Bulk foam stability and rheological behavior of aqueous foams prepared by clay particles and alpha olefin sulfonate

2019 ◽  
Vol 291 ◽  
pp. 111250 ◽  
Author(s):  
Shuyan Chen ◽  
Hongjuan Liu ◽  
Jingjing Yang ◽  
Yujie Zhou ◽  
Jianan Zhang
1983 ◽  
Vol 23 (01) ◽  
pp. 152-154 ◽  
Author(s):  
Peter B. Rand ◽  
Andrew M. Kraynik

Introduction The physical characteristics of aqueous foams make them excellent candidates for drilling fluids in geothermal formations. A major concern in this application is the foam-forming ability of a surfactant system in the harsh geothermal environment. While investigating the stability of various foams in an autoclave. we observed a dramatic increase in drainage times with increasing generation pressure, even though the liquid volume fraction of the foam was held constant. This effect appears to result from a decrease in cell size with increasing autoclave pressure and therefore is an artifact of the foam generation technique in which the pressure path of the foam changes with autoclave pressure. A theoretical model of drainage predicts that drainage times should increase with decreasing cell size. as observed. These results emphasize that proper control of cell size can have a substantial effect on the apparent stability of a foam. Experimental Procedure The foam is generated in the pressurized autoclave (Fig. 1) by metering surfactant solution and gas through a foam generator consisting of a tube tightly packed with stainless steel wool. A pressure 250 psig (1. 72 MPa) greater than the autoclave pressure pressure 250 psig (1. 72 MPa) greater than the autoclave pressure was used to supply the gas and surfactant solution in all experiments. This technique permits the generation of foam at the desired temperature and pressure with control on the liquid volume fraction. In the autoclave, foam is dispensed into a 10-oz. (311-g) covered glass container. A quartz viewing port permits visual observation. The relative foam stability is assessed by measuring the gravity drainage of liquid from the foam into a graduated cylinder. The time required for 25% and 50% of the original liquid to drain is recorded. Results Initial experiments at room temperature yielded surprising results. For foams produced at autoclave pressures ranging from 1 to 20 atm (0. 1 to 2. 0 MPa), the drainage times increased with pressure by an order of magnitude, as shown in Fig. 2, even though the liquid volume fractions of the foams were essentially identical. Nitrogen gas and an alpha olefin sulfonate foamer were used in these tests. The drainage experiments were repeated for several good foamers of various surfactant types (anionic, amphoteric, cationic, and nonionic) and gas combinations (air, argon, and nitrogen) at 1 and at 20 atm (0. 1 to 2. 0 MPa) (Table 1). As shown, the same systematic increase in drainage times with increasing pressure also was observed in these experiments, suggesting that the effect was not dependent on the chemistry of the gas/liquid interface in the foams. Because of gas compressibility, and the varying pressure profiles in the foam generator, the influence of pressure on the foam structure. specifically the cell size, was explored. Foam Drainage An effect of cell size on foam drainage has been discussed in the literature. SPEJ P. 152


Author(s):  
Muhammad Khan Memon ◽  
Ubedullah Ansari ◽  
Habib U Zaman Memon

The residual oil after primary or secondary oil recovery can be recovered by the methods of EOR (Enhanced Oil Recovery). The objective of this study is screening the surfactants that generate maximum stable foam in the presence of brine salinity at 92oC. Laboratory experiments have been performed to examine and compare the stability of generated foam by individual and blended surfactants in the synthetic brine water. AOS C14-16 (Alpha Olefin Sulfonate) and SDS (Sodium Dodecyl Sulfonate) were selected as main surfactants. Aqueous stability test of AOS C14-16 and SDS with brine water salinity 62070ppm was performed at 92oC. AAS (Alcohol Alkoxy Sulfate) was blended with SDS and AOS C14-16. The solution was stable in the presence of brine salinity at same conditions. Salt tolerance experimental study revealed that AOS C14-16 did not produce precipitates at 92oC. Further, the foam stability of surfactant blend was performed. Result shows that, the maximum life time of generated foam was observed by using blend of 0.2wt% SDS+0.2wt% AOS+0.2wt% AS-1246 and 0.2wt% AOS+0.2wt% IOSC15-18+0.2wt% AAS surfactants as compared to the foam generated by individual surfactants. The success of generated foam by these surfactant solutions in the presence of brine water is the primary screening of surfactant stability and foamability for EOR applications in reservoirs type of reservoirs.


2020 ◽  
Vol 17 (6) ◽  
pp. 1634-1654
Author(s):  
Asad Hassan Syed ◽  
Nurudeen Yekeen ◽  
Eswaran Padmanabhan ◽  
Ahmad Kamal Idris ◽  
Dzeti Farhah Mohshim

AbstractLauryl betaine (LB) as an amphoteric surfactant carries both positive and negative charges and should be able to generate stable foam through electrostatic interaction with nanoparticles and co-surfactants. However, no previous attempts have been made to investigate the influence of nanoparticles and other co-surfactants on the stability and apparent viscosity of LB-stabilized foam. In this study, a thorough investigation on the influence of silicon dioxide (SiO2) nanoparticles, alpha olefin sulfonate (AOS) and sodium dodecyl sulfate (SDS), on foam stability and apparent viscosity was carried out. The experiments were conducted with the 2D Hele-Shaw cell at high foam qualities (80%–98%). Influence of AOS on the interaction between the LB foam and oil was also investigated. Results showed that the SiO2-LB foam apparent viscosity decreased with increasing surfactant concentration from 0.1 wt% to 0.3 wt%. 0.1 wt% SiO2 was the optimum concentration and increased the 0.1 wt% LB foam stability by 108.65% at 96% foam quality. In the presence of co-surfactants, the most stable foam, with the highest apparent viscosity, was generated by AOS/LB solution at a ratio of 9:1. The emulsified crude oil did not imbibe into AOS-LB foam lamellae. Instead, oil was redirected into the plateau borders where the accumulated oil drops delayed the rate of film thinning, bubble coalescence and coarsening.


1970 ◽  
Vol 47 (12) ◽  
pp. 505-509 ◽  
Author(s):  
Toshio Nagai ◽  
Shigeru Hashimoto ◽  
Izumi Yamane ◽  
Akira Mori

2008 ◽  
Author(s):  
R. Farajzadeh ◽  
R. Krastev ◽  
P. L. J. Zitha ◽  
Albert Co ◽  
Gary L. Leal ◽  
...  

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