Sergio Rapagnà

Prof. Sergio Rapagnà

orcid

Research Focus & Metrics

Academic Career Length

20Years (2007-Present)

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

Representative Publications

View All Publications
1 September 2010 in Bioresource Technology
Verified
Journal Article
Closed access
SRSergio Rapagnà
Sergio Rapagnà
Gallucci KatiaGallucci Katia
Gallucci Katia
MMManuela Di Marcello
Manuela Di Marcello
MMMuriel Matt
Muriel Matt
MNManfred Nacken
Manfred Nacken
PFPier Ugo Foscolo
Pier Ugo Foscolo

1 June 2011 in Fuel Processing Technology
Verified
Journal Article
Closed access
RMRudy Michel
Rudy Michel
SRSergio Rapagnà
Sergio Rapagnà
MMManuela Di Marcello
Manuela Di Marcello
PBPhilippe Burg
Philippe Burg
MMMuriel Matt
Muriel Matt
RGRené Gruber
René Gruber

1 January 2018 in Waste Management
Verified
Journal Article
Closed access
SRSergio Rapagnà
Sergio Rapagnà
Gallucci KatiaGallucci Katia
Gallucci Katia
PFPier Ugo Foscolo
Pier Ugo Foscolo

1 August 2019 in Fuel Processing Technology
Verified
Journal Article
Closed access
ESElisa Savuto
Elisa Savuto
Andrea Di CarloAndrea Di Carlo
Andrea Di Carlo
ASAndrew Steele
Andrew Steele
SHSteffen Heidenreich
Steffen Heidenreich
Gallucci KatiaGallucci Katia
Gallucci Katia
SRSergio Rapagnà
Sergio Rapagnà

23 April 2020 in Applied Sciences
Verified
Journal Article
Open access
PDF file
ESElisa Savuto
Elisa Savuto
JMJan May
Jan May
Andrea Di CarloAndrea Di Carlo
Andrea Di Carlo
Gallucci KatiaGallucci Katia
Gallucci Katia
Andrea Di GiulianoAndrea Di Giuliano
Andrea Di Giuliano
SRSergio Rapagnà
Sergio Rapagnà
The gasification of lignite could be a promising sustainable alternative to combustion, because it causes reduced emissions and allows the production of syngas, which is a versatile gaseous fuel that can be used for cogeneration, Fischer-Tropsch synthesis, or the synthesis of other bio-fuels, such as methanol. For the safe and smooth exploitation of syngas, it is fundamental to have a high quality gas, with a high content of H2 and CO and minimum content of pollutants, such as particulate and tars. In this work, experimental tests on lignite gasification are carried out in a bench-scale fluidized-bed reactor with olivine as bed material, chosen for its catalytic properties that can enhance tar reduction. Some operating parameters were changed throughout the tests, in order to study their influence on the quality of the syngas produced, and pressure fluctuation signals were acquired to evaluate the fluidization quality and diagnose correlated sintering or the agglomeration of bed particles. The effect of temperature and small air injections in the freeboard were investigated and evaluated in terms of the conversion efficiencies, gas composition, and tar produced.

4 January 2023 in Energies
Verified
Journal Article
Open access
PDF file
APAlessandro Antonio Papa
Alessandro Antonio Papa
ESElisa Savuto
Elisa Savuto
Andrea Di CarloAndrea Di Carlo
Andrea Di Carlo
ATAlessandra Tacconi
Alessandra Tacconi
SRSergio Rapagnà
Sergio Rapagnà
This work concerns the activities of the European project BLAZE that aims to integrate a pilot-scale gasifier unit with a Solid Oxide Fuel Cell (SOFC). The objective is to identify the optimal operating conditions for a gasifier and hot gas cleaning and conditioning unit to produce H2-rich syngas with contaminants levels within the limits for the safe operation of the SOFC (750 mg/Nm3 and 75 mg/Nm3 for toluene and naphthalene, respectively). Experimental tests were carried out on a bench-scale gasification plant with a catalytic filter candle placed in the freeboard, to study the influence of temperature (1032 up to 1137 K), bed materials (olivine or olivine/dolomite 80/20%), and a nickel-based catalyst. The tests with a ceramic filter candle filled with catalyst and the mixture of olivine and dolomite in the bed gave the best results in terms of gas composition and gas yield, but the tar content was still higher than the limits for the SOFC. To increase the residence time of the gas in the catalytic bed a new metallic filter candle was tested. This candle, with almost the same external volume, allowed doubling the amount of catalyst used. Under these conditions, the content of toluene and naphthalene was reduced below 150 and 50 mg/Nm3, respectively.