Maria Victoria Tuttolomondoa,
Juan Manuel Galdopórporaa,
Lea Trichetb,
Hugo Voisinb,
Thibaud Coradinb and
Martin Federico Desimone*a
aIQUIMEFA-CONICET, Facultad de Farmacia y Bioquimica, Universidad de Buenos Aires, Junin 956 Piso 3, (1113) Ciudad Autónoma de Buenos Aires, Argentina. E-mail: desimone@ffyb.uba.ar; Fax: +54-1149648254; Tel: +54-1149648254
bSorbonne Universités, UPMC Univ Paris 06, CNRS, UMR 7574, Laboratoire de Chimie de la Matière Condensée de Paris, F-75005 Paris, France
First published on 24th June 2015
A large family of azo dyes have been developed and used in the textile industry, including for leather tainting, and are therefore expected to exhibit strong interactions with collagen-based materials. Here we investigate the mechanisms of adsorption of the Remazol black B dye on type I collagen hydrogel. Higher and stronger retention of the dye is achieved in alkaline conditions, correlated with enhanced thermal and mechanical stability of the hydrogel. The formation of a covalent bond between the dye and the protein network via a Michael reaction is suggested and supported by the detailed analysis of the kinetics and thermodynamics of the sorption reaction. Type I collagen hydrogels combine low cost, fast sorption, high loading and strong retention capacity together with low storage volume, making them promising materials for dye remediation. Dye-modified hydrogels may also find applications in the biomedical field.
From an environmental point of view, special interest in dyes arises from the fact that, even at very low concentration (down to 1 ppm), they can make water highly colored, making it not only aesthetically unacceptable, but also preventing light from reaching the deeper layers of water curses, altering the flora and in consequence the fauna of the aqueous ecosystems. There are cases where this change is so drastic that eutrophication takes place.4 In addition, azo dyes (whatever their type) can suffer NN bond rupture if the conditions of the medium are reductive, producing and releasing aromatic amines to the water bodies. These amines are considered extremely toxic due to their carcinogenic properties.5–7
Traditional waste water treatments are generally inefficient when dealing with water contaminated with such kinds of synthetic dyes because of their chemical stability.8 There are many ways of treating contaminated waters, namely physical, chemical and biological treatments.9–14 The less costly are the physical ones based on adsorption.15–18 When dealing with azo dyes the latter can be considered the safest because no breakage of the azo bond occurs, drastically diminishing the probability of generating potentially toxic aromatic amines.19 On the other hand, a common problem associated with adsorption is related to the adsorption products disposal, which implies a waste moving cost to a preliminary storage place before the final disposal of the waste. Additionally, this transient storage place can create a second contamination source if the dye leaks out or permeates through the sorbent and reaches the soil.
Considering that many dyes have been developed for strong binding on leather products that are skin-based materials and, therefore, rich in type I collagen, we hypothesized that collagen hydrogels could also interact strongly with these molecules. Type I collagen is a very abundant and well characterized biomolecule that accounts for 35% of the dry weight of any mammal. The basic structure of type I collagen is –gly–X–Y–gly– where X and Y are proline and 4-hydroxyproline respectively.20–24 From a physicochemical point of view it is a semi-flexible helicoidal polyelectrolyte, 300 nm in length and 1.5 nm in diameter. Assembled within fibrils, the collagen molecule ends are displaced from each other about 67 nm, which produces the characteristic striations seen in TEM microscopy. Importantly type I collagen is a waste product of many industries and it is cheap and easy to obtain in a purified form.25
In this work, we have studied the adsorption of Remazol black B, a sulfonated reactive azo dye, on type I collagen hydrogels. We demonstrate that the highest sorption rates are obtained in alkaline conditions where electrostatic interactions are expected to be repulsive, suggesting the formation of covalent bonds between the dye and the protein network via a Michael addition reaction. This hypothesis is supported by the significant increase in thermal stability and rheological properties of the hydrogels. Detailed kinetics and thermodynamic analyses enlighten the co-existence of weak and strong chemisorption processes, whose balance depends on pH and dye concentration. Altogether type I collagen hydrogels combine several chemical, physical and economical advantages for their application as water cleaning sorbents. Further investigation of the biological behavior of dyed hydrogels will also be of interest.
After adjustment of the collagen concentration to 1.75 mg mL−1 with 500 mM acetic acid, aliquots of 250 μL of the solution were put in each well of a 24-well plate. The plate was incubated in NH3-saturated atmosphere at 20 °C until the hydrogel was obtained. The hydrogels were then left in a fume hood to evaporate the ammonia until the pH was neutral.
Differential Scanning Calorimetry (DSC) measurements were performed on a TA instrument model Q20. Temperature was calibrated with In (430 K, 3.3 J mol−1). Approximately 20 mg of each sample was first equilibrated at 20 °C before a ramp of temperature of 5 °C min−1 up to 90 °C was applied.
Rheological measurements were conducted on an Anton-Paar rheometer model MCR 302. The geometry used was a 25 mm diameter disk with a rough surface (reference PP 25/S). Collagen hydrogel at a 1.75 mg mL−1 concentration were placed in PTFE circular chambers with an inner diameter slightly larger than the geometry allowing rheological measurements at low modulus range. These samples were incubated in NH3 saturated atmosphere at 20 °C overnight and then washed with water and Tris buffer pH 9.00. The obtained hydrogels were incubated for 2 days either with an aqueous solution (8 mL) of Remazol black 2 mg mL−1 in Tris buffer or with Tris buffer alone for controls. The rheological behavior of the samples was investigated under sinusoidal deformations with a frequency of oscillations ranging from 0.1 to 100 Hz at set strain (0.1%) and under a normal force of 0.04 N. Frequency dependence of G′ and G′′ was recorded and oscillations up to 10 Hz were considered consistent. All experiments and their corresponding measurements were conducted in triplicate.
The FTIR spectra of samples were recorded on a Bruker spectrometer model Equinox 500. The hydrogels were lyophilized overnight and then crushed in a powder. The powder was then disposed on the diamond crystal of a Universal ATR Sampling Accessory and pressed before the obtention of the spectrum between 4000 and 600 cm−1 with a resolution of 1 cm−1. 16 scans were recorded under dry air purge. The corresponding measurements were conducted in triplicate. As a control a spectrum of Remazol black powder was also recorded.
The hydrogels used to perform rheology analysis were lyophilized overnight and then crushed as a powder. The powder was then disposed on the crystal of a Universal ATR Sampling Accessory and pressed before recording the spectrum between 4000 and 600 cm−1. The corresponding measurements were conducted in triplicate. As a control a spectrum of Remazol black powder was also recorded.
In additional experiments, Remazol black solutions were subjected to two pretreatments. In first place, an 800 μg mL−1 sodium bisulphite solution was added to a 2 mg mL−1 dye solution and the reaction left to proceed for 30 minutes at 60 °C to inactivate the vinylsulphone.30 Alternatively, hydrolysis of the vinylsulphone group of the dye was achieved by reaction with a 10 mg mL−1 NaOH solution at 90 °C for 1 hour, according to the procedure described by Agarwal et al.30
All experiments and their corresponding measurements were conducted in triplicate under identical conditions and statistically analyzed by one-way ANOVA. In all cases, the differences were considered to be significant when p < 0.05.
The pseudo-first-order equation is the simplest and most used to describe the adsorption of a solute in liquid solution onto an adsorbent. The law that defines the first order equation is:
(1) |
qt = qe(1 − e−klt) | (2) |
Alternatively, dye adsorption onto porous materials can follow a pseudo-second-order law that assumes the existence of delay in the adsorption process due to the presence of an outer limit layer or an external resistance. It can be expressed in the following way:
(3) |
(4) |
The Elovich equation can be applied to chemisorption processes and assumes that the adsorption sites are heterogeneous. It can be expressed as
(5) |
The modified Freundlich model, first developed by Kuo and Lotse, is described by
(6) |
(7) |
Langmuir and Freundlich models have been widely used to fit data in the biosorption equilibrium process. The first of them hypothesizes that the interaction between sorbate and sorbent is homogeneous, with homogeneous union sites until the first monolayer is formed on the sorbent surface. The second model has a better fit when adsorption sites are heterogeneous and have different interactions.32 The equations that describe both isotherms are:
Langmuir:
(8) |
Freundlich
qeq = kCeqn | (9) |
Another equation that was initially applied to gases but can be used to fit biosorbent adsorption data is the Dubinin–Radushkevich (DR) equation. This model assumes that pores are filled with adsorbed molecules according to adsorption force fields in the micropores and the interactions with the adsorbed molecules. When applying this equation to adsorption on solid phase, the adsorbed amount at any sorbate concentration is assumed to be a Gaussian function of the Polanyi potential (ε):33
qeq = qDRe−kDRε2 | (10) |
(11) |
The Temkin isotherm includes a factor that explicitly considers the sorbate–sorbent interactions. If extremely low and high values are ignored, the model assumes that the sorption heat (that is a function of the temperature) of all the molecules of a layer will decrease linearly instead of logarithmically as each layer is completed.34
(12) |
(13) |
qe = BlnAT + BlnCe | (14) |
The adsorption of Remazol black on these collagen hydrogels was investigated at pH 5.00, 7.00 and 9.00. As can be seen in Fig. 2, no significant difference in adsorption rate (p < 0.05) was evidenced when sorption was performed at pH 5.00 and 7.00, where 60% of the initial dye content is adsorbed. In contrast, at pH 9.00, nearly 80% of the dye was adsorbed to the collagen hydrogel.
Type I collagen is a polyampholyte polymer with 15–20% ionizable charges. Its maximum positive charge is achieved at pH 2.50 (+254 mV) and its isoelectric point is ca. pH 9.20. Between pH 6.50 and 9.00 it shows minimal electrostatic repulsion with a net value of +38 mV.20 Thus at pH of 5.00 and 7.00, collagen matrices are slightly positively-charged due to the presence of protonated amines allowing for attractive electrostatic interaction with the sulfonate-bearing negatively-charged RB molecules.35,36 However, these electrostatic interactions cannot account for the increase in dye sorption observed at pH 9.00. Rather it can be attributed to another reaction following the Michael addition mechanism that was previously reported to occur between vinylsulfone-bearing reactive dyes and free –NH2 (or –OH) groups of proteins, such as keratin and silk, in alkaline media.30,37–41 This reaction proceeds following the scheme presented in Fig. 3.
To test this hypothesis, the dye molecule was submitted to two different treatments, i.e. hydrolysis and blockage of the sulfonate group, before being put in contact with the collagen hydrogel. As shown on Fig. 2 both treatments leveled down the adsorption rates, which became insensitive to pH, supporting the idea that the vinylsulfone groups are involved in the non-electrostatic interactions occurring at pH 9.00 between the plain dye and collagen. Noticeably, the collagen molecule has a relatively small amount of free amino (lysine, arginine, histidine: 8%) and hydroxyl groups (serine, hydroxyproline, threonine: 14%) capable of reacting with the vinylsulphone group of the reactive dye via the Michael addition pathway, in fair agreement with the 20% increase in dye removal at pH 9.00 compared to neutral and acidic conditions.
Attempts made to desorb the dye at various pHs (from 4 to 10) and temperatures (from 4 °C to 37 °C) or using urea 6 M and NaCl 6 M were unsuccessful. Competitive sorption assays using other molecules with sulfate moieties such as chondroitin sulfate or the sodium sulfate salt did not hinder the binding of the dye. These results further support the existence of a covalent interaction between the dye and the collagen gel.
Attempts were made to identify the formation of the dye–collagen bond at pH 9.00 using FTIR. The main absorption bands in collagen samples are those from amide A (3400–3440 cm−1), amide I (CO stretching, 1656 cm−1), amide II (N–H stretching, 1592 cm−1) and amide III (C–N stretching and N–H stretching, 1145–1300 cm−1). These peaks validate the integrity in the conformation of the collagen molecules. Additional peaks at 1450 cm−1, 1315 cm−1 and 1240 cm−1 are associated with C–H bending modes C(CH2)2 torsion and CN stretching/NH deformation, respectively. The ratio of transmission intensity T1454/T1234 often used to assess the stability of proteins is close to 1, which indicates that the triple helical structure of collagen is conserved.42
Remazol black B displays peaks at 3483, 2929, 1660 and 1490 cm−1, for –OH stretching vibration, aromatic –CH stretching vibration, –CC– stretching and –NN– stretching vibration, respectively.43 Peaks at 1053 cm−1 and 1124 cm−1 represent the SOO asymmetric stretching in sulfonic acid groups. These peak values confirm the presence of –SO3−Na+ moieties in the dye structure.43 As shown on Fig. 4, the FTIR spectra of the dyed hydrogel gathers the main vibration bands of the two components, without significant variations in the relative peak intensities.
Fig. 4 FTIR spectra of collagen hydrogel, Remazol black and dyed hydrogel in the 4000 and 600 cm−1 (upper figure) and higher resolution in the 900 and 1600 cm−1 (lower) range. |
The impact of RB adsorption at pH 9.00 on the properties of the collagen hydrogels was also investigated by DSC and rheological measurements. As shown in Fig. 5, the initial collagen hydrogels have a denaturation temperature, corresponding to the breaking of the protein triple helix, near 55 °C in agreement with the literature.44 After dye sorption at pH 5.00 there were no significant differences in the thermal stability. Meanwhile there is a slight increase of approximately 4 °C at pH 7.00 and at pH 9.00, the thermal event is shifted to 68 °C. As a comparison, collagen hydrogels cross-linked using malondialdehyde, hexamethylene diisocyanate and glutaraldehyde exhibit 4.2 °C, 9.0 °C and 19 °C increase in the denaturation temperatures.45
Fig. 5 DSC profiles of a control collagen and a Remazol black dyed sample at various pHs. The samples were first equilibrated at 20 °C before the heating ramp. Exotherms are up. |
Pure collagen hydrogels tend to deform under their own weight and are relatively fragile (Fig. 6a) while dyed collagen gels keep their original shape and are easy to handle (Fig. 6b). Rheological measurements also indicate a significant stabilization of the collagen hydrogel upon reaction with RB (Fig. 6c). The G′ modulus at 10 kHz increased from 0.1 to 1 kPa and G′′ from 0.03 to 0.2 Pa. The increase in the values of G′ and G′′ is higher than the obtained with concentrated collagen hydrogels,46 collagen nanocomposites46 silicified collagen47 and even for some glutaraldehyde-fixed collagen hydrogels.46,47
The hydrogel cross-linking had another interesting consequence on its properties. When weight loss and volume reduction vs. time upon drying in ambient conditions were registered, both dye exposed and not exposed hydrogels showed a rapid weight loss during the first 40 minutes, followed by a continuous slow decrease down to 70 minutes (Fig. 7a). However, after 70 minutes, the RB–collagen gels exhibited ca. 5% of the initial volume (Fig. 7b–d) whereas the pure hydrogel volume was impossible to measure due to its extreme dehydration. This is attributed to the strong contraction of the collagen network upon drying while the crosslinking of the collagen by RB enhance interfibrillar interactions and therefore limits its contraction.48
To further understand the mechanisms of interactions between RB and collagen gels, the kinetics of dye sorption were investigated at pH 9.00. The sorption rate varied with the dye concentration but the sorption equilibrium was reached in less than 24 h in all situations (Fig. 8). The results were subjected to kinetic analysis using the pseudo-first-order, pseudo-second-order, Elovich and modified Freundlich models.
Fig. 8 Decoloration kinetics adjusted with the: (a) pseudo first order, (b) pseudo second order, (c) Elovich and (d) modified Freundlich models for RB adsorption onto collagen hydrogels. |
As can be seen in Table 1, no model was satisfactory at the lowest dye concentration (10 μg mL−1). This can be attributed to the fact that nearly 100% of the initial dye content is adsorbed on the collagen network within the very first minutes of the reaction so that a limited number of experimental points are available. At intermediate concentrations (20 and 100 μg mL−1), neither the Elovich nor the modified Freundlich model allows for a suitable fitting of the experimental data (R2 < 0.86). Hence, in these conditions, the sorption process is not mainly based on chemisorption and the dye transport to the collagen surface does not involve intra-particle diffusion. In contrast, both pseudo-first- and pseudo-second-order models provide reasonable fitting of the data. At the highest tested concentration (200 μg mL−1), the pseudo-second-order model is the most accurate. Importantly, the Elovich model also provides a suitable fitting of the experimental data. This can be explained considering that the covalent binding of the dye on the collagen surface becomes more significant. Therefore, the kinetic barrier corresponding to the Michael addition reaction at the fiber surface has to be taken into account and the contribution of chemisorption to the overall adsorption process should be considered. One important outcome of these data is that the balance between physisorption and chemisorption mechanisms depends on the dye concentration.
Cc RB (μg mL−1) | Pseudo 1° order | Pseudo 2° order | Elovich | Modified Freundlich | ||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|
qe (μg mg−1) ± SD | k1 (mg μg−1 h−1) ± SD | R2 | qe (μg mg−1) ± SD | k2 (mg μg−1 h−1) ± SD | R2 | β (g μmol−1) ± SD | α (μmol g−1 h−1) ± SD | R2 | kF (L g−1 h−1) ± SD | M ± SD | R2 | |
200 | 150.6 ± 4.3 | 0.3206 ± 0.03 | 0.9287 | 167.1 ± 3.17 | 0.02789 ± 3 × 10−3 | 0.9998 | 0.03658 ± 2 × 10−3 | 317.0 ± 59.91 | 0.9771 | 314.4 ± 11.83 | 4.797 ± 0.32 | 0.9579 |
100 | 88.34 ± 2.4 | 0.4082 ± 0.04 | 0.9401 | 97.16 ± 3.4 | 0.006177 ± 1 × 10−3 | 0.9295 | 0.06991 ± 0.01 | 341.4 ± 22.29 | 0.8582 | 206.7 ± 16.80 | 5.834 ± 1.05 | 0.8234 |
20 | 15.92 ± 0.17 | 0.4998 ± 0.02 | 0.9867 | 17.34 ± 0.42 | 0.04622 ± 7 × 10−3 | 0.9295 | 0.4690 ± 0.08 | 205.3 ± 18.93 | 0.8586 | 42.50 ± 2.84 | 7.512 ± 1.50 | 0.8302 |
10 | 10.51 ± 0.46 | 0.6623 ± 0.15 | 0.7714 | 11.52 ± 0.68 | 0.08676 ± 0.03 | 0.7609 | 0.7380 ± 0.20 | 224.9 ± 36.8 | 0.7195 | 29.43 ± 2.76 | 7.689 ± 2.2 | 0.7071 |
This could be further clarified by obtaining adsorption isotherms at different pHs, that confirmed that the maximum adsorption capacity of the collagen hydrogels is larger at pH 9.00 than at pH 5.00 and 7.00 at all concentrations (Fig. 9). These isotherms were analyzed using the Langmuir, Freundlich, Dubinin–Radushkevich and Temkin adsorption models.
Fig. 9 Adsorption isotherms of RB onto collagen at different pHs. The fitting curves were obtained using (a) Langmuir, (b) Freundlich, (c) Dubinin–Radushkevich and (d) Temkin equations. |
The differences in the fitting parameters found between the Langmuir and Freundlich models were small (Table 2). The Langmuir model is based on the assumption that adsorption exists up to the formation of a homogeneous monolayer of the adsorbate interacting with the sorbent. Thus, a tendency to saturate the interaction sites of the hybrid matrices could be deduced from these results. The Freundlich model presents a better adjustment to materials with heterogeneous adsorption sites. Here, the good fitting to this model further confirms the presence of multiple interactions between the dye and the collagen hydrogel. In addition, the value of n significantly drifts closer to 0 with increasing pH, indicating the increased heterogeneity in terms of interactions of the dye molecule with the collagen surface.49 Interestingly, the Freundlich model appears to fail at reproducing sorption values at high initial dye concentration at pH 9.00. Coming back to the kinetics studies, it can be suggested that an excess of dyes can lead to the saturation of binding sites by physisorption or electrostatic interactions, which decreases the number of sites available for covalent binding.
Model | Parameter | Collagen hydrogel pH 9.00 | Collagen hydrogel pH 7.00 | Collagen hydrogel pH 5.00 | |||
---|---|---|---|---|---|---|---|
Value | R2 | Value | R2 | Value | R2 | ||
Langmuir | qm (μmol g−1) ± SD | 1052.0 ± 43.1 | 0.9300 | 383.8 ± 50.0 | 0.9650 | 709.2 ± 292.2 | 0.9359 |
Ka (L mmol−1) ± SD | 11.24 ± 1.86 | 111.40 ± 26.04 | 243.60 ± 142.90 | ||||
ΔG0 (kJ mol−1) | −5.990 | −11.700 | −13.600 | ||||
Freundlich | K ± SD | 2015.0 ± 158.0 | 0.9317 | 843.8 ± 121.9 | 0.9454 | 1314.0 ± 292.6 | 0.9297 |
N ± SD | 0.3088 ± 0.0251 | 0.6742 ± 0.0586 | 0.8119 ± 0.0954 | ||||
Dubinin–Radushkevich | qDR (μmol g−1) ± SD | 888.2 ± 41.8 | 0.7680 | 202.9 ± 9.7 | 0.9150 | 257.5 ± 14.3 | 0.9197 |
kDR (mol2 kJ−2) ± SD | 8.70 ± 1.96 | 162.70 ± 30.40 | 255.90 ± 48.93 | ||||
EDR (kJ mol−1) | 42.15 | 20.14 | 22.69 | ||||
Temkin | K (mL mg−1) ± SD | 177.20 ± 12.36 | 0.9194 | 65.21 ± 4.38 | 0.9287 | 75.68 ± 8.43 | 0.8433 |
B (J mol−1) ± SD | 2.1160 ± 0.5994 | 0.1517 ± 0.0213 | 0.1447 ± 0.0330 |
The Dubinin–Radushkevich model shows a similar failure in reproducing sorption data for high concentration of dyes at pH 9.00 whereas it allows for a reasonable fitting of the sorption values in more acidic conditions (Table 2). The constant related to the adsorption energy (kDR) increases when the pH decreases in agreement with the adsorption phenomena that take place at lower pH and the predominant covalent interaction that occurs at pH 9.00. On the contrary, the Temkin model is more suitable for basic conditions where the parameter related to the heat of sorption (B) is also higher.
The standard free energy (ΔG0) of the adsorption process can be obtained using the following equation:
ΔG0 = −RTlnKa | (15) |
The mean free energy value of adsorption EDR (kJ mol−1) can be calculated using the Dubinin–Radushkevich equation:
EDR = (2kDR)−1/2 | (16) |
In the adsorption processes, where chemical interactions of weak intensity (such as electrostatic interactions) are dominant, the value of the EDR parameter is between 8 and 16 kJ mol−1. Lower values are related to physisorption processes and values higher than 16 kJ mol−1 are related to coordination or covalent bonds formation.21,31 Herein, EDR values obtained at pHs 5.00 and 7.00 are around 20 kJ mol−1 suggesting significant interaction between the dye and collagen. At pH 9.00 the EDR value was 42 kJ mol−1, supporting the hypothesis of stronger covalent bond formation.
These data suggest that type I collagen hydrogels exhibit several advantages for reactive azo-dye remediation from water. Sorption capacity of collagen hydrogel at pH 9.00 was ca. 1 mmol g−1 (i.e. 1 g g−1). Even in acidic conditions that are closer to natural waters, the capacity was >0.5 g g−1, larger than reported values for activated carbon.50,51 The adsorption process is fast, the adsorbent (collagen) is biodegradable, and azo dyes don't suffer rupture that could origin products even more toxic than the dye without degradation. The interaction between collagen and dye is chemically-stable limiting the risk of secondary contamination due to dye leaching from the sorbent. Another advantage of such hydrogels is their ability to reduce the generation of waste due to their strong reduction in weight and volume upon drying that should reduce the needed storage area leading also to reduction costs. Their application in water remediation would also constitute a new valorization route for industrial processes producing collagen as waste. In parallel cross-linked collagen hydrogels are currently widely used for biomedical applications but they face an important issue related to the cytotoxicity of the cross-linking agent. Relevant biological data for RB are still scarce but suggest that it exhibits a lower toxicity than glutaraldehyde,52 calling for a deeper investigation of the in vitro and in vivo properties of these dye–collagen hydrogels.
Footnote |
† In memoriam Prof. Dr Luis E. Diaz. |
This journal is © The Royal Society of Chemistry 2015 |