Lorenzo Bertin

Prof. Dr. Lorenzo Bertin

Department of Civil, Environmental and Materials Engineering, Engineering Faculty of the University of Bologna, via Terracini 28, I- 40131, Bologna, Italy

Research Focus & Metrics

Academic Career Length

26Years (2001-Present)

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

Representative Publications

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1 July 2011 in Chemical Engineering Journal
Verified
Journal Article
Closed access
Lorenzo BertinLorenzo Bertin
Lorenzo Bertin
FFFrancesco Ferri
Francesco Ferri
Alberto ScomaAlberto Scoma
Alberto Scoma
LMLeonardo Marchetti
Leonardo Marchetti
FFFabio Fava
Fabio Fava

8 October 2015 in Green Chemistry
Verified
Journal Article
Closed access
PDF file
GMGonzalo Agustin Martinez
Gonzalo Agustin Martinez
SRStefano Rebecchi
Stefano Rebecchi
DDDeborha Decorti
Deborha Decorti
JDJoana M. B. Domingos
Joana M. B. Domingos
ANAndrea Natolino
Andrea Natolino
FFFabio Fava
Fabio Fava
The development of a multi-purpose four step-cascading biorefinery scheme for the valorization of red grape pomace (GP) was proposed. The consecutive processes were respectively dedicated to (a) the recovery of polyphenols by supercritical CO2 extraction, (b) the production of volatile fatty acids (VFAs) by anaerobic acidogenic digestion, (c) the exploitation of produced VFAs as the precursors for the biotechnological production of polyhydroxyalkanoates (PHAs) and (d) the production of a CH4-rich biogas by the anaerobic digestion of solid leftovers from the acidogenic process. More than 2.7 g of total polyphenols (as gallic acid equivalents) per 100 g of dry matter were extracted. A high content of valuable proanthocyanidins occurred in the recovered polyphenolic fraction. The dephenolized GP was anaerobically digested under batch acidogenic conditions, obtaining about 20 g L−1 of total VFAs in the liquid effluent. The latter matrix was employed to feed a pure culture of a Cupriavidus necator strain, which was induced to produce and store PHAs under nitrogen-limiting conditions. The process was carried out in 0.5 L-shake flasks by using a two-step production approach. In particular, pre-grown biomass was fed with different concentrations of the acidic effluent (20 or 40% v/v) in two sequential batch processes. Poly(3-hydroxybutyrate) was accumulated up to 63% of the cells dry weight when pre-grown biomass was fed with 40% of the acidic effluent. No inhibitory effects due to non-VFA compounds occurring in the actual acidogenic effluent were observed. Finally, the anaerobic digestion of the exhausted solid fraction from the acidogenic process allowed obtaining 113 mL of biomethane per gram of fed volatile solids.

9 April 2009 in Journal of Chemical Technology & Biotechnology
Verified
Journal Article
Closed access
PDF file
MBM. Beccari
M. Beccari
Lorenzo BertinLorenzo Bertin
Lorenzo Bertin
DDD. Dionisi
D. Dionisi
FFF. Fava
F. Fava
SLSilvia Lampis
Silvia Lampis
Marianna VillanoMarianna Villano
Marianna Villano

1 December 2016 in Chemical Engineering Journal
Verified
Journal Article
Closed access
SRStefano Rebecchi
Stefano Rebecchi
DPDavide Pinelli
Davide Pinelli
Lorenzo BertinLorenzo Bertin
Lorenzo Bertin
Fabiana ZamaFabiana Zama
Fabiana Zama
FFFabio Fava
Fabio Fava
DFDario Frascari
Dario Frascari

1 January 2016 in Chemical Engineering Journal
Verified
Journal Article
Closed access
DFDario Frascari
Dario Frascari
ABAurora Esther Molina Bacca
Aurora Esther Molina Bacca
Fabiana ZamaFabiana Zama
Fabiana Zama
Lorenzo BertinLorenzo Bertin
Lorenzo Bertin
FFFabio Fava
Fabio Fava
DPDavide Pinelli
Davide Pinelli

17 February 2021 in FEBS Open Bio
Verified
Journal Article
Open access
PDF file
MEMicaela Degli Esposti
Micaela Degli Esposti
DMDavide Morselli
Davide Morselli
FFFabio Fava
Fabio Fava
Lorenzo BertinLorenzo Bertin
Lorenzo Bertin
FCFabrizio Cavani
Fabrizio Cavani
Paola FabbriPaola Fabbri
Paola Fabbri
Building new value chains, through the valorization of biomass components for the development of innovative bio‐based products (BBPs) aimed at specific market sectors, will accelerate the transition from traditional production technologies to the concept of biorefineries. Recent studies aimed at mapping the most relevant innovations undergoing in the field of BBPs (Fabbri et al. 2019, Final Report of the Task 3 BIOSPRI Tender Study on Support to R&I Policy in the Area of Bio‐based Products and Services, delivered to the European Commission (DG RTD)), clearly showed the dominant position played by the plastics sector, in which new materials and innovative technical solutions based on renewable resources, concretely contribute to the achievement of relevant global sustainability goals. New sustainable solutions for the plastic sector, either bio‐based or bio‐based and biodegradable, have been intensely investigated in recent years. The global bioplastics and biopolymers market size is expected to grow from USD 10.5 billion in 2020 to USD 27.9 billion by 2025 (Markets and Markets, 2020, Bioplastics & Biopolymers Market by Type (Non‐Biodegradable/Bio‐Based, Biodegradable), End‐Use Industry (Packaging, Consumer Goods, Automotive & Transportation, Textiles, Agriculture & Horticulture), Region ‐ Global Forecast to 2025), and this high growth is driven primarily by the growth of the global packaging end‐use industry. Such relevant opportunities are the outcomes of intensive scientific and technological research devoted to the development of new materials with selected technical features, which can represent feasible substitutes for the fossil‐based plastic materials currently used in the packaging sectors and other main fields. This article offers a map of the latest developments connected to the plastic sector, achieved through the application of biotechnological routes for the preparation of completely new polymeric structures, or drop‐in substitutes derived from renewable resources, and it describes the specific role played by biotechnology in promoting and making this transition faster.