TY  - JOUR
EP  - 4945
SN  - 08870624
PB  - American Chemical Society
N1  - cited By 2
SP  - 4939
TI  - Emulsion Breakage Mechanism Using Pressurized Carbon Dioxide
AV  - none
UR  - https://www.scopus.com/inward/record.uri?eid=2-s2.0-85067955266&doi=10.1021%2facs.energyfuels.9b00606&partnerID=40&md5=234ccb5907f0e7d1854ef1065508a7a8
A1  - Azizi, A.
A1  - Aman, Z.M.
A1  - May, E.F.
A1  - Haber, A.
A1  - Ling, N.N.A.
A1  - Husin, H.
A1  - Johns, M.L.
JF  - Energy and Fuels
VL  - 33
Y1  - 2019///
N2  - The production of water during crude oil extraction may result in the formation of stable water-in-oil emulsions. Such emulsions are problematic for a variety of reasons; for example, they increase the fluid viscosity and hence the pumping costs. Previously, Ling; et al. NMR Studies of the Effect of CO2 on Oilfield Emulsion Stability. Energy Fuels 2016, 307, 5555-5562  have shown that treating these water-in-crude oil emulsions with subcritical CO2 at 50 bar can lead to their breakage. These measurements utilized benchtop NMR pulsed field gradient (PFG) techniques to monitor the evolution in the emulsion droplet size distribution, which is a precursor to emulsion breakage. Experimental limitations meant, however, that the measurements were performed only following depressurization of the applied CO2 and as such were unable to directly distinguish between two potential mechanisms for emulsion breakage as proposed in the literature: (i) CO2 bubble formation within the water droplets upon depressurization or (ii) the removal of surface-adsorbed asphaltenes. Here, we develop a new apparatus and perform the required emulsion droplet sizing measurements using NMR PFG techniques with the sample under pressure during CO2 treatment. A distinct growth in the droplet size was observed during the treatment, which is consistent with mechanism (ii); however, further growth was observed following depressurization and shown to be consistent with mechanism (i); thus, both are relevant. The efficacy of the treatment was then further assessed for the case of NaCl addition to the aqueous phase. © 2019 American Chemical Society.
IS  - 6
KW  - Carbon dioxide; Crude oil; Drops; Emulsification; Emulsions; Ostwald ripening; Sizing (finishing operation); Sodium chloride; Water treatment
KW  -  Breakage mechanism; Crude oil extraction; Oilfield emulsions; Potential mechanism; Pressurized carbon dioxide; Pulsed field gradients; Water in oil emulsions; Water-in-crude oil emulsion
KW  -  Lead removal (water treatment)
ID  - scholars11527
ER  -