Juan
Teng
,
Min
Lin
,
Jing
Gao
,
Xuezhi
Dai
,
Xianqiu
Lan
and
Hang
Song
*
School of Chemical Engineering, Sichuan University, Chengdu 610065, China. E-mail: 714433744@qq.com; 1554065674@qq.com; 1248381392@qq.com; xuezhidai@outlook.com; 13699006688@163.com; hangsong@vip.sina.com; Tel: +86 28 85405221
First published on 14th November 2018
A new type of tropine-based ionic liquid (IL) gels were synthesized and characterized by Fourier transform infrared spectra (FT-IR), elemental analysis (EA), X-ray diffraction (XRD), thermogravimetric analysis (TGA), scanning electron microscopy (SEM) and zeta potential measurements, and the swelling behavior of ionic liquid (IL) gels were further investigated. FT-IR, EA and XRD indicated the successful synthesis of IL gels, TGA analysis showed that the IL gels had good thermal stability, SEM showed that the introduction of ILs made the gel surface rough, and increased the specific surface area. The swelling values of IL gels were well correlated by the second-order kinetics equation with the correlation coefficients of at least 0.99. Furthermore, the IL gels were used as adsorbent to adsorb bovine albumin (BSA), the maximum adsorption capacity was up to 700 mg g−1.
Gels have unique water absorption, water retention and bionic characteristics. Gels were widely used in industrial, agricultural, pharmaceutical and bio-engineering materials and other fields.14 Recently, modified gels have been reported and used as separation media in protein absorption,15,16 and showed satisfactory performance. ILs gels were used to modified carbon nanotubes17 and absorption dyes.18
BSA is the main component of bovine plasma protein, accounting for about 42% of total plasma protein.19 The structure of BSA is similar to that of human serum albumin (HSA).20 Therefore, BSA is often widely used as a protein model for in vitro studies, which requires isolation of protein samples. However, the currently studied materials21–23 have low adsorption capacity for proteins, generally ranging from a few milligrams to tens of milligrams of protein per gram of material, and have poor biocompatibility.24–27
Very recently, tropine-based ILs have been synthesized by us and successfully used to extract active ingredients from Chinese medicine28 or to separate proteins.29 In this study, tropine-based ILs were constructed into gels to obtain a new type of separation media. FT-IR, EA, XRD, TGA, SEM and zeta potential were used to characterize the synthesized IL gels. Moreover, the swelling behavior of IL gels were investigated and corrected by Fick model and second-order model. The synthesized IL gel was used for BSA adsorption.
:
1.2) were taken in a 100 mL single-necked flask with 30 mL ethyl acetate as solvent. The flask was sealed and the contents reacted in dark for 24 h at room temperature. The white crude product obtained was washed 3 times with 30 mL of ethyl acetate after reaction, and dried in vacuum for 24 h at 80 °C, then the white tropine-based ILs ([ATropine]+[Cl]−) was obtained with a yield of 96%.
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| Fig. 1 The synthesis route of IL gels (green bud-like icon represents [ATropine]+[Cl]−, the line connecting this structure was one or more MBA molecules, they polymerize to form a network structure). | ||
The synthesis route of ILs gels is depicted in Fig. 1(b), briefly, a certain amount of [ATropine]+[Cl]−, MBA (as cross-linking agent), AIBN (as initiator, accounted for 10% of the total mass of reactants) and methanol (as solvent) were taken in a 100 mL three-necked flask and were reacted at 50 °C for 6 h. After the reaction, the crude white gel was washed 3 times with 30 mL ethanol, and dried by vacuum freezing drying method, after which the gels were obtained. Four gels (Gel 0, Gel a, Gel b, Gel c) with different compositions were synthesized under the same procedure except that different molar ratio of [ATropine]+[Cl]−: MBA was used (the molar ratio of [ATropine]+[Cl]−: MBA were 0
:
1, 1
:
1, 2
:
1, 3
:
1, respectively).
| W (%) = M1/M0 × 100% | (1) |
| Q = (C0 − C1)V/m | (2) |
O at 1650 cm−1, the strong peak at 1530 cm−1 was the symmetrical bending vibration of N–H, which was peculiar to N–H trans-conformation. These peaks can also be found in the corresponding position in Gel b, which indicated that the MBA component was involved in the formation of Gel b. Comparing Gel 0 and Gel b, the peak of the anti-symmetrical stretching vibration of Gel 0 at 2916 cm−1 methylene produces a blue shift; this was because methylene groups in the cationic components of the tropine ILs and methylene groups of MBA influences by loss of charge. The C–H antisymmetric stretching vibration of methylene produces a blue shift. The introduction of ILs enhances the peaks at 1450 cm−1 and 1296 cm−1. The biggest difference between Gel b and Gel 0 was that a new peak appears below 1200 cm−1; for example, the new peak at 1042 cm−1 was the symmetrical bending vibration of O–H. Comparing Gel b and [ATropine]+[Cl]−, Gel b at 3700 cm−1 to 3300 cm−1 has stretching vibration peaks of N–H instead of [ATropine]+[Cl]− at 3274 cm−1, which has stretching vibration peaks of O–H. Meanwhile, for [ATropine]+[Cl]−, stretching vibration peak of
C–H at 3030 cm−1 disappears; it also showed that [ATropine]+[Cl]− participates in the polymerization reaction.
:
MBA = 2
:
1, ILs accounted for the largest mass fraction of the gel was obtained, which was 51.59%. When the ratio of [ATropine]+[Cl]− and MBA in the formulation increased from 2
:
1 to 3
:
1, the proportion of ILs in the fraction of the ILs gel obtained decreased from 51.59% to 43.07%. This may be because as the proportion of addition of [ATropine]+[Cl]− increases, part of the [ATropine]+[Cl]− preferentially polymerizes but with only a small amount of MBA into polymer molecules. Since the content of ILs component in the molecule predominates, the formed polymer molecules had a linear non-reticulated structure and had a relatively high polarity, thereby dissolving in a solvent. This part of the polymer molecule dissolved in the solvent consumes [ATropine]+[Cl]−, so that the mass fraction of ILs in the polymer molecule precipitated from the solvent was lowered.
| ILs Gel | ILs (g) | MBA (g) | AIBN (g) | Mass ratio of ILs |
|---|---|---|---|---|
| Gel 0 | 0 | 1 | 0.02 | 0 |
| Gel a | 1 | 1 | 0.20 | 37.17% |
| Gel b | 2 | 1 | 0.30 | 51.59% |
| Gel c | 3 | 1 | 0.40 | 43.07% |
The swelling or contraction process of the gel mainly reflects the hydrophilic groups in the gel, or the interaction of the hydrophobic groups with the solvent. If the hydrophilic group forms a hydrogen bond with the solvent, the solvent easily penetrates into the gel, which means that the gel has a large swelling ability in such a solvent; in contrast, if the hydrophilic group is incapable of forming hydrogen bonds with a solvent, the swelling ability of the gel in such a solvent is small.33 Moreover, the amount of the initiator is different, and the chain length of the synthesis is different, which also causes the difference in swelling ability; the crosslinking density also has a certain influence on the swelling ability of the gel. However, the reason for different trends of swelling ratio in water and in alcohols is still unclear.
The swelling dynamics is used to describe the swelling rate of gel. The data can be fitted with the empirical equation to obtain more information about the swelling process. The most commonly used swell dynamics models are the Fick model (eqn (3))34 and the second-order dynamics model (eqn (4)):35
| Wt = Kpt0.5 | (3) |
| t/W = 1/KsWe2 + t/W∞ | (4) |
The dynamics experiment was carried out in 0.01 M phosphate buffer (PBS). Fig. 8(a) shows the change in IL gels swelling ratio as a function of time. The variation in swelling behaviours of IL gels in PBS is the same as that in water, the swelling ratio follows the order Gel c > Gel a > Gel b > Gel 0.
![]() | ||
| Fig. 8 (a) The time dependence of swelling ratio for IL gels. (b) The fitted plots of Fick model. (c) The fitted plots of second-order dynamics model. | ||
To further discuss the swelling behaviour of IL gels, the swelling data were fitted by Fick model and second-order dynamics model, the fitted plots are shown in Fig. 8(b and c), respectively, and the fitted parameters are listed in Table 2.
| Sample | R 2 | |
|---|---|---|
| Fick model | Second-rate model | |
| Gel 0 | 0.9885 | 0.9911 |
| Gel a | 0.9904 | 0.9986 |
| Gel b | 0.9920 | 0.9993 |
| Gel c | 0.9945 | 0.9995 |
From Fig. 8(b), the swelling behaviour can be well described by the Fick function only before the swelling reaches equilibrium. The expression of the Fick model is that the diffusion coefficient is constant, but in the early and late swelling, the diffusion coefficient of the solvent in the different swelling ratio of the gel is variable, so the Fick model did not describe the swelling of the gel well. Fig. 8(c) showed that the swelling data of IL gels can be well fitted with the second-order dynamics model in the whole range. It can be seen from Table 2 that the swelling data of IL gels can be well correlated by both Fick model and second-order dynamics model, but the second-rate model can provide more ideal correlation results with R2 above 0.99.
| Entry | BSA initial concentration (mg mL−1) | Adsorbent temperature (°C) | Adsorption time (h) | Solid–liquid ratio (g L−1) | pH | Adsorbing capacity (mg g−1) |
|---|---|---|---|---|---|---|
| 1 | 0.6 | 25 | 4 | 2.5 | 7.2 | 73.3 |
| 2 | 1.0 | 25 | 4 | 2.5 | 7.2 | 236.7 |
| 3 | 1.2 | 25 | 4 | 2.5 | 7.2 | 351.6 |
| 4 | 1.4 | 25 | 4 | 2.5 | 7.2 | 471.2 |
| 5 | 1.6 | 25 | 4 | 2.5 | 7.2 | 583.9 |
| 6 | 2.0 | 25 | 4 | 2.5 | 7.2 | 724.4 |
| 7 | 2.2 | 25 | 4 | 2.5 | 7.2 | 731.8 |
| 8 | 2.4 | 25 | 4 | 2.5 | 7.2 | 733.1 |
| 9 | 2.6 | 25 | 4 | 2.5 | 7.2 | 734.5 |
| Entry | BSA initial concentration (mg mL−1) | Adsorbent temperature (°C) | Adsorption time (h) | Solid–liquid ratio (g L−1) | pH | Adsorbing capacity (mg g−1) |
|---|---|---|---|---|---|---|
| 1 | 2.2 | 25 | 4 | 1.0 | 7.2 | 567.8 |
| 2 | 2.2 | 25 | 4 | 2.0 | 7.2 | 558.1 |
| 3 | 2.2 | 25 | 4 | 2.5 | 7.2 | 541.2 |
| 4 | 2.2 | 25 | 4 | 4.0 | 7.2 | 439.4 |
| 5 | 2.2 | 25 | 4 | 5.0 | 7.2 | 369.8 |
| 6 | 2.2 | 25 | 4 | 7.5 | 7.2 | 278.7 |
| 7 | 2.2 | 25 | 4 | 10.0 | 7.2 | 201.3 |
| 8 | 2.2 | 25 | 4 | 12.5 | 7.2 | 168.5 |
| Entry | BSA initial concentration (mg mL−1) | Adsorbent temperature (°C) | Adsorption time (h) | Solid–liquid ratio (g L−1) | pH | Adsorbing capacity (mg g−1) |
|---|---|---|---|---|---|---|
| 1 | 2.2 | 25 | 4 | 2.5 | 2 | 68.9 |
| 2 | 2.2 | 25 | 4 | 2.5 | 3 | 278.8 |
| 3 | 2.2 | 25 | 4 | 2.5 | 4 | 540.2 |
| 4 | 2.2 | 25 | 4 | 2.5 | 5 | 698.1 |
| 5 | 2.2 | 25 | 4 | 2.5 | 6 | 491.4 |
| 6 | 2.2 | 25 | 4 | 2.5 | 7 | 446.7 |
| 7 | 2.2 | 25 | 4 | 2.5 | 8 | 382.5 |
| 8 | 2.2 | 25 | 4 | 2.5 | 9 | 271.8 |
| 9 | 2.2 | 25 | 4 | 2.5 | 10 | 245.6 |
| 10 | 2.2 | 25 | 4 | 2.5 | 11 | 223.9 |
| Entry | BSA initial concentration (mg mL−1) | Adsorbent temperature (°C) | Adsorption time (h) | Solid–liquid ratio (g L−1) | pH | Adsorbing capacity (mg g−1) |
|---|---|---|---|---|---|---|
| 1 | 2.2 | 25 | 0.5 | 2.5 | 5 | 509.2 |
| 2 | 2.2 | 25 | 1 | 2.5 | 5 | 625.7 |
| 3 | 2.2 | 25 | 1.5 | 2.5 | 5 | 653.1 |
| 4 | 2.2 | 25 | 2 | 2.5 | 5 | 709.6 |
| 5 | 2.2 | 25 | 2.5 | 2.5 | 5 | 711.3 |
| 6 | 2.2 | 25 | 3 | 2.5 | 5 | 713.4 |
| 7 | 2.2 | 25 | 3.5 | 2.5 | 5 | 714.8 |
| 8 | 2.2 | 25 | 4 | 2.5 | 5 | 715.2 |
The structure of proteins is sensitive to temperature and can change drastically with a slight change in temperature, so 25 °C was selected as the experimental temperature.
According to Table 3, with the increase of the BSA initial concentration, the adsorption capacity of IL Gel (b) first rapidly increases, and finally stabilizes after the BSA initial concentration of about 2.2 mg mL−1. At the low BSA concentration, the adsorbent has abundant adsorption sites, which enables most BSA to be adsorbed, but the total capacity of BSA is limited, so the adsorption amount is low.36 Therefore, the BSA initial concentration of 2.2 mg mL−1 is used for further investigations.
It can be seen from Table 4 that the solid–liquid ratio has a significant influence on the adsorption capacity. As the solid–liquid ratio increases, the adsorption capacity of IL gels steeply decreases after the solid–liquid ratio of about 2.5 g L−1. Although the increase in the solid–liquid ratio provides many adsorption sites, there are still many adsorption sites that are not adsorbed after the adsorption of BSA in the solution is completed. Thus, the solid–liquid ratio of 2.5 g L−1 was selected for further investigations.
In general, the pH has two main effects on the adsorption process: one is to change the surface charge properties and change the amount of adsorbent, the second is to change the surface charge properties and change the amount of protein. According to Table 5, in the range of pH 2–10, the adsorption amount of IL gels for BSA increases first and then decreases with the increase of pH value. When the pH is 5, the adsorption amount reaches the maximum. Considering that the isoelectric point of BSA is 5, and the adsorption effect of IL gels on BSA is good and did not destroy the protein activity, the experiment was carried out with the pH 5. As the pH changed, the charged amount of BSA in the solution changed, and the interaction between BSA and the IL gels also changed, so that the adsorption amount of BSA by the IL gels changes. Since the pH value of the solution will affect the conformation of the protein to certain extent, the peracid and alkali would destroy the natural activity of the protein. In addition, when the pH was lower or higher than the isoelectric point of the protein, the adsorption capacity was lowered due to the electrostatic repulsion. When the pH was equal to the isoelectric point of the protein, there was no net charge on the protein, and the adsorption effect was the best, which was similar to the results in the literature.36,37 Therefore, pH = 5 was selected for further investigations.
Table 6 shows that the adsorption time of the adsorbing capacity of BSA increases first and then stabilizes. Although IL gels provide many sites of adsorption, BSA proteins still take some time to occupy the active site. Considering that the adsorption equilibrium was attained in about 2 h, it was selected as the adsorption time for further investigations.
In the same optimization condition of 25 °C coupled with the BSA initial concentration of 2.2 mg mL−1, the solid–liquid ratio of 2.5 g L−1, the pH value of 5 and the adsorption time of 2 h, the adsorption capacity was up to 312.4 mg g−1, 715.3 mg g−1 and 728.5 mg g−1 for ILs gel (a), (b) and (c), respectively.
Compared with other reported adsorbent materials as summarized in Table 7, the synthesized IL gels exhibit comparable high adsorption capacity. It can be explained as follows: IL gels are hydrophilic gels, which have the characteristics of rapid water absorption and swelling properties, so that the adsorbed substrate can enter the interior of the gel adsorbent with the solution of fast and low resistance, so as to interact with the adsorption site inside the gel.
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