Davide Manca

Prof. Davide Manca

orcid

Research Focus & Metrics

Academic Career Length

31Years (1996-Present)

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

Representative Publications

View All Publications
1 March 2015 in Safety Science
Verified
Journal Article
Closed access
Salman NazirSalman Nazir
Salman Nazir
LSLinda Johnstone Sorensen
Linda Johnstone Sorensen
KØKjell Øvergård
Kjell Øvergård
DMDavide Manca
Davide Manca

13 October 2022 in Energies
Verified
Journal Article
Open access
PDF file
AIAndrea Isella
Andrea Isella
DMDavide Manca
Davide Manca
Global warming is becoming an increasing issue, and greenhouse gas (GHG) emissions represent the engine of such a phenomenon. This review aims to identify the origin of GHG emissions and focus in detail on the ones related to (petro) chemical industries. The industrial sector is the primary GHG emitter among all the other anthropogenic sources. The chemical industry is the first in charge of that (having accounted for about 6.5% of the global GHG emissions in 2018). Thought-provoking data such as yearly productivities and emission factors related to the predominant chemicals prompt the reader to acquire a sense of the critical activities responsible for carbon-intensive emissions, which should be the first to be decarbonized. Specifically, ammonia synthesis and steam cracking resulted in the most polluting processes of the chemical industry, being responsible for the release of about 440 and 228 Mt-CO2,eq/y, respectively, in 2020. The same approach also applies to oil refining. Due to the massive amounts of oil barrels produced daily, oil refining is a key player in industrial GHG emissions (about 3% of the global emissions in 2018). Indeed, in 2020, refineries emitted nearly 1313 Mt-CO2,eq/y.

7 October 2014 in Process Safety Progress
Verified
Journal Article
Closed access
PDF file
Salman NazirSalman Nazir
Salman Nazir
DMDavide Manca
Davide Manca

1 March 2024 in Chemical Engineering Journal
Verified
Journal Article
Open access
AIAndrea Isella
Andrea Isella
RORaffaele Ostuni
Raffaele Ostuni
DMDavide Manca
Davide Manca

1 October 2019 in Computers & Chemical Engineering
Verified
Journal Article
Closed access
ABAnton Ochoa Bique
Anton Ochoa Bique
LMLeonardo K.K. Maia
Leonardo K.K. Maia
FMFabio La Mantia
Fabio La Mantia
DMDavide Manca
Davide Manca
EZEdwin Zondervan
Edwin Zondervan

1 December 2015 in Computers & Chemical Engineering
Verified
Journal Article
Open access
MBM. Barello
M. Barello
DMDavide Manca
Davide Manca
RPR. Patel
R. Patel
Iqbal M MujtabaIqbal M Mujtaba
Iqbal M Mujtaba
YesThe performance of a batch reverse osmosis (RO) desalination process in terms of permeate quantity and salinity as a function of feed pressure and feed salinity is evaluated by using laboratory experiments and process modelling. Special attention is paid to the water and salt permeability constants (Kw, Ks) which affect the permeate and salt flux across the membrane. Kw and Ks are found to be strongly pressure-dependent for the batch system which is in-line with earlier observations for continuous RO systems. However, the most important findings of this work are the dependence of Kw and Ks on feed salinity, something that have never been observed or reported in the literature. In order to better qualify these observations, further experiments with the batch system are conducted with a constant feed salinity so that the operating condition resembles that of a continuous RO process