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Behaviours of Polymers and Surfactants Solutions in

Presence of Electrolytes

C. Noïk, C. Yang

To cite this version:

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REVUE DE L’INSTITUT FRANÇAIS DU PÉTROLE VOL. 52, N° 2, MARS-AVRIL 1997

266

BEHAVIORS OF POLYMERS

AND SURFACTANTS SOLUTIONS

IN PRESENCE OF ELECTROLYTES

Chemical methods for enhanced oil recovery have been studied for a long time. Chemical method rate expressed by the ratio efficiency/procedure price becomes favorable according to the recent progress of the alkali-surfactant-polymer combination method. The advantages of alkali-surfactant-polymer flooding and micelle-polymer flooding are combined by this procedure.

The compatibility between polymer and surfactant solutions is the main parameter for the optimisation of this combination method. In order to obtain the sufficient viscosity and the low interfacial tension of these solutions, it is necessary to know the conditions under which the different additives are compatible. We have studied the monophase to diphase transition of the system, the critical salinity of the phase separation and the effect of temperature (1).

1 PHASE BEHAVIOR OF THE SYSTEM

At fixed salinity, a solution of surfactant solution (TRS 10-80) at 2% active material with 5% of n-butanol is mixed with 1% polyacrylamide (AD 37)-n-butanol solution in different proportions. The solutions are stirred and rested at constant temperatures (30, 60, 80, 90¡C) until the equilibrium is reached. Figure 1 represents the chemical stability domain at 30¡C of TRS10-80/AD37 solutions as a function of the total salinity. In general, we observed either a monophasic solution or a separation in two liquid phases.The composition

Figure 1

Phase behavior of TRS 10Ð 80+ polyacrylamide solution

(30¡C, n-butanol 50 g/l).

of each phase has been analyzed for several polymer-surfactant system choosen near the phase separation limit. The upper phase is rich in surfactant and n-butanol compared to the initial composition. The lower phase contains mainly thepolyacrylamide.

2 CRITICAL SALINITY OF PHASE SEPARATION

The determination of the critical salinity of phase separation was performed as a function of polymer or surfactant concentration and structure. Figure 2 indicates that the salinity where the phase separation occurs increases as

One phase Two phases 20 15 10 5 0 0 200 400 600 Polymer concentration (ppm) Salinity NaCl (g/l) 800 1000 n-butanol 50 g/l. 30C 1.6 1.2 1.0 0.8 0.4 concentration TRS 10-80 (%) Hydrolysis degree of th e polyacrylamide AO 37 (37 %) AO 10 (2 %) AO 60 (44 %)

C. YANG

RIPED1

C. NOÏK

IFP2

(1) PO Box 910, Beijing - China

(2) 1 et 4, avenue de Bois-PrŽau, 92852 Rueil-Malmaison Cedex - France

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REVUE DE L’INSTITUT FRANÇAIS DU PÉTROLE VOL. 52, N° 2, MARS-AVRIL 1997

267

the polymer or surfactant concentration decreases. This salinity value also depends on the polyacrylamide rate of hydrolysis.

Moreover, with the same experimental condition, the monophasic domain is enhanced at higher salinity when the n-butanol additive is changed by a more hydrosoluble additive like isobutanol. In the same way, the addition of 1% alkylpolyethoxy sulfonate (AES) to 1% TRS 10-80 solution with 2% n-butanol (ATN system) enhances the compatibility between polymer and surfactant by increasing the solubility of the products.

Figure 2

Variation of the critical salinity of TRS 10Ð 80+

poly-acrylamide solution vs. the surfactant concentration (30¡C, n-butanol 50 g/l).

For the ATN system, we also observed that the critical salinity increases when the polymer is non-ionic like scleroglucan polysaccharide or when a terpolymer Hostamer is used (Table 1).

TABLE 1

ATN 1% + 0.5% polymer-30¡C

polymer AD37 Scleroglucan Hostamer critical salinity - NaCl g/l 19 30 57

3 RHEOLOGICAL BEHAVIOR

In the monophasic domain, the liquid phase has a classical behavior of pseudoplastic fluid. Polyacrylamide viscosity decreases with an increase of petroleum sulfonate concentration. Surfactants in polymer solution behave as a salt on the polyacrylamide molecule dimension and have no effect on scleroglucan conformation.

4 STABILITY AS A FUNCTION OF TEMPERATURE

Compatibility between polymer and surfactant increases with temperature. As shown in Figure 3, for the ATN system, NaCl critical salinity increases with temperature and varies with polymer structure. Over 60¡C, surfactant concentration has an important effect on phase separation as the critical salinity decreases drastically. Phases analysis indicates that salts molecules are mainly in the polymer lower phase.

For thermal stability studies, the viscosity evolutions of different solutions over two months at 30, 60 and 90¡C are presented in Figure 4. Stability as a function of time is strictly dependent on the polymer structure. The more degradable polymer, i.e polyacrylamide, the less stable the formulation. Hostamer Ñsurfactant formulations has a better thermal behavior.

Figure 3

Variation of critical salinity of ATN + AD37 solution vs. ATN concentration (Cp = 500 mg/l, 30, 60, 80¡C).

Figure 4

The thermal stability of Hostamer solution in the presence surfactants (30, 60, 90¡C). 0.30 0.50 0.70 0.90 1.10 1.30 0 10 20 30 40 50 60 70 Time (days) Normalized V iscocity Cp: 500 ppm 1% sulfonate 1: ATN 30¡C 2: TRS 10-80 30¡C 3: TRS 10-80 60¡C 4: ATN 60¡C 5: TRS 10-80 90¡C 6: ATN 90¡C 1 2 3 4 5 6 0 10 20 30 40 50 60 70 80 90 100 0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6 ATN Conc. (%) Salinity NaCl (g/l) ATN-AES: TRS: n-butanol (1.1:2) Cp: 500 ppm 30¡C 60¡C 90¡C 2.0 4.0 6.0 8.0 10.0 12.0 14.0 0.0 0.4 0.6 1.2 1.6 2.0 2.4 TRS 10-80(%) Concentration Salinity NaCl (g/l) n-butanol 50 g/l. 30C Two phases One phase Polymer concentration Cp - 500 ppm Cp - 200 ppm Cp - 800 ppm

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REVUE DE L’INSTITUT FRANÇAIS DU PÉTROLE VOL. 52, N° 2, MARS-AVRIL 1997

268

REFERENCES

1 Work done in collaboration with IFP: IFP Report 38 391.

October (1990).

2 Gilanyi T. and E. Wolfram (1975), Proc. Int. Conf. Colloid

Surf. Sci., 1, pp. 633-640.

3 Nagarajan R. and M.P. Harold (1980), Int. Symp. Solution

Behavior of Surfactant, Postdam, New York.

4 Yang C.Z (1986), SPE/DOE 14931.

5 Rivenq R., A. Donche A. and C. Noik (1980), SPE 19635. 6 Muller G. (1981), Polymer Bulletin, 5, pp. 31-37.

Final manuscript received in January 1997

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