Highly stable foams generated in mixed systems of ethanediyl-1,2-bis(dodecyldimethylammonium bromide) and alcohols

Bing-Lei Songa, Xiao-Na Yua, Jian-Xi Zhao*b and Guo-Jing Sunb
aThe Key Laboratory of Food Colloids and Biotechnology, Ministry of Education, School of Chemical and Material Engineering, Jiangnan University, Wuxi, Jiangsu 214122, P. R. China
bInstitute of Colloid and Interface Chemistry, College of Chemistry and Chemical Engineering, Fuzhou University, Fuzhou, Fujian 350108, P. R. China. E-mail: jxzhao.colloid@fzu.edu.cn

Received 20th August 2015 , Accepted 15th September 2015

First published on 16th September 2015


Abstract

Stable foams were generated using a cationic gemini surfactant, ethanediyl-1,2-bis(dodecyldimethylammonium bromide) (12-2-12) together with a linear alcohol, hexanol (C6OH) or heptanol (C7OH), in aqueous solution. The foam stability was determined using the half-life of foam height falling (t1/2) as the index. The results showed that C7OH was more efficient than C6OH together with 12-2-12 to stabilize the foams. To generate the most stable foams, the optimum addition for both C6OH and C7OH was determined. The adsorption of the mixtures at the air/water interface was studied using surface tension measurements. The intermolecular interactions and the composition of the mixed monolayer were estimated by Rubingh–Rosen theory and the surface excess was derived from the Gibbs equation. The total surface excess that included both 12-2-12 and alcohols, was shown to significantly increase following the addition of alcohols suggesting the active molecules were more densely packed at the interface. The interfacial dilational rheology of the films was examined using the oscillating drop technique. The results showed that a highly stable foam always corresponded to a highly elastic adsorption film. The present study suggests a new formula for the generation of highly stable foams using a gemini surfactant with a short spacer together with a linear alcohol.


1. Introduction

Foams consist of gas bubbles separated by three-dimensional water channels and hence are metastable systems. Foam related techniques such as microcellular foaming technology have been applied to produce polymeric foams with highly oriented and elongated cell structures.1 It is known that the lifetime of an individual thin film that separates the two phases dominates the stability of foams. R. Krastev et al. reveal that the stability of foam films is related to the film thickness, the equilibrium of which is determined by the interplay of the dispersion attraction, electrical double-layer repulsion and short-range molecular interactions.2 Surfactants are the most commonly added compounds used to stabilize foams by preventing bubbles in the foam from coalescing and allowing the lifetime of the film to be greatly increased. Pioneering studies strongly suggested that films which can effectively stabilize foams should possess excellent interfacial viscoelasticity and be of particularly high elasticity.3–13 For example, D. Langevin et al.13 investigated the stability of foams formed by several nonionic surfactants. The foam evolvement was found to be controlled by film elasticity at different stages. The high film elasticity usually corresponds to a dense structure of the adsorption monolayer, where the adsorbed surfactant molecules are tightly packed.8,14,15

Gemini surfactant consists of two hydrophobic tails and two hydrophilic head-groups linked by a spacer per molecule.16 It has been clear that the gemini structure of a short spacer can form a densely packed monolayer at the air/water interface.17 In our previous studies, we have successfully constructed stable foams using gemini surfactants with a short spacer as stabilizers, such as ethanediyl-1,2-bis(alkyldimethylammonium bromide) or 2-hydroxyl-propanediyl-1,3-bis(alkyldimethylammonium bromide).18–20 Even so, however, there still remains gaps at the adsorption monolayers formed by the adsorbed gemini molecules due to the electrostatic repulsion. Consequently, the foam stability may be further enhanced if these gaps in the adsorption monolayers can be partly filled. To achieve this purpose, nonionic surfactants or linear alcohols with small head-groups may be effective additives. Many authors have studied the interactions of alcohols with ionic surfactants (including ionic gemini surfactants) and concluded that linear alcohols effectively promoted the ionic surfactant to form a dense adsorption monolayer.21–25 However, to our knowledge, none of these studies focused on the relationship between foam stability and system composition. This work first reports highly stable foams generated in the mixed systems of a gemini surfactant with a short spacer (12-2-12) and hexanol (C6OH) or heptanol (C7OH). The interfacial adsorption and the dilational viscoelasticity of the adsorbed films are characterized to explore the underlying mechanism. The presented system utilizes the advantages of gemini surfactant structure and provides a new formula of stable foam systems.

2. Experimental

2.1 Materials

Gemini surfactant, ethanediyl-1,2-bis(dodecyldimethylammonium bromide) (abbreviated as 12-2-12), was synthesized in our laboratory and confirmed by 1H NMR and elemental analysis (ESI). Hexanol (C6OH, AR) and heptanol (C7OH, AR) were purchased from Sinopharm Chemical Reagent Co. Ltd (China). All solutions were prepared with Milli-Q water with a resistivity of 18.2 MΩ cm.

2.2 Measurements

Foam stability. Foam stability was indexed by the half-life t1/2. This was the time required for the collapse of the foam to half of its initial height according to Tehrani-Bagha and Holmberg' proposals26 and was determined using the previously described setup.18 Air with a constant flow speed of 68 mL min−1 was bubbled through a porous glass disc fixed at the bottom of a cylindrical glass container (25 mm internal diameter, 140 mm height) filled with 5 mL of the test solution. Foam was produced until a height of 40 mm, i.e., a volume of 20 cm3, and the valve then shut immediately. The time needed for the collapse of the foam to half of its initial height was recorded. The experiments were repeated at least three times and all presented values were the means from these replicates. The temperature was kept at 25 ± 0.1 °C throughout the experiments using a water bath.
The surface tension. The surface tension of the surfactant aqueous solutions with or without additives was measured with a CHAN DCA-315 tension meter equipped with a Pt–Ir du Noüy ring to investigate adsorption at the air/water interface. The circumference of the ring was 5.930 cm. The ratio of the outside radius to the radius of the ring cross section (R/r) was 53.1218. The error of surface tension measurements was within 0.1 mN m−1.
Interface dilational rheology. Interface dilational rheology was measured using an optical angle meter OCA-20 with an oscillating drop accessory ODG-20. The equilibrated interface was disturbed by sinusoidal oscillations. The accessible frequency range was 0.01–1 Hz and the relative area (A) variation was ∼6%. These conditions followed the range of linear viscoelasticity. Oscillations led to sinusoidal changes in the surface area and the radius, i.e. in the drop shape. The changes in drop shape were monitored by a CCD camera with a minimum of 50 frames per second. At the end of the experiment, the software retrieved the images and calculated the change in area and respective changes in surface tension for each cycle. Using Fourier transform analysis, the complex dilational modulus (ε*) and phase angle (θ) were determined and the dilational elasticity ε and dilational viscosity η were calculated by the relations
 
ε = |ε∗|cos[thin space (1/6-em)]θ (1)
 
image file: c5ra16799j-t1.tif(2)

3. Results and discussion

3.1 Foam stability

Fig. 1 shows the semi-logarithmic plots of the characteristic decay time, t1/2, against the surfactant (12-2-12) concentration, Cs, in the presence of hexanol (C6OH) or heptanol (C7OH). For all the systems, t1/2 rapidly rose with increasing 12-2-12 concentration and plateaus over a narrow concentration range of 0.75–1.1 mmol L−1 irrespective of the addition of C6OH or C7OH. These characteristic concentrations were close to their cmcs in the presence of the alcohols as discussed in Section 3.2. In contrast, the longest decay time of the foams, t1/2,max, strongly depended on both the species and concentration of alcohols, which is more clearly shown in Fig. 2. For each added alcohol, a sharp maximum appeared in the plot of t1/2,max versus Ca (the concentration of alcohol). Compared with that of 12-2-12 alone, the addition of alcohol could greatly enhance the foam stability and the t1/2,max attained 1413 min at 5.5 mmol L−1 C6OH and 1497 min at 0.7 mmol L−1 C7OH, which were two-fold higher than that (754 min) stabilized by 12-2-12 without additive.20 Notably, the concentration of C7OH to yield the maximum of t1/2,max was only one-fifth of C6OH, indicating that C7OH was a much more efficient additive to reform the foams stabilized by 12-2-12.
image file: c5ra16799j-f1.tif
Fig. 1 Semi-logarithmic plots of foam decay time, t1/2, for foam height to fall by 50% as a function of 12-2-12 concentration in the presence of C6OH (a) and C7OH (b) at 25 °C.

image file: c5ra16799j-f2.tif
Fig. 2 The maximum foam stability time t1/2,max as a function of the added quantity of alcohol: (squares) C6OH and (circles) C7OH.

3.2 Surface tension curves

To understand the role of adding alcohols in stabilizing the foams, the surface tension of aqueous 12-2-12 solutions without and with different concentrations of alcohols was measured by the du Noüy ring technique. Fig. 3 shows the semi-logarithmic plots of surface tension versus surfactant concentration. At low surfactant concentrations, the systems with alcohol exhibited smaller values of surface tension than that for 12-2-12-alone. This was attributed to the formation of a mixed adsorption film that reduced the surface tension of water more effectively. From Fig. 3, the critical micelle concentration (cmc) could be derived from the break point. The minimum surface tension (γcmc) at the cmc and the concentration (C20) required to reduce a 20 mN m−1 surface tension of water were also obtained. The three parameters characterized the ability of micelle formation and the effectiveness and the efficiency in surface tension reduction, respectively.27 In the presence of alcohols, all three parameters were smaller than those generated by 12-2-12 alone (see Table 1), showing the synergistic effect of adding alcohols with 12-2-12. Comparatively, C7OH was more synergistic than C6OH with 12-2-12, which was also observed by Khan and colleagues.25 Thus, the quantity of C7OH required to produce identical synergism was considerably smaller than that of C6OH as seen in Fig. 3.
image file: c5ra16799j-f3.tif
Fig. 3 Semi-logarithmic plots of surface tension versus surfactant 12-2-12 concentration in the presence of C6OH (a) and C7OH (b) at 25 °C.
Table 1 Surface active parameters of surfactant systems at 25 °Ca
Systems cmc (mmol L−1) C20 (mmol L−1) γcmc (mN m−1) 1010Γ12-2-12 (mol cm−2) 1010ΓCOH (mol cm−2) 1010Γt (mol cm−2)
a ∗ indicates where the alcohol itself made the surface tension of water reduced to over 20 mN m−1. The data in parentheses are the total mole number of the alkyl tails (Γt,tails) at the interface per area unit (cm2) including the alkyl tails of both 12-2-12 and alcohol.
12-2-12 alone 0.91 0.18 30.6 2.54 2.54 (5.08)
[thin space (1/6-em)]
12-2-12 + C6OH with a constant concentration (mmol L−1):
4.0 0.89 0.12 28.4 2.32 0.75 3.07 (5.39)
5.0 0.86 0.11 27.3 2.24 0.92 3.16 (5.40)
5.5 0.84 0.093 27.1 2.21 1.02 3.23 (5.44)
6.0 0.84 0.075 26.8 2.19 1.10 3.29 (5.48)
6.5 0.82 0.073 26.7 2.16 1.18 3.34 (5.50)
8.0 0.81 0.064 26.5 2.10 1.41 3.51 (5.61)
10.0 0.79 0.025 26.3 2.03 1.79 3.82 (5.85)
12.0 0.77 24.1 1.93 1.94 3.87 (5.80)
[thin space (1/6-em)]
12-2-12 + C7OH with a constant concentration (mmol L−1):
0.3 0.89 0.18 30.2 2.39 0.40 2.79 (5.18)
0.5 0.88 0.16 29.8 2.32 0.57 2.89 (5.21)
0.7 0.87 0.14 29.4 2.27 0.76 3.03 (5.30)
1.0 0.86 0.11 28.5 2.23 0.95 3.18 (5.41)
2.0 0.85 0.059 26.7 2.12 1.38 3.50 (5.62)
3.0 0.79 0.025 24.3 1.98 1.96 3.94 (5.92)
4.0 0.75 22.6 1.87 2.47 4.34 (6.21)


3.3 Synergistic effect and mixed adsorption of 12-2-12/alcohol at the air/water interface

According to Rubingh–Rosen theory, the composition of a mixed adsorption monolayer (X1σ and X2σ, where the subscripts 1 and 2 stand for 12-2-12 and alcohol, respectively) and the molecular interaction parameter βσ can be calculated by following formulas27–29
 
image file: c5ra16799j-t2.tif(3)
 
image file: c5ra16799j-t3.tif(4)
where C1, C2 and C12 are respectively the mole concentrations of 12-2-12, alcohol and their mixture in the bulk solution required to produce a given surface tension value, and α1 and α2 (= 1–α1) are the mole fractions of 12-2-12 and alcohol in the bulk solution on an active component only basis. The activity coefficients f1σ and f2σ of the surfactant and the alcohol in the mixed monolayer are related to βσ
 
fσ1 = exp[βσ(1 − Xσ1)2] (5)
 
fσ2 = exp[βσ(Xσ1)2] (6)
βσ indicates the deviation from ideality. For ideal mixing of two components, βσ assumes a value of zero. A positive βσ value means repulsive interactions amongst mixed species whereas a negative βσ value corresponds to an attractive interaction. In addition, the value of βσ also exhibits the degree of interaction between the two components within the adsorption monolayer, i.e. the more negative the value, the greater the interaction. In the current study, all βσ values were negative (Table 2) suggesting that the interaction was more attractive between the two components in the monolayer than the self-interaction of each component before mixing. This phenomenon was consistent with the previous observation for the mixture of a similar gemini surfactant, butanediyl-1,4-bis(cetyldimethylammonium bromide) (16-4-16), and identical alcohols.25
Table 2 Surface composition (Xσ), activity coefficient (fσ) and interaction parameter (βσ) of binary mixtures of gemini surfactant 12-2-12 and alcohol calculated at 40 mN m−1a
  α2 Xσ1 Xσ2 fσ1 fσ2 βσ
a The CC6OH and CC7OH are the bulk concentrations of the corresponding alcohol in the solution. α2 is the mole fraction of alcohol on an active-component-only basis. The subscripts 1 and 2 represent surfactant and alcohol, respectively.
12-2-12 + C6OH
CC6OH/mmol L−1
4.0 0.918 0.757 0.243 0.948 0.598 −0.898
5.0 0.939 0.708 0.292 0.923 0.624 −0.940
5.5 0.947 0.684 0.316 0.907 0.633 −0.977
6.0 0.953 0.665 0.335 0.897 0.652 −0.967
6.5 0.958 0.647 0.353 0.887 0.670 −0.958
8.0 0.969 0.598 0.402 0.864 0.724 −0.903
10 0.979 0.532 0.468 0.822 0.777 −0.893
12 0.982 0.498 0.502 0.868 0.870 −0.563
[thin space (1/6-em)]
12-2-12 + C7OH
CC7OH/mmol L−1
0.3 0.418 0.864 0.136 0.967 0.259 −1.811
0.5 0.573 0.802 0.198 0.928 0.297 −1.891
0.7 0.678 0.750 0.250 0.884 0.330 −1.972
1.0 0.772 0.701 0.299 0.844 0.393 −1.901
2.0 0.891 0.606 0.394 0.805 0.598 −1.399
3.0 0.944 0.502 0.498 0.712 0.708 −1.368
4.0 0.963 0.431 0.569 0.717 0.827 −1.025


The Gibbs equation can be used to calculate the surface excess Γ:

 
image file: c5ra16799j-t4.tif(7)
where n is a constant depending on the number of species adsorbed at the interface. In Fig. 3, the semi-logarithmic plots of surface tension are represented as a function of the surfactant concentration and therefore Γ corresponds to the surface excess of 12-2-12 (Γs), where n is accounted for as 2, as suggested by other authors.30–33 For 12-2-12 alone, Γs is 2.54 × 10−10 mol cm−2, which is close to that reported by Sikirić et al.32 and Sun et al.33 Fig. 4 shows a gradual decrease in Γs with competitively adsorbing alcohol molecules. This phenomenon agreed with the mixture of cetyltrimethylammonium bromide (CTAB) and propanol, where the adsorption of CTAB at the solution–air interface decreased with increasing propanol concentration.34


image file: c5ra16799j-f4.tif
Fig. 4 Surface excess as a function of the concentration of alcohol in bulk solution for (a) 12-2-12/C6OH and (b) 12-2-12/C7OH mixtures: (circles) Γs, (filled circles) Γa and (squares) Γt.

The surface excess of alcohol Γa can be approximately estimated by following formula:

 
image file: c5ra16799j-t5.tif(8)

As seen in Fig. 4, Γa monotonously increased with addition of alcohol in the solution. Thus, total surface excess Γt (equal to the sum of Γs and Γa) kept rising with increasing concentration of alcohol in the bulk solution. Taking into account the two tails per gemini molecule, the total number of alkyl tails including both 12-2-12 and alcohol molecules absorbed at the air/water interface per area-unit (Γt,tails) was calculated as the sum of 2Γs and Γa. The results are listed in the parentheses in the last line of Table 1. With the addition of alcohol in the solution, the Γt,tails significantly increased and was always larger than that generated by 12-2-12 without additive. These results apparently indicate that the addition of alcohol promoted the formation of a more densely packed monolayer in comparison to that of 12-2-12 alone, agreeing with the role of linear alcohols in other surfactant systems.21–25 Moreover, the C7OH had higher efficiency than the C6OH. For example, at a comparable concentration of 4.0 mmol L−1 of alcohol, the Γt,tails was 6.21 mol cm−2 for C7OH and 5.39 mol cm−2 for C7OH, respectively (Table 1). As emphasized in the introduction, the densely packed monolayer is an important basis for enhancing foam stability because it creates high interfacial elasticity and is subsequently discussed in more detail.

3.4 Dilational rheology of adsorption films

Previous studies have suggested that foam stability is closely related to the elasticity of the surfactant adsorbed film.5,6,8,9,11–13 Briefly, the dilational behavior for a typical system of 12-2-12/0.7 mmol L−1 C7OH at different surfactant concentrations is illustrated, others are available in the ESI. Fig. 5 shows the experimental plots of the complex dilational modulus ε*, dilational elasticity ε, dilational viscosity η and phase angle θ as a function of the frequency of sinusoidal oscillation, all of these showed frequency dependence analogous to the previous observations.18–20 The increasing disturbance frequency resulted in a decrease in the response time, over which the surfactant molecules exchanged between the interface and the bulk, and also moved inside the monolayer to restore equilibrium. At low frequencies, the time of the surfactant response was sufficient and thus various relaxation processes coming from diffusion and adsorption of surfactants35 and/or conformational changes of adsorbed molecules36 can occur. At high frequencies, the response time was too short and the monolayer behaved as if it were insoluble. The phase angles were always positive for each of the mixtures over the range of examined frequencies, indicating that the phase of interfacial tension oscillation preceded that of the interfacial area oscillation.
image file: c5ra16799j-f5.tif
Fig. 5 Experimental plots of complex modulus (ε*, a), interfacial elasticity (ε, b), interfacial viscosity (η, c) and phase angle (θ, d) as a function of frequency (v), respectively, for the mixed adsorption films in 12-2-12/0.7 mmol L−1 C7OH aqueous solutions at 25 °C. The symbols represent different surfactant concentrations: log(C mmol−1 L−1) = −1.38 (□), −1.18 (○), −0.93 (△), −0.63 (▿), −0.52 (◇), −0.30 (⊲).

In addition to frequency influence, the bulk concentration of surfactant also determined the viscoelastic behavior of the solutions, which are shown in Fig. 6. At a designated frequency, the experimental ε and η run through a maximum with increasing surfactant concentration. This was similar to the behavior of both conventional surfactants9,14,15,37 and gemini surfactants18–20 at the air/water interface. Generally, an increase in the surfactant concentration in the bulk solution could have two effects, one was to increase the interface excess Γ, which, in turn, led to a higher elasticity and the second was to accelerate the molecular exchange between bulk and interface. The fast exchange at high concentration tended to even out any interface tension gradient dγ, which decreased the interfacial elasticity. Thus at low concentrations, the increase in ε was dominant, whereas at high concentrations, ε decreased as the molecular exchange was speeded up. This “crossover” was mirrored in a maximum of ε(C) curve.


image file: c5ra16799j-f6.tif
Fig. 6 Semi-logarithmic plots of dilational interfacial elasticity (ε, a) and interfacial viscosity (η, b) as a function of the surfactant concentration C for 12-2-12/0.7 mmol L−1 C7OH aqueous solutions. The symbols indicate different frequencies: ν/Hz = 0.010 (□), 0.046 (○), 0.100 (△), 0.464 (▿) and 1.000 (◇).

3.5 LVT model description for the experimental data

The Lucassen-van den Tempel (LVT) model was most commonly used to describe the viscoelastic behavior of the soluble monolayer.38,39 This model assumed that the material transport involved in the adsorption kinetics was governed only by diffusion without energy barriers and was considered the instantaneous coupling between the interface rheology and adsorption kinetics. The model predicted the viscoelastic moduli through the following equations
 
image file: c5ra16799j-t6.tif(9)
 
image file: c5ra16799j-t7.tif(10)
with
 
image file: c5ra16799j-t8.tif(11)
where ε0 is the theoretical high-frequency limit of surface elasticity and ω0 is the molecular exchange parameter. Fig. 7 shows the fitting results for the system of 12-2-12/0.7 mmol L−1 C7OH using eqn (9) and (10), in which the LVT model describes the experimental data accurately.

image file: c5ra16799j-f7.tif
Fig. 7 Concentration dependent plots of high-frequency limit elasticity ε0,fit for (a) 12-2-12/C6OH and (b) 12-2-12/C7OH mixtures.

According to the LVT model, at low frequencies, the dilational interfacial elasticity was close to zero, irrespective of the concentration of surfactant in the bulk phase as seen in Fig. S16. This could be explained as the interfacial tension gradient resulting from interface deformation almost vanished during the experimental time. At high frequencies, the dilational elasticity showed little change with further increasing frequency. Over this range, the work frequency was significantly higher than the characteristic frequency of the various relaxation processes occurring at and near the interface, and thus the interface film embodied the character of insoluble film. By eqn (11), ξ approaches to 0 when ν → ∞, and thus ε = ε0 according to eqn (9). This procedure appeared simplistic but the high-frequency limit of elasticity could not often be determined since the high-frequency limit was not included experimentally. Thus the fitting parameters ε0,fit and ω0,fit were considered to substitute for ε0 and ω0. The fitting procedure was carried out so that the couples of ε0,fit and ω0,fit values best described both the experimental ε(ν, C) and η(ν, C) curves. Table S3 lists the fitting results for several of the typical systems. As revealed in Fig. 7, the ε0,fit was also concentration-dependent analogous to ε0.

3.6 Film elasticity and foam stability

In the studies a relationship between the foam stability and the elasticity of the film has been shown.18–20 High interfacial elasticity is closely related to high foam stability. However, it was noticed that in this relationship the interfacial elasticity should choose its high-frequency limit where the influence of frequency can be excluded. For 12-2-12/C6OH mixtures, Fig. 7a shows that at a comparable surfactant concentration, the ε0,fit in the presence of 5.5 mmol L−1 alcohol was always larger than the other two ε0,fit generated in the presence of 4.0 and 8.0 mmol L−1 C6OH. Similarly, for 12-2-12/C7OH mixtures, the ε0,fit in the presence of 0.7 mmol L−1 alcohol was also the largest at comparable surfactant concentrations (Fig. 7b). This explained that the optimum effect of adding alcohols in enhancing foam stability was at 5.5 mmol L−1 for C6OH and 0.7 mmol L−1 for C7OH, respectively, as shown in Fig. 2.

As indicated in previous studies,18–20 a more quantitative analysis should be based on the limit of elasticity obtained on the level of identical surface excesses rather than that of the same concentrations in the bulk solution.14,18–20 For this purpose, we plotted the adsorption isotherms with a Frumkin-form (Fig. 8), which were derived from fitting the surface tension data by Szyszkowski formula and then calculating the surface excesses by the Gibbs equation.27 Combining Fig. 7 and 8, at an identical surface excess of 2 × 10−10 mol cm−2, the ε0,fit was 218 mN m−1 for 12-2-12/0.7 mmol L−1 C7OH and 195 mN m−1 for 12-2-12/5.5 mmol L−1 C6OH, respectively. The larger ε0,fit for the C7OH system than that for the C6OH system mirrored the higher foam stability for the former as indicated in Section 3.1.


image file: c5ra16799j-f8.tif
Fig. 8 Frumkin adsorption isotherms for 12-2-12/5.5 mmol L−1 C6OH (a) and 12-2-12/0.7 mmol L−1 C7OH (b) mixtures.

4. Conclusions

This paper investigated highly stable foam systems generated by a cationic gemini surfactant, ethanediyl-1,2-bis(dodecyldimethylammonium bromide) (12-2-12), together with a linear alcohol, hexanol (C6OH) or heptanol (C7OH). The maximum half-life t1/2,max of bubbles attained 1413 min for 12-2-12/5.5 mmol L−1 C6OH and 1497 min for 12-2-12/0.7 mmol L−1 C7OH, which were two-fold higher than that stabilized by 12-2-12 without additives. The added alcohol can further fill in the gaps of the monolayers formed by the gemini surfactant with a short spacer, producing more stable foams. The adsorption and interfacial rheology measurements reveal that the foam stability is closely related to the surface activity and interfacial elasticity of the mixed systems. Addition of alcohols decreases the cmc and γcmc of 12-2-12, indicating the aggregation and adsorption of mixed systems are greatly enhanced because of the synergistic effect of alcohols with 12-2-12. All values of interaction parameter βσ for mixed systems are negative, suggesting the presence of attractive interactions between the two components in the monolayer. At an identical surface excess of 2 × 10−10 mol cm−2, the ε0,fit obtained by fitting interfacial rheology data with LVT model was 218 mN m−1 for 12-2-12/0.7 mmol L−1 C7OH and 195 mN m−1 for 12-2-12/5.5 mmol L−1 C6OH, respectively. These results reveal that 12-2-12/C7OH systems can generate more stable foams at lower alcohol concentrations than that of 12-2-12/C6OH, indicating that alcohols with longer alkyl tail length are more effective additives in stabilizing foams. The obtained results suggest a new formula to generate highly stable foams using a gemini surfactant with a short spacer together with a linear alcohol. The systems presented have potential wide ranging applications in the construction of new complex fluids.

Acknowledgements

Support from the National Natural Science Foundation of China (Grants No. 21473032 and 21273040) is gratefully acknowledged.

References

  1. T. R. Kuang, H. Y. Mi, D. J. Fu, X. Jing, B. Y. Chen, W. J. Mou and X. F. Peng, Ind. Eng. Chem. Res., 2015, 54, 758–768 CrossRef CAS.
  2. J. L. Toca-Herrera, N. Krasteva, H. J. Muller and R. Krastev, Adv. Colloid Interface Sci., 2014, 207, 93–106 CrossRef CAS PubMed.
  3. J. L. Joye, G. Hirasaki and C. A. Miller, Langmuir, 1994, 10, 3174–3179 CrossRef CAS.
  4. J. L. Joye, G. Hirasaki and C. A. Miller, J. Colloid Interface Sci., 1996, 177, 542–552 CrossRef CAS.
  5. A. A. Sonin, A. Bonfillon and D. Langevin, J. Colloid Interface Sci., 1994, 162, 323–330 CrossRef CAS.
  6. A. Espert, R. V. Klitzing, P. Poulin, A. Colin, R. Zana and D. Langevin, Langmuir, 1998, 14, 4251–4260 CrossRef CAS.
  7. H. Fruhner, K. D. Wantke and K. Lunkenheimer, Colloids Surf., A, 1999, 162, 193–202 CrossRef.
  8. V. Bergeron, Langmuir, 1997, 13, 3474–3482 CrossRef CAS.
  9. C. Stubenrauch and R. Miller, J. Phys. Chem. B, 2004, 108, 6412–6421 CrossRef CAS PubMed.
  10. P. Koelsch and H. Motschmann, Langmuir, 2005, 21, 6265–6269 CrossRef CAS PubMed.
  11. E. Santini, F. Ravera, M. Ferrari, C. Stubenrauch, A. Makievski and J. Krägel, Colloids Surf., A, 2007, 298, 12–21 CrossRef CAS PubMed.
  12. L. Wang and R. H. Yoon, Int. J. Miner. Process., 2008, 85, 101–110 CrossRef CAS PubMed.
  13. D. Georgieva, A. Cagna and D. Langevin, Soft Matter, 2009, 5, 2063–2071 RSC.
  14. F. Monroy, J. Giemanska-Kahn and D. Langevin, Colloids Surf., A, 1998, 143, 251–260 CrossRef CAS.
  15. C. Stenvot and D. Langevin, Langmuir, 1988, 4, 1179–1183 CrossRef CAS.
  16. F. M. Menger and C. A. Littau, J. Am. Chem. Soc., 1991, 113, 1451–1452 CrossRef CAS.
  17. E. Alami, G. Beinert, P. Marie and R. Zana, Langmuir, 1993, 9, 1465–1467 CrossRef CAS.
  18. X. N. Wu, J. X. Zhao, E. J. Li and W. S. Zou, Colloid Polym. Sci., 2011, 289(9), 1025–1034 CAS.
  19. Y. You, X. N. Wu, J. X. Zhao, Y. Z. Ye and W. S. Zou, Colloids Surf., A, 2011, 384, 164–171 CrossRef CAS PubMed.
  20. X. N. Wu, W. S. Zou and J. X. Zhao, Acta Phys.-Chim. Sin., 2012, 28, 1213–1217 CAS.
  21. B. D. Casson and C. D. Bain, J. Phys. Chem. B, 1999, 103, 4678–4686 CrossRef CAS.
  22. M. Villeneuve, N. Ikeda, K. Motomura and M. Aratono, J. Colloid Interface Sci., 1998, 204, 350–356 CrossRef CAS PubMed.
  23. H. Matsubara, T. Eguchi, H. Takumi, K. Tsuchiya, T. Takiue and M. Aratono, J. Phys. Chem. B, 2009, 113, 8847–8853 CrossRef CAS PubMed.
  24. R. Mohammad, I. A. Khan, Kabir-ud-Din and P. C. Schulz, J. Mol. Liq., 2011, 162, 113–121 CrossRef CAS PubMed.
  25. I. A. Khan, R. Mohammad, S. Alam and Kabir-ud-Din, J. Dispersion Sci. Technol., 2010, 31, 129–137 CrossRef CAS PubMed.
  26. A. R. Tehrani-Bagha and K. Holmberg, Langmuir, 2010, 26, 9276–9282 CrossRef CAS PubMed.
  27. M. J. Rosen, Surfactants and Interfacial Phenomena, John Wiley & Sons Inc., 2nd edn, 1988 Search PubMed.
  28. D. N. Rubingh, in Solution Chemistry of Surfactants, ed. K. L Mittal, Plenum, New York, 1979, vol. 1, pp. 337–354 Search PubMed.
  29. M. J. Rosen and X. Y. Hua, J. Colloid Interface Sci., 1982, 86, 164 CrossRef CAS.
  30. R. Zana, J. Colloid Interface Sci., 2002, 248, 203–220 CrossRef CAS PubMed.
  31. Z. X. Li, C. C. Dong and R. K. Thomas, Langmuir, 1999, 15, 4392–4396 CrossRef CAS.
  32. M. Sikirić, I. Primŏzič and N. Filipović-Vinceković, J. Colloid Interface Sci., 2002, 250, 221–229 CrossRef PubMed.
  33. Y. Sun, Y. Feng, H. Dong, Z. Chen and L. Han, Cent. Eur. J. Chem., 2007, 5, 620–634 CrossRef CAS.
  34. A. Zdziennicka and B. Hańczuk, J. Colloid Interface Sci., 2008, 317, 44–53 CrossRef CAS PubMed.
  35. J. Lucassen and M. van den Tempel, Chem. Eng. Sci., 1972, 27, 1283–1291 CrossRef CAS.
  36. F. Monroy, S. Rivillon, F. Ortega and R. G. Rubio, J. Chem. Phys., 2001, 115, 530–539 CrossRef CAS PubMed.
  37. V. I. Kovalchuk, J. Krägel, A. V. Makievski, F. Ravera, L. Liggieri, G. Loglio, V. B. Fainerman and R. Miller, J. Colloid Interface Sci., 2004, 280, 498–505 CrossRef CAS PubMed.
  38. J. Lucassen and M. van den Tempel, Chem. Eng. Sci., 1972, 27, 1283–1291 CrossRef CAS.
  39. J. Lucassen and M. van den Tempel, J. Colloid Interface Sci., 1972, 41, 491–498 CrossRef CAS.

Footnote

Electronic supplementary information (ESI) available. See DOI: 10.1039/c5ra16799j

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