Abstract
Guerbet amine-oxide was synthesized by using Guerbet acid, N,N′-diethyl-1,3-propanediamine and hydrogen peroxide. Its structure was confirmed by FT-IR spectra and mass spectra. The critical micelle concentration (CMC) and the interfacial tension between the crude oil and water were measured. The results showed that the CMC of the Guerbet amine-oxide is 2.14 × 10−5 mol/L and the interfacial tension could be lowered to ultralow levels. The core flood test showed that the surfactant and polymer binary system could increase oil recovery by 24.7% above the water flood.
1. Introduction
China's oil import dependence has been rising since 1993 and will exceed 70% in 2020 [1]. Meanwhile, the average recovery factor from China’s oilfields is only 24.11%. Clearly, it is needed to enhance oil recovery in China. In the past few years, in order to improve oil recovery, alkaline–surfactant–polymer (ASP) filed tests have been carried out in China’s Daqing oil field and showed great success [2]. The use of alkali can reduce surfactant adsorption on reservoir rock and generate in situ surfactants with acidic oils, and these in situ generated surfactants can produce synergistic effects with the added surfactants in removing residual oil [3]. However, it also caused some side effects, including scaling and corrosion damage to the lifting system, strong emulsification, and greatly decreased liquid production [4]. For these reasons, some surfactant–polymer pilot tests have been performed in China [5]. Undoubtedly, surfactants play a very important role in the flooding formulations. According to capillary number theory, to mobilize trapped residual oil, it often requires a low interfacial tension to overcome capillary forces to allow the oil to flow [6]. The application of surfactants can effectively reduce the interfacial tension; thus, it becomes a major parameter for evaluating the performance of flood surfactants. Generally speaking, the tighter the surfactant arranges at the oil/water interface, the lower interfacial tension can be obtained [7]. The hydrophilicity of the branched surfactant head groups can overcome the steric repulsion between the tails and forms a compact layer, which has a positive effect on reducing the interfacial tension at the oil/water interface [8, 9]. Guerbet alcohol is a type of branched alcohol, which is substituted by an alkyl group in the 2-position. Some literatures have reported its use as a raw material for the preparation of oil displacement gents [10, 11]. However, some of these surfactants are poor hydrolytic stability [12], or their synthetic routes are relatively complicated.
Amine-oxide surfactants are a class of zwitterionic surfactants [13]. They exhibit cationic behaviour in acid solution [14] and characteristics of a nonionic surfactant in an alkaline condition [15]. These surfactants show less irritation to the skin, high foaming properties, and excellent thickening function [16], which is benefit for oil recovery [17].
In this work, we synthesized the Guerbet amine-oxide and investigated its performance in oil recovery.
2. Experimental
2.1. Materials
Guerbet acid (2-decyltetradecanoic acid) (commercial product) was purchased from Jin Tenglong Trade Co., Ltd. N,N-dimethyl-1,3-propane diamine (analytically grade) was purchased from Tci Company, and phosphorus trichloride was obtained from West Asia Reagent Company. Hydrogen peroxide (30%) was purchased from Aladdin Reagent Company. Ethylenediaminetetraacetic acid disodium salt was purchased from Tianjin Damao Reagent Company. Dehydrated crude oil with a density of 810 kg/m3 and a viscosity of 9 MPa·s was derived from the 733 well of the Jing 11 block. Partially hydrolyzed polyacrylamide (HPAM) with an average molecular weight of 17 MDa and a degree of hydrolysis of 23% was provided by Hengju Company with the commercial name of KY-4s.
The water used in the experiments is formation water with a salinity of 10951 mg/L.
2.2. Analytical Methods
The FT-IR spectra were recorded using a Thermo Nicolet is5 recording spectrometer.
ESI-MS spectra were obtained on a WatersXevoTQ mass spectrometer. The instrument was operated in the positive ion mode.
Measurements of the surface tension were carried out on a Junao tensiometer.
The Interfacial tensions were measured by means of the spinning-drop technique at 54°C using a TX 550 spinning-drop interfacial tensiometer at the rotational speed of 5000 rpm.
Viscosity measurements were conducted on a Haake Mars rheometer at 54°C with a shear rate of 7.34 s−1.
2.3. Synthesis
The synthetic route of the Guerbet amine-oxide is illustrated in Scheme 1.
2.3.1. Synthesis of 2-Decyltetradecanoyl Chloride
In a 100 ml three-neck flask equipped with a magnetic stirrer, 14.72 g of 2-decyltetradecanoic acid was added, and the flask was placed into an oil bath in a controlled temperature oil bath at 85°C. Next, 2.2 g of phosphorus trichloride was charged into the flask. The mixture was stirred for 4 hours. After that, the flask was taken out of the oil bath and cooled to room temperature. The mixture in the flask was then transferred to a separatory funnel and allowed to stand overnight. The lower layer was discarded, while the upper layer was collected and kept sealed.
2.3.2. Synthesis of 2-Decyltetradecyl Amidopropyl-N,N-dimethylamine
0.05 mol (22.6 g) of the obtained 2-decyltetradecanoyl chloride was charged into a 100-ml three-neck flask. Afterward, 0.2 mol of N,N-dimethyl-1,3-propane diamine was dropped into the flask under stirring. The resulting mixture was washed three times with distilled water and dried at 65°C overnight.
2.3.3. Synthesis of 2-Decyltetradecyl Amidopropyl-N,N-dimethylamine Oxide
9.04 of 2-decyltetradecyl amidopropyl-N,N-dimethylamine was added in a 100 mL three-neck flask. Next, 0.5 g of ethylenediaminetetraacetic acid disodium salt was dissolved in 20 mL distilled water and poured into the flask. The flask was immersed in an oil bath at 80°C with vigorously stirring. Then, 4.55 g of hydrogen peroxide was added dropwise using a dropping funnel. After the addition, the solution was stirred for 12 hours, followed by the addition of 0.5 g of sodium sulfite to remove the excess hydrogen peroxide. The obtained solid product was washed three times with petroleum ether and then dried under vacuum.
3. Results and Discussion
3.1. IR Spectra
The IR spectra of the synthesized dimethylamine and its oxide are shown in Figure 1, where A and B represent dimethylamine and its oxide, respectively. It can be seen from Figure 1 that there was an additional absorption appeared at 916.86 cm−1 in B, which was the characteristic band of the dimethylamine oxide. The bands at 3291.65 cm−1 could be assigned to N-H stretching vibration absorption, while the bands at 2917.73 cm−1 and 2849.43 cm−1 could be assigned to the unsymmetric stretching vibration absorption of CH3 and asymmetric stretching vibration absorption of CH2. Another band at 1637.25 cm−1 could be identified as stretching vibration of the C=O. The absorption at 1375.99 cm−1 inferred to C-N.
3.2. Mass Spectra
The ESI-MS spectrum of the amine-oxide is shown in Figure 2. The ion at m/z = 469 corresponded to [M + H]+, while an m/z value of 937.94 could be identified as [2M + H]+.
3.3. Surface Tension and CMC of the Synthesized Surfactant
The curves of surface tension versus log concentration of the synthesized amine-oxide surfactant at 25°C are illustrated in Figure 3. The CMC (critical micelle concentration) values of the surfactant were calculated from interception point of the two tangent straight lines at low concentrations [18]. As it can be seen from Figure 3, the surface tension values gradually decreased with increasing concentration of the synthesized surfactant concentration, reaching a minimum surface tension value of 24.7 mN/m at 298.15 K, while the surfactant had a CMC value of 2.14 × 10−5 mol·L−1.
3.4. Polymer Selection
In the surfactant-polymer flooding, the addition of polymer can increase water viscosity and decrease the water/oil mobility ratio. Such a change can lead to a better sweep efficiency and more efficient oil displacement in the swept zone [19]. In view of average permeability of the targeted reservoir, which is 146 mD, the HPAM with the molecular weight of 1700 MDa was selected based on the field test experiences [20]. Its viscosity-concentration curve is shown in Figure 4. In view of viscosity loss which caused by mechanical shearing and degradation effects of the heat or bacteria, the concentration polymer was set at 1000 mg/L [21].
3.5. Interfacial Tension of the Surfactant-Polymer System
It is well known in the literature that as the capillary number is increased, residual saturations are decreased [22]. In theory, based on the definition of the capillary number, the interfacial tension, flow rate, and viscosity of the flooding fluid are associated with the capillary number. However, in the practical flooding process, only the interfacial tension can greatly increase the capillary number. In fact, in a successful displacement process, the injected surfactant slug must achieve ultralow interfacial tension (<0.01 mN/m) [23].
Factors that affect the interfacial tension include reservoir temperature, salinity, time, and concentration of the surfactant. For a given reservoir, reservoir temperature is fixed. The salinity is relatively stable in most cases. Thus, the effects of surfactant concentration and time on the interfacial tension between crude oil and surfactant-polymer solution were investigated. The surfactant concentration used in the experiments ranged from 0.05 to 0.3%, and the polymer concentration was 1000 mg/L. The results are shown in Figure 5.
As it can be seen from Figure 5, the interfacial tension between surfactant-polymer solution and crude oil could be reduced to ultralow levels in a wide range of surfactant concentrations. In addition, the equilibrium interfacial tension decreased with the increase of the surfactant concentration. The interfacial tension is related to adsorption of the surfactant at the oil/water interface. At a low surfactant concentration, the adsorption rate is faster than that of desorption, so more and more surfactant molecules are accumulated at the oil/water interface, which leads to the reduction of the interfacial tension. When the rate of adsorption equals the rate of desorption, the interfacial tension can reach the lowest value. If the surfactant concentration continues to rise, the monolayer adsorption of the surfactant converts to a bilayer adsorption, and the adsorption rate is slow down while desorption rate is increased, which will result in the increase of the interfacial tension [24].
3.6. Core Flood Experiments
As we know, for reservoirs, the permeability has a big effect on the oil recovery. To simulate reservoir condition, a sand-packed core with a permeability of 154 mD was used to carry out flooding tests. The core was evacuated for 24 hours and saturated with the formation water. After that, the core was displaced by crude oil until the residual water saturation was created. Then, 0.3 pore volume of the surfactant/polymer slug was injected into the core, followed by water flood using a constant rate of 0.4 ml/min until 98% water cut was reached. The results are depicted in Figure 6. It showed a significant increase in the oil production for the surfactant/polymer slug. The water cut dropped after the injection of the surfactant/polymer slug; in the mean time, the injection pressure rose rapidly. Total oil recovery reached 77.3%, which was 24.7 percent more than water flood.
4. Conclusion
Guerbet amine-oxide has been synthesized, and its structure was confirmed by FT-IR and ESI-MS. The surfactant showed a relative lower CMC and interfacial tension. The results obtained from core flood experiment showed that the synthesized surfactant could have the application potential in surfactant-polymer enhanced oil recovery.
Data Availability
The data used to support the findings of this study are available from the corresponding author upon request.
Conflicts of Interest
The authors declare that they have no conflicts of interest.
Acknowledgments
This work was supported by the continuous effective of oil production in Huabei Oil Field Project (grant number 2017E-1507).