction conditions (17 wt% Arundo donax L. loading, 160 °C, Amberlyst-70/Arundo donax L. weight ratio 0.2 wt/wt), the xylose yield was 96.3 mol%. In the second step, the cellulose-rich solid residue was exploited through the chemical or enzymatic route, obtaining glucose yields of 32.5 and 56.2 mol%, respectively. This work proves the efficiency of this innovative combination of chemical and biological catalytic approaches, for the selective conversion of hemicellulose and cellulose fractions of Arundo donax L. to versatile platform products.

1 March 2014 in New Biotechnology
Verified
Journal Article
Closed access
IBIsabella De Bari
Isabella De Bari
DCDaniela Cuna
Daniela Cuna
VMVincenzo Di Matteo
Vincenzo Di Matteo
Federico LiuzziFederico Liuzzi
Federico Liuzzi

3 December 2020 in Processes
Verified
Journal Article
Open access
PDF file
IBIsabella De Bari
Isabella De Bari
Federico LiuzziFederico Liuzzi
Federico Liuzzi
Alfredo AmbricoAlfredo Ambrico
Alfredo Ambrico
TMTrupo Mario
Trupo Mario
Biomass-derived sugars are platform molecules that can be converted into a variety of final products. Non-food, lignocellulosic feedstocks, such as agroforest residues and low inputs, high yield crops, are attractive bioresources for the production of second-generation sugars. Biorefining schemes based on the use of versatile technologies that operate at mild conditions contribute to the sustainability of the bio-based products. The present work describes the conversion of giant reed (Arundo donax), a non-food crop, to ethanol and furfural (FA). A sulphuric-acid-catalyzed steam explosion was used for the biomass pretreatment and fractionation. A hybrid process was optimized for the hydrolysis and fermentation (HSSF) of C6 sugars at high gravity conditions consisting of a biomass pre-liquefaction followed by simultaneous saccharification and fermentation with a step-wise temperature program and multiple inoculations. Hemicellulose derived xylose was dehydrated to furfural on the solid acid catalyst in biphasic media irradiated by microwave energy. The results indicate that the optimized HSSF process produced ethanol titers in the range 43–51 g/L depending on the enzymatic dosage, about 13–21 g/L higher than unoptimized conditions. An optimal liquefaction time before saccharification and fermentation tests (SSF) was 10 h by using 34 filter paper unit (FPU)/g glucan of Cellic® CTec3. C5 streams yielded 33.5% FA of the theoretical value after 10 min of microwave heating at 157 °C and a catalyst concentration of 14 meq per g of xylose.