Carbon capture and storage (CCS): the way forward

M Bui, CS Adjiman, A Bardow, EJ Anthony… - Energy & …, 2018 - pubs.rsc.org
Carbon capture and storage (CCS) is broadly recognised as having the potential to play a
key role in meeting climate change targets, delivering low carbon heat and power …

An overview of CO 2 capture technologies

N MacDowell, N Florin, A Buchard, J Hallett… - Energy & …, 2010 - pubs.rsc.org
In this paper, three of the leading options for large scale CO2 capture are reviewed from a
technical perspective. We consider solvent-based chemisorption techniques, carbonate …

[HTML][HTML] Accurate statistical associating fluid theory for chain molecules formed from Mie segments

T Lafitte, A Apostolakou, C Avendaño… - The Journal of …, 2013 - pubs.aip.org
A highly accurate equation of state (EOS) for chain molecules formed from spherical
segments interacting through Mie potentials (ie, a generalized Lennard-Jones form with …

[HTML][HTML] Group contribution methodology based on the statistical associating fluid theory for heteronuclear molecules formed from Mie segments

V Papaioannou, T Lafitte, C Avendaño… - The Journal of …, 2014 - pubs.aip.org
A generalization of the recent version of the statistical associating fluid theory for variable
range Mie potentials [Lafitte et al, J. Chem. Phys. 139, 154504 (2013)] is formulated within …

Molecular-based equations of state for associating fluids: A review of SAFT and related approaches

EA Müller, KE Gubbins - Industrial & engineering chemistry …, 2001 - ACS Publications
We present a review of recent advances in the statistical associating fluid theory (SAFT). In
contrast to the “chemical theory”, in which nonideality is explained in terms of chemical …

Equations of state for the calculation of fluid‐phase equilibria

YS Wei, RJ Sadus - AIChE journal, 2000 - Wiley Online Library
Progress in developing equations of state for the calculation of fluid‐phase equilibria is
reviewed. There are many alternative equations of state capable of calculating the phase …

Vapour–liquid equilibria in the carbon dioxide–water system, measurement and modelling from 278.2 to 318.2 K

A Valtz, A Chapoy, C Coquelet, P Paricaud… - Fluid phase equilibria, 2004 - Elsevier
New experimental VLE data of CO2–water binary system are reported over a wide
temperature range from 278.2 to 318.2 K and pressures up to 8MPa. A static-analytic …

Enrichment at vapour–liquid interfaces of mixtures: Establishing a link between nanoscopic and macroscopic properties

S Stephan, H Hasse - International Reviews in Physical Chemistry, 2020 - Taylor & Francis
Component density profiles at vapour–liquid interfaces of mixtures can exhibit a non-
monotonic behaviour with a maximum that can be many times larger than the densities in …

Asphaltene precipitation in crude oils: Theory and experiments

E Buenrostro‐Gonzalez, C Lira‐Galeana… - AIChE …, 2004 - Wiley Online Library
The precipitation of asphaltenes in two Mexican crude oils was measured using a
combination of high‐pressure isothermal expansion and atmospheric titration with n …

SAFT-γ force field for the simulation of molecular fluids. 1. A single-site coarse grained model of carbon dioxide

C Avendano, T Lafitte, A Galindo… - The Journal of …, 2011 - ACS Publications
An application of the “top-down” concept for the development of accurate coarse-grained
intermolecular potentials of complex fluids is presented. With the more common “bottom-up” …