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  4. Extension of vibrating-wire viscometry to electrically conducting fluids and measurements of viscosity and density of brines with dissolved CO2 at reservoir conditions
 
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Extension of vibrating-wire viscometry to electrically conducting fluids and measurements of viscosity and density of brines with dissolved CO2 at reservoir conditions
File(s)
Viscosity and density of brine + CO2 - rev 12 accepted.docx (626.44 KB)
Accepted version
Author(s)
Calabrese, Claudio
McBride-Wright, Mark
Maitland, Geoffrey C
Trusler, JP Martin
Type
Journal Article
Abstract
In order to design safe and effective storage of anthropological CO2 in deep saline aquifers, it is necessary to know the thermophysical properties of brine–CO2 solutions. In particular, density and viscosity are important in controlling convective flows of the CO2-rich brine. In this work, we have studied the effect of dissolved CO2 on the density and viscosity of NaCl and CaCl2 brines over a wide range of temperatures from 298 to 449 K, with pressures up to 100 MPa, and salinities up to 1 mol·kg–1. Additional density measurements were also made for both NaCl and CaCl2 brines with dissolved CO2 at salt molalities of 2.5 mol·kg–1 in the same temperature and pressure ranges. The viscosity was measured by means of a vibrating-wire viscometer, while the density was measured with a vibrating U-tube densimeter. To facilitate the present study, the theory of the vibrating-wire viscometer has been extended to account for the electrical conductivity of the fluid, thereby expanding the use of this technique to a whole new class of conductive fluids. Relative uncertainties were 0.07% for density and 3% for viscosity at 95% confidence. The results of the measurements show that both density and viscosity increase as a result of CO2 dissolution, confirming the expectation that CO2-rich brine solutions will sink in an aquifer. We also find that the effect of dissolved CO2 on both properties is sensibly independent of salt type and molality.
Date Issued
2019-09-01
Date Acceptance
2019-07-19
Citation
Journal of Chemical and Engineering Data, 2019, 64 (9), pp.3831-3847
URI
http://hdl.handle.net/10044/1/77555
URL
https://pubs.acs.org/doi/10.1021/acs.jced.9b00248
DOI
https://www.dx.doi.org/10.1021/acs.jced.9b00248
ISSN
0021-9568
Publisher
American Chemical Society
Start Page
3831
End Page
3847
Journal / Book Title
Journal of Chemical and Engineering Data
Volume
64
Issue
9
Copyright Statement
© 2019 American Chemical Society. This document is the Accepted Manuscript version of a Published Work that appeared in final form in Journal of Chemical and Engineering Data, after peer review and technical editing by the publisher. To access the final edited and published work see https://doi.org/10.1021/acs.jced.9b00248
Identifier
http://gateway.webofknowledge.com/gateway/Gateway.cgi?GWVersion=2&SrcApp=PARTNER_APP&SrcAuth=LinksAMR&KeyUT=WOS:000486361300017&DestLinkType=FullRecord&DestApp=ALL_WOS&UsrCustomerID=1ba7043ffcc86c417c072aa74d649202
Subjects
Science & Technology
Physical Sciences
Technology
Thermodynamics
Chemistry, Multidisciplinary
Engineering, Chemical
Chemistry
Engineering
AQUEOUS NACL SOLUTIONS
CARBON-DIOXIDE
TEMPERATURES
PRESSURES
RANGE
WATER
SEQUESTRATION
FORMULATION
SOLUBILITY
EQUATION
Publication Status
Published
Date Publish Online
2019-08-16
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