2017
DOI: 10.3390/en10040516
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CO2 Foam Stability Improvement Using Polyelectrolyte Complex Nanoparticles Prepared in Produced Water

Abstract: Abstract:Despite the increasing interest in CO 2 foam flooding for enhanced oil recovery applications, it is challenging to have a successful field operation as the performance of the surfactant is often affected by the presence of crude oil and salinity of the water. It is also challenging to dispose of huge amounts of water associated with the field operation. Due to the incompatibility of the produced water with chemicals used in the foam system, the produced water cannot be used as an injecting fluid. The … Show more

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Cited by 29 publications
(10 citation statements)
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References 19 publications
(18 reference statements)
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“…Selection of surfactants for foaming application in EOR, CO 2 sequestration, hydraulic fracturing, and other upstream applications is a challenging task [17][18][19][20][21][22][23][24][25]. A surfactant for foaming applications should be generally thermally stable, compatible with reservoir brine and other chemicals, have lower adsorption on reservoir rock, have high foamability and foam stability, and should be economically viable [26][27][28][29][30].…”
Section: Introductionmentioning
confidence: 99%
“…Selection of surfactants for foaming application in EOR, CO 2 sequestration, hydraulic fracturing, and other upstream applications is a challenging task [17][18][19][20][21][22][23][24][25]. A surfactant for foaming applications should be generally thermally stable, compatible with reservoir brine and other chemicals, have lower adsorption on reservoir rock, have high foamability and foam stability, and should be economically viable [26][27][28][29][30].…”
Section: Introductionmentioning
confidence: 99%
“…The surfactant was dissolved in 33.3 and 66.7 kppm brines to form 1 w/w % reference solutions. Polyelectrolyte complex nanoparticles (PECNP) were prepared according to the procedure developed by Barati and co-workers. ,, Branched polyethylenimine (PEI) was obtained from Sigma-Aldrich with an average molecular weight of 25 000 g/mol, 1.03 g/mL density at 25 °C, and corresponding viscosity ranging between 13 000 and 18 000 cP at 50 °C. DS was provided from Sigma-Aldrich with 500 000 g/mol molecular weight.…”
Section: Methodsmentioning
confidence: 99%
“…The mixing ratio of PEI to DS to the diluting brine solution (PEI:DS:brine) was chosen to be 3:1:0.1 to make positively charged nanoparticles. This ratio was developed based on previous observations with zeta potential and particle size measurements. , The nanoparticle solution was mixed with surfactant solutions (1 w/w %) in both 33.3 kppm and 66.7 kppm brine systems for 20 min to form the PECNP/surfactant complexation with different mixing ratios of PECNP:surfactant (1:9, 2:8, 3:7, and 4:6). The concentration of the surfactant remains constant in mixing with nanoparticles (1 w/w %).…”
Section: Methodsmentioning
confidence: 99%
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“…One option, to improve the fluid transport efficiency through fractures and increase the recovery of non-aqueous phase liquids for aquifer remediation, is to reduce the gas mobility by foaming the injectant. [5][6][7][8][9][10][11][12][13] Foam provides mobility control in fractures and systems featuring large permeability contrasts. [14][15][16][17] Accurate and detailed understanding of foam physics contributes to successful use of foam for aquifer remediation, improved hydrocarbon recovery efficiency, and hydraulic fracturing.…”
Section: Introductionmentioning
confidence: 99%