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 OJAppS  Vol.11 No.12 , December 2021
Kinetic and Thermodynamic Study of the Dephosphation of Wastewater by Clay Materials from Côte d’Ivoire
Abstract: Phosphorus is introduced into the aquatic environment from different point sources, mainly by domestic and industrial wastewater; contributing to the eutrophication of water bodies. The most common way for wastewater dephosphation is the injection of expensive chemicals into these bodies of water. Thus, the main objective of this work was to find an alternative to chemicals by using clay materials from Côte d’Ivoire to adsorb phosphate ions from aqueous solutions. The clay samples, taken from various regions were characterized by X-ray diffraction. They have a different mineralogical composition. The influence of various parameters such as the pH of the medium, contact time, the ion force, temperature, etc. on the adsorption was studied. Adsorption is influenced by the temperature, the pH of the medium, valence of the saturated cation and the clay composition. It is described by a kinetic model of the pseudo-second order. The salt of the medium has no significant effect on the process. The thermodynamic study revealed that adsorption is spontaneous, endothermic and that it is done by electrostatic means of physical nature.

1. Introduction

Water is a vital resource that man uses for his needs. Its good quality allows us to eat, practice sports, fishing, tourism in order to have a good physical, moral, financial health, etc., but the various anthropic activities exercised by man on the natural environment considerably degrade the quality of the environment and water resources. Indeed, the demographic growth of urban cities, the establishment of industrial areas near waterways, the use of chemical fertilizers, the development of livestock have considerably increased the production of wastewater that is often enriched in organic matter and nutrients (phosphorus and nitrogen, in particular) necessary for plant growth. These waters, when discharged into nature without adequate treatment, cause an imbalance in aquatic ecosystems and eutrophication of lakes, rivers, streams and watercourses with low hydrodynamics [1] [2] [3] [4].

In fact, eutrophication is characterized by the anarchic appearance of aquatic plants (algae, macrophytes...) [5] and plankton when a bodie of water contains a high concentration of phosphate and nitrogen. These invasive aquatic plants considerably reduce the quantity of drinking water, prevent the practice of sports, tourism activities, fishing (industrial or artisanal), the production of drinking water [3] [5] [6], which has very significant repercussions on the human and socio-economic health of a municipality or a region. Today, eutrophication is a major environmental problem.

To solve this problem of eutrophication, manual and mechanical removal, the application of herbicides, biological attack and the use of financial and material resources are commonly used, but it turns out that these processes are not very effective and that aquatic plants reappear immediately. In addition, several studies have proposed preventive and curative methods to fight against eutrophication [2] [7] [8]. These studies point out that phosphorus is the limiting factor [1] [9] [10] [11] on which action must be taken to reduce the proliferation of aquatic plants, and consequently the limitation of the eutrophication phenomenon. The dephosphatation of wastewater is undoubtedly a means of controlling eutrophication. It can be done by physicochemical processes based on precipitation reactions with iron, aluminum or calcium based reagents, biological processes with bacteria and adsorption which has many advantages, and can be done with several types of materials including biomaterials.

In a policy of environmental protection, biomaterials, natural, abundant, inexpensive and with great capacities of phosphate adsorption, are increasingly used [12] [13] [14]. It is appropriate to complement these studies by valorizing other biomaterials as phosphate adsorbents. It is within this framework that our study is included, with the ambition to participate in an environmental protection policy to use clay materials from Côte d’Ivoire for wastewater dephosphation.

To achieve this goal, after having collected clay samples in various regions of Ivory Coast, we will determine their mineralogical characteristics, then study the influence of various parameters such as the contact time, the pH of the medium, the temperature, the ionic strength and the quantity of clay on the adsorption, finally to identify the mechanisms of adsorption brought into play and to make a comparative study of the effectiveness of the adsorbents.

2. Materials and Methods

2.1. Clay Samples

The study is carried out on three different clays of the soils of Ivory Coast. These are a sample from Korhogo noted KOR, a sample from Katiola noted KAT and a sample from Anyama noted ANY. These samples were previously characterized by X-ray diffraction using a BRUKER D8 ADVANCE apparatus operating at the wavelength λ = 1.7903 Å of cobalt.

The clay samples taken from the soil, are dried in the shade for several days, then they are crushed in an agate mortar. The resulting powder is sieved to 100 μm. Then, these well-crushed and sieved samples, underwent sedimentation to collect the clay fraction with diameter < 2 µm. Then, the collected clay fractions, were treated with saturating cations (Mg2+ and/or Na+). This treatment resulted in 6 clay solutions at 10 g∙l−1, designated ANY-Na; ANY-Mg; KAT-Na; KAT-Mg; KOR-Na and KOR-Mg that served as adsorbents.

2.2. Adsorption Procedure

The solution used as the phosphate source was obtained by dissolving potassium hydrogen phosphate KH2PO4 in distilled water.

The adsorption experiments were performed in Batch system, checking the influence of parameters such as clay mass, pH of the medium, contact time, ionic strength, temperature and initial phosphate concentration on the adsorption phenomenon. The tests were performed by mixing a certain volume of 10 g∙l−1 clay solution with a volume of phosphate solution containing salt (NaCℓ or MgCl2), so as to have a mixture of volume 10 mL and 5 mg∙l−1 of phosphate. The resulting mixtures were then kept under stirring at 480 rpm using a VIBRAMAX 100 type mechanical stirrer for 120 minutes (previously determined reaction time) at the temperature of 303 K, then the supernatants taken after centrifugation at 5000 rpm for a period of 30 minutes using a centrifuge type UNIVERSAL 320R, were analyzed with a UV-Visible spectrophotometer at the wavelength 880 nm using an apparatus type SHIMADZU UV 1700. To each supernatant was added 1 mL of a mixture consisting of ammonium molybdate, potassium antimony double tartrate, concentrated sulfuric acid, ascorbic acid and water, 15 minutes before the spectrophotometer analysis. The residual phosphate concentration was determined using a calibration curve made from a range of known phosphate concentrations.

The tests relating to the influence of the contact time, were carried out by varying the contact time from 0 to 5 hours. For the influence of the mass, the efficiency of phosphate removal was studied by varying the clay mass from 5 to 50 mg. To check the influence of pH, the tests were performed by varying the pH from 2 to 10 with a decimolar solution of HCl or NaOH. For the temperature, the values 293 K (20˚C), 303 K (30˚C), 313 K (40˚C) and 323 K (50˚C) were chosen. To better understand the influence of Na+ and/or Mg2+ ions on the adsorption process, the tests were performed by varying (from 0 to 0.1 mol∙l−1) the salt concentration (NaCl or MgCl2) of the clay-phosphate solution mixtures.

3. Results

3.1. Characterization of the Clay Samples

3.1.1. Mineralogical Analysis

The X-ray diffraction spectra obtained are presented in Figures 1-4:

· The diffractograms in Figure 1 and Figure 2 reveal that the ANY sample contains chlorite (lines at 14.09 Å; 7.06 Å; 4.71 Å; 3.53 Å; and 2.82 Å), illite (lines at 9.94 Å; 4.98 Å; and 1.99 Å), and smectites (lines at 14.83 Å (Figure 2(a)) and lines at 17.04 Å and 8.49 Å (Figure 2(b))). Associated with these minerals are quartz (lines at 4.25 Å; 3.34 Å; 2.28 Å; 2.13 Å and 1.82 Å) and rutile (lines at 3.2 Å and 2.46 Å).

Figure 1. X-ray diffractogram of the total rock of the ANY sample.

Figure 2. X-ray diffractograms of the fine fraction of the ANY sample. (a) Normal slide; (b) sample treated with ethylene glycol; (c) sample treated at 773 K.

· The diffractograms in Figure 3 and Figure 4 show that the KAT and KOR samples consist of kaolinite (lines at 7.15 - 7.17 Å; 4.46 Å and 3.57 Å), illite (lines at 9.94 Å; 4.98 Å and 1.99 Å), quartz (lines at 4.25 Å; 3.34 Å; 2.28 Å; 2.13 Å and 1.82 Å) and rutile (line at 3.24 Å and 2.46 Å). In addition to these minerals, sample KAT also contains smectites (lines at 14.17 Å and 4.03 Å) and sample KOR, goethite (lines at 4.15 Å and 2.56 Å).

3.1.2. Mineralogical Composition

The theoretical results of the mineralogical composition of the clay samples are given in Table 1.

The results show that sample ANY is richer in quartz (25.69%), illite (21.44%) and chlorite (23.54%) than the other two samples, however it contains the lowest content of smectite (12.50%). The highest smectite content (20.90%) is contained in sample KAT. As for sample KOR, it is relatively rich in goethite (9.14%), kaolinite (49.71%) and rutile (1.52%), however it is less rich in illite (2.80%). The presence of goethite could make the KOR sample particularly adsorbent.

Figure 3. X-ray diffractogram of the total rock of the KAT sample.

Figure 4. X-ray diffractogram of the sample KOR. C: chlorite; G: goethite; I: illite; K: kaolinite; Q: quartz; R: rutile; S: smectite.

3.2. Effect of Contact Time

The results obtained during the tests related to kinetics, are presented in Figure 5(a) and Figure 5(b).

Figure 5(a) and Figure 5(b) show that the amount of phosphates adsorbed increases with increasing contact time following two different slopes. The first slope, which is strong, is located in the first 60 minutes of contact and would correspond to a fast adsorption rate. The second slope is gentle and a saturation level is observed. This phase could reflect a slow adsorption rate and express the equilibrium between the adsorption and desorption of phosphates. The major part of the phosphates fixed on the adsorbent, is obtained in the first hour with efficiency in the order of 76%, 66%, 65% and 64% respectively for the samples KOR-Mg, KOR-Na, ANY-Na and ANY-Mg. For the KAT-Mg and KAT-Na

Table 1. Proportion of mineral phases in the clay samples.

Figure 5. Effect of contact time on the amount of phosphate adsorbed (C0 = 5 mg∙l−1; clay mass = 40 mg; Stirring = 480 rpm; V = 10 ml; pH = 6.6; T = 303 K). (a) Sodium samples; (b) Magnesium samples.

samples, the efficiency were 41% and 33.5% respectively.

3.3. Effect of Clay Mass

Figure 6(a) and Figure 6(b) show the adsorption efficiency as a function of clay mass.

The results show that the phosphate removal efficiency increases with increasing clay mass. For all the samples except KOR-Mg, a maximum removal of 86.37% to 97.91% was obtained for a mass of 40 mg of clay. For KOR-Mg, it is 20 mg. Above 40 mg, the removal efficiency is almost constant. This could indicate a saturation of the medium.

3.4. Effect of pH on Phosphate Removal

The results obtained during the tests relating to the influence of the pH of the medium on the adsorption of phosphates, are presented on Figure 7(a) and Figure 7(b).

Figure 6. Adsorption efficiency as a function of clay mass (C0 = 5 mg∙l−1; pH = 6.6; Stirring = 480 rpm; V = 10 ml; Contact time = 2 h; T = 303 K). (a) Sodium samples; (b) Magnesium samples.

The results show that the quantity of phosphate adsorbed by the samples increases between pH = 2 and pH = 6 then a strong decrease is observed when the pH is higher than 8. This decrease is probably due to the charged surface of the clay losing the electrostatic attraction on the phosphates. Moreover, the evolution profile of the quantity of phosphates adsorbed from the samples ANY-Na, ANY-Mg, KAT-Mg and KOR-Mg, shows a plateau between pH 4 and pH 8. For samples KAT-Na and KOR-Na, the evolution profile shows a peak around pH 6. Overall, the adsorption capacity reaches a maximum value between pH 4 and 8.

3.5. Effect of Ion Force on Adsorption

The study of the effect of the salinity of the medium on the adsorption, is represented on Figure 8(a) and Figure 8(b).

Figure 7. Effect of medium pH on the amount of phosphate adsorbed (C0 = 5 mg∙l−1; clay mass = 40 mg; Stirring = 480 rpm; V = 10 ml; Contact time = 2 h; T = 303 K). (a) Sodium samples; (b) Magnesium samples.

Figure 8. Effect of ion force on the adsorption efficiency (C0 = 5 mg∙l−1; clay mass = 40 mg; stirring = 480 rpm; V = 10 ml; pH = 6.6; T = 303 K). (a) Sodium samples; (b) Magnesium samples.

The different curves obtained (Figure 8(a) and Figure 8(b)) show two phases. In the first phase, between 0 and 10−2 mol∙l−1, the retention rate of phosphates increases rapidly to reach a maximum value at 10−2 mol∙l−1. In the second phase (salt content > 10−2 mol∙l−1), a plateau is observed for samples ANY-Na, ANY- Mg, KAT-Mg, KOR-Na and KOR-Mg. In contrast, the profile of the sodium KAT sample shows a gentle slope, so that salt addition causes a small change in phosphate removal rate of about 10%. This suggests that ion force has virtually no influence on the process.

3.6. Effect of Temperature

The tests relating to the influence of the temperature on the adsorption of phosphates by the clay, gave the results represented on Figure 9(a) and Figure 9(b).

These results reveal that increasing the temperature increases the adsorption capacity of the clay. This suggests that the adsorption reaction is endothermic.

Figure 9. Effect of temperature on the amount of phosphate adsorbed (C0 = 5 mg∙l−1; clay mass = 40 mg; Stirring = 480 rpm; V = 10 ml; pH = 6.6). (a) Sodium samples; (b) Magnesium samples.

Above 313 K, the adsorption capacity decreases slightly for the samples ANY-Na, ANY-Mg, KAT-Mg and KOR-Mg. This decrease is due to the desorption phenomenon that occurs.

3.7. Kinetic Models of Adsorption

The kinetic study of adsorption allows us to examine the influence of contact time on retention. For this purpose, the pseudo first order (Equation (1)) and pseudo second order (Equation (2)) kinetic models were applied to describe the mechanism of phosphate adsorption kinetics by clay samples. Their linear expressions are [15] [16]:

log ( q e q t ) = log ( q e ) k 1 2.303 t (1)

t q t = 1 k 2 q e 2 + t q e (2)

The parameters of the two kinetic models are grouped in Table 2.

According to the parameters reported in Table 2, in the case of the pseudo-first order kinetic model, the experimentally determined amount of phosphates adsorbed at equilibrium is different from the theoretical value. On the other hand, for the pseudo-second order kinetic model, the amount of phosphates adsorbed at equilibrium, determined experimentally is approximately equal to the theoretical value. Moreover, the correlation coefficients R2, are very close to unity for the second order. These last two observations, suggest that the pseudo-second order kinetic model gives a better correlation with the experimental results. On the other hand, magnesium-saturated samples adsorb phosphates more than sodium-saturated samples. The KOR sample has a greater adsorption capacity than the ANY sample which is greater than the KAT sample.

3.8. Thermodynamic Study of the Adsorption

The thermodynamic parameters are determined from the following equations [17] [18]:

ln K d = Δ H R T + Δ S R (3)

Δ G = Δ H T Δ S (4)

The values of the thermodynamic parameters of the different clay supports used are grouped in Table 3.

Table 2. Kinetic parameters relating to the adsorption of phosphates.

Table 3. Values of the thermodynamic parameters.

The free enthalpy values ∆H are positive and less than 40 kJ∙mol−1. This confirms the endothermic nature of the adsorption reaction. The ∆G values are negative and decrease with increasing temperature. In addition, the ∆G values are greater than - 20 kJ∙mol−1. These observations show that the adsorption reaction is spontaneous and this spontaneity increases with temperature. For all samples, the positive values of the entropy ∆S, suggest an increase in disorder at the solid-liquid interface during adsorption.

4. Discussion

The knowledge of the operating conditions at the dephosphation by clays, led us to study the influence of contact time, clay mass, pH of the medium, ionic strength and temperature on the adsorption. Thus, the phase of rapid increase of the adsorption capacity being situated in the first 60 minutes of contact, shows that the speed of adsorption is fast. This could be explained by the fact that the electrostatic attraction of the adsorbent surface on the phosphates is accompanied by a great mobility of the ions in solution, which would increase the kinetic energy of these particles, as well as the frequency of collision between them and the surface of the clay. The clay samples used therefore have a high reactivity towards phosphorus. After this phase, the speed becomes slower and slower since the binding forces involved are weak, some adsorbates could detach from the surface (desorption phenomenon) and go into solution. This could lead to an equilibrium between adsorbed and desorbed fractions [15]. The adsorption process does follow the pseudo-second order kinetic model. These results corroborate several studies that have shown that phosphate adsorption kinetics obey the pseudo-second order [12] [13] [14] [19] [20].

Regarding the increase in adsorption efficiency with clay mass, it would be due to the increase in adsorbent surface area and the number of active sites offered on the adsorbent surface [21]. Above 40 mg, the removal efficiency is almost constant. This is probably related to the formation of a deposit by aggregate formation in the reactor. Indeed, the increasing contribution in adsorbent leads progressively to the formation of a compact mass of clay. This mass would cause a covering of the contact surfaces, which would make less available the acceptor sites on the surface of the adsorbent and would lead to a saturation of the aqueous medium. Work related to the contact of phosphates with various materials has yielded similar results [12] [22] [23] [24] [25].

In an acidic environment, the adsorption of hydronium ions H3O+ creates additional positive charges on the clay surface, which could increase the electrostatic attraction of phosphate anions. The distribution curve in Figure 10 shows that the phosphate anions are progressively put into solution from pH 2. Thus, the phosphates bind to the charged surface of the clay as they are produced, resulting in an increase in the retention efficiency of the phosphates. A similar result was obtained by [12] [24] [26]. As for the reduction of the performance of retention of phosphorus when the pH is basic, would be related to several factors.

Figure 10. Distribution curves of species from orthophosphoric acid H3PO4 [31].

It seems that hydroxide ions OH compete with phosphate ions to occupy the adsorption sites on the one hand, and on the other hand, to the charged surface of the clay which loses the electrostatic attraction on the phosphate anions HPO 4 2 and PO 4 3 arriving at the adsorbent surface [21]. In a basic environment, negative charges on the clay surface outnumber positive charges. Therefore, the pH of the medium has an effect on phosphate adsorption. However, the rate of phosphate adsorption is better around a neutral pH. This result corroborates those of [27] [28] [29] [30]. According to [27], the natural environment of pH varying between 5.5 and 7.5 is favorable for phosphate removal.

The study of the effect of temperature on adsorption showed that the reaction is endothermic in nature. This result is in agreement with those of [27] [32] [33]. Above 313 K, a decrease of the adsorption capacity was observed for some samples. This decrease could be due to the desorption of some phosphates. A similar result was obtained by [23] [24] during nitrate and phosphate removal by a modified bentonite. In Effect, a decrease in adsorption capacity was observed at temperatures above 303 K by [23] and 311K by [24] respectively. The magnitude of the free energy ∆G is used to determine the type of adsorption process [13]. Thus, ∆G values greater than −20 kJ∙mol−1, as in our case, would correspond to an electrostatic interaction between the adsorption sites and the phosphate ions. This result explains well the observations of the influence of pH on adsorption. The values of ∆H, which are lower than 40 kJ∙mol−1, suggest that the adsorption is due to physisorption or physical adsorption and involves only relatively weak intermolecular forces such as Van Der Waals forces. However, this type of mechanism is characterized by its rapidity and reversibility by allowing an accumulation of layers (multilayer formation). Hence the rapid adsorption kinetics during the first hour of contact and the desorption observed beyond 313 K. Moreover, the increase in temperature could make the bonds involved in the process even weaker, which could lead to the detachment of the adsorbate from the surface and pass into solution.

The phase of increase of the dephosphation rates when the salt concentration is lower than 10−2 mol∙l−1, shows that the presence of alkaline elements in solution, increases the performance of the adsorbents used. Indeed, the fixation of these alkalis on the surface of the clay could increase the quantity of positive charges and increase the electrostatic attraction of the adsorbent surface on the phosphate anions. Alkalis not retained by the clay, could form screens that would prevent some phosphates from accessing the adsorbent surface so that further adsorption of phosphates would be less easy. This could explain the nearly constant rates when the salt concentration is greater than 10−2 mol/L. However, the presence of Ca2+, Mg2+, etc. does not interfere with the adsorption process [34]. The performance of magnesian samples must be due to the binding intensity of cations mediating the binding of phosphate ions. This intensity depends on the valence and the degree of hydration of the cation [35]. In fact, weakly hydrated bivalent ions such as Mg2+, i.e. surrounded by a weak layer of water, are more energetically retained than strongly hydrated monovalent ions such as Na+ [35]. Thus during saturation of clay samples, the amount of magnesium bound would be large compared to that of sodium. Therefore, magnesium bridges would be more numerous than sodium bridges. Moreover, according to Figure 10, the monovalent phosphoric ion H 2 PO 4 would be the predominant species in the pH range of our tests (pH between 6 and 7). Thus during the adsorption process, two H 2 PO 4 ions could be retained via a Mg2+ ion, while via a Na+ ion, only one H 2 PO 4 ion could bind. As a result, magnesian samples could remove more phosphates than sodium samples.

The Korhogo clay had the highest phosphate retention efficiency, followed by the Anyama clay and then the Katiola clay, suggesting that phosphate removal depends on the clay. Indeed, the Korhogo sample, which is mostly kaolinite (49.7%), contains a significant amount of goethite (9.14%). This iron oxide strongly increases the specific surface and improves the adsorption capacity [36], since Fe3+ ions have a high affinity for phosphorus. Hence a high adsorption capacity for the KOR sample compared to the others without goethite. Concerning the ANY sample, it contains appreciable quantities of 2:1 minerals such as smectites (12.5%), illite (21.44%) and chlorite (23.54%), that is to say a total of 57.48% of 2:1 minerals compared to 35.9% for the KAT sample (20.9% smectite and 15% illite) which also contains 22.5% kaolinite (type 1:1 clay). The ANY sample, which contains more 2:1 minerals, adsorbs phosphates better than the KAT sample. This finding suggests that the mineralogical composition of the clay samples may give an explanation for the different adsorption capacities [37] and then that 2:1 type minerals have greater adsorption capacities compared to 1:1 type minerals [38].

5. Conclusions

This study investigated the capacity of the clays to adsorb phosphate ions from aqueous solutions in order to valorize clay materials from Côte d’Ivoire. These clay samples, collected in various regions of Côte d’Ivoire, were characterized by X-ray diffraction. This characterization revealed that the ANY sample contains chlorite, smectites, illite, quartz and rutile; the KAT sample consists of kaolinite, smectites, illite, quartz and rutile. KOR Sample contains kaolinite, illite, quartz, rutile and goethite. The study of the factors likely to influence the adsorption, were carried out. The results of the kinetic showed that the adsorption process follows the model of pseudo-second order. The values of the thermodynamic parameters indicate that the reaction is a spontaneous, endothermic physisorption (or physical adsorption) and that a disorder occurs at the solid-liquid interface during the reaction. The adsorption of phosphates is influenced by the pH of the medium, the temperature, the valence of the saturating cation and its degree of hydration, the presence of iron oxide and the mineralogical composition of the clay. However, the salinity of the medium does not disturb the process.

In perspective, it would be pertinent:

· to treat the natural effluents with the clay materials. Indeed, the natural water has a much more complex composition than the synthetic solutions which were used for this work. Thus a comparison could be made on the thermo- dynamic and kinetic plan and to check if there is similarity of the results;

· to study the desorption of phosphates retained on the surface of the clay in order to consider a probable use of the sludge produced as fertilizer in agriculture since some samples showed a tendency to desorption.

Cite this paper: Pierre, A. , Brice, K. and Vamoussa, C. (2021) Kinetic and Thermodynamic Study of the Dephosphation of Wastewater by Clay Materials from Côte d’Ivoire. Open Journal of Applied Sciences, 11, 1307-1323. doi: 10.4236/ojapps.2021.1112099.
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