DOI:
10.1039/D4MA00408F
(Paper)
Mater. Adv., 2024,
5, 6234-6247
Synergistic co-adsorptive removal of crystal violet and chromium(VI) from water by pozzolan-charcoal based geopolymer composites
Received
19th April 2024
, Accepted 27th June 2024
First published on 8th July 2024
Abstract
In this study, the geopolymer composites GP0, GP7.5-CP, and GP10-CP were synthesized using mixtures of pozzolan (Pz) and waste charcoal powders (CP) as precursors with CP mass contents of 0, 7.5 and 10%, respectively. The geocomposites obtained were characterized by X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FTIR), Brunauer–Emmett–Teller (BET) surface analysis and scanning electron microscopy analysis (SEM). The sequestration performance for crystal violet (CV) and chromium VI (Cr VI) was evaluated in mono- and bi-component systems. The incorporation of 7.5% CP (GP7.5-CP) resulted in a ∼19% increase in the specific surface area and densification of the functional groups. Incorporation of CP increased the adsorption capacity due to (1) increased surface areas (2) increased active functional group density and distribution, and (3) shielding effect of CP on acidic sites improving CV adsorption. The adsorption capacities in binary systems were 45 and 59% higher than in single solute systems for CV and Cr(VI), respectively. The Rq > 1 and 1/n > 1 implied synergistic and cooperative adsorption, denoting adsorption of Cr(VI) creates new binding sites for CV adsorption. Ultrahigh adsorption density of 2803 and 3659 mg g−1 in single solute systems was achieved for CV and Cr(VI), respectively. The adsorption mechanism is multi-mechanistic involving the reduction of HCrO4− to Cr3+ by the donor groups of geocomposites, ion exchange, electrostatic and hydrogen bonding interactions. Modification of geopolymers with coal ash stupendously ameliorates their adsorption capacity for simultaneous adsorption of dyes and heavy metals in water.
1. Introduction
Geopolymers are a class of eco-materials resulting from a polymerization/polycondensation reaction between amorphous or semi-crystalline aluminosilicate feedstock and alkaline or phosphoric acid solution at ambient temperature or below 100 °C.1 The aluminosilicate sources preferentially used can be natural (volcanic slag, pozzolana, metakaolin, pumice, and laterite), industrial (fly ash, blast furnace slag, and dolochar)2,3 or ashes derived from incineration of solid wastes.4 Surface properties such as specific surface area, cation exchange capacity and functional group identities and distribution make geopolymers excellent low-cost emerging adsorbents for the removal of dyes, toxic metals, personal and pharmaceutical care compounds (PPCCs) and surfactants from wastewater.5 Dyes and heavy metals constitute a prevalent class of water pollutants. Particularly, due to their high toxicity and low biodegradability, crystal violet (CV) and hexavalent chromium (Cr(VI)) are the pollutants most commonly found in wastewater and are considered the most hazardous to human health and the environment. Their presence in the ecosystem can lead to genotoxicity, respiratory problems, kidney failure and permanent blindness.6–8 However, recent studies have reported geopolymer adsorption as one of the most effective remediation methods for eliminating these types of pollutants. For example, Qiu et al.9 synthesized a fly ash-based geopolymer for Cr(VI) removal and recorded an adsorption capacity of 49.751 mg g−1. Grillo et al.10 reported an adsorption efficiency of 70% of Cr(VI) on pumice-based geopolymers. López et al.11 assessed the CV binding capacity of a bentonite-based geopolymer and reported a sequestration density of 4.36 mg g−1. According to Jacques et al.,12 acidic functional groups negatively impacts the adsorption of CV. Aluminosilicates, such as geopolymers, contain acidic sites which may thus diminish their adsorption potential for CV. This could explain the low adsorption capacity of 11.06 and 4.36 mg g−1 for volcanic scoria and bentonite geopolymer materials for CV uptake, respectively.11,13 Functionalization of geopolymers with the addition of adjuvants to the geopolymeric network makes it possible to improve the adsorptive properties for CV by clouding the acidic sites rendering them inaccessible while providing new active sites for adsorption of both CV and Cr(VI). For example, Sarkar et al.14 synthesized bivalent metal ion-modified geopolymers (Ni-LDSGP and Zn-LDSGP) for fluoride removal. The study revealed that the incorporation of these bivalent ions resulted in their addition to the geopolymer chain and an increase in specific surface area from 30.84 to 58.14 and 53.42 m2 g−1 for Ni-LDSGP and Zn-LDSGP, respectively. The modified geopolymers exhibited superior adsorption capacity for fluoride than pristine sample. In contrast, incorporation of metakaolin (MK) into volcanic ash based geopolymers ameliorated the surface areas with no significant change in adsorption capacity for methylene blue dye. However, the rapidity of the adsorption process increased with increase in MK fraction.15 Tome et al.16 showed during the synthesis of laterite (LA)-rice husk ash (RHA) geopolymers that the addition of 5% RHA improved the porosity and densification of the functional groups and that the resulting eco-adsorbent had a Malachite Green adsorption capacity 5 times greater than laterite. Zhang et al.17 prepared geopolymer composites based on metakaolin and chitosan (CS) for crystal violet adsorption. They reported that the addition of 1.0% CS resulted in an increase in surface chemical functions and a high porosity of 50.97% of the CS/PG composite, respectively, resulting in a fixation efficiency of ∼95% in CV during a continuous treatment of 14 h. He et al.18 synthesized Lithium hydroxide modified geopolymer (Li-ABW) composite for effective Cr(VI) removal from water. They showed that the integration of Li into the geopolymeric network resulted in an increase in specific surface area (∼55.75%) and total pore volume (∼91.29%) inducing a sequestration removal efficiency of 85.45% generated by electrostatic interactions. The aforementioned geopolymer pretreatment methods have their inherent limitations. The incorporation of monovalent or divalent metals can lead to secondary water pollution in the event of leaching from the geopolymer structure, and the functionalization of the geopolymer can introduce site-specific interactions that can induce specificity in adsorbate binding. Furthermore, most of adsorption studies involving geopolymers entailed adsorption in single-solute systems, and only a few have investigated the co-adsorption behaviour in binary systems. For example, Fang et al.19 prepared geopolymer microspheres based on three solid wastes, coal gangue, fly ash and blast furnace slag, for the mixed adsorption of methylene blue and Cr(VI). In the bi-component system, Cr(VI) was preferentially adsorbed implying antagonistic effects. Yu et al.20 reported the simultaneous removal of Cu2+ and Cr(VI) on metakaolin-based geopolymer modified with cetyltrimethylammonium bromide (CTAB). The study showed that pretreatment with CTAB produced a geopolymer composite that could sorb anions without loss of the ability to adsorb cations. In the studies, however, the adsorption rates in binary systems were not examined. Besides equilibrium adsorption capacity, adsorption rates provide an important criterion in selection of adsorbents, especially modified geopolymers.15 The effect of co-existence of anionic and cationic adsorbates on reaction rates is not well understood. Furthermore, the rarity of industrial waste precursors in many developing countries, particularly in remote areas, limits their exploration whereas the use of CTAB makes synthesis operations more costly than with carbonaceous additives such as carbonized sugarcane bagasse and tyre ash.21,22 Pozzolan is a plentiful aluminosilicate suitable for geopolymer development.21 Additionally, geopolymers are known to be better adsorbents than their precursors.4,13,15,16,23 While the use of coal powders (CPs) as adjuvants in the synthesis of geopolymers is hypothesized to reduce accessibility of CV to the acidic sites, the resultant antagonistic or protagonist effect in the binary elimination of anionic Cr(VI) is also unknown. Furthermore, while adsorption capacities at equilibrium of adsorbents in binary systems have been evaluated, adsorption kinetics/rates in binary systems are seldom evaluated. To date, there is no work reported on the co-elimination of cationic crystal violet and anionic chromium(VI) in binary systems by geopolymer composites. Evaluating the adsorption capacity and rate and potential limitations of these new materials would improve our understanding of their chemistry and effectiveness in multicomponent systems expected in real wastewater. The solidification of coal powder in geopolymers as new composite adsorbents with ultrahigh adsorption capacities for simultaneous sequestration of heavy metal and dye in water presents the novelty of the present work. The present study evaluated and examined the mechanisms associated with the simultaneous sequestration of the toxic cationic CV dye and a hyper-toxic heavy metal Cr(VI) in artificial waters under various experimental conditions by pozzolan- and charcoal powder-based geopolymers.
2. Materials and methods
2.1. Chemical reagents
Crystal violet (C25H30N3Cl, 99% purity), potassium dichromate (K2Cr2O7, 99.9% purity), methylene blue (99.9% purity), sodium thiosulphate penta hydrate (99. 9% purity), sublimed Iodine (99% purity), sodium silicate (96% purity), sodium chloride (99. 5%), sodium hydroxide (98% purity) and hydrochloric acid (37% purity) were obtained from Sigma-Aldrich. All chemicals were used as is, without further purification.
2.2 Synthesis of geomaterials
The pozzolan (Pz) and charcoal waste (CP) used as aluminosilicate source and an additive, for the synthesis of the geopolymer composites were obtained from a quarry located in the commune of Quanté (latitude 4°; 40′; 39.37′′North and longitude 9°; 40′; 56. 34′′East) and from an industrial site for the production of commercial domestic charcoal in the Littoral-Cameroon region, respectively. The raw materials were ground and sieved to particle sizes below 100 μm, the resulting powders were washed, and oven dried at 105 °C for 72 hours. The alkaline solution was prepared by first mixing the sodium hydroxide solution (12 M) with a commercial sodium silicate solution (28.7 wt% SiO2, 8.9 wt% Na2O and 62.4 wt% H2O; density 1.37 g mL−1) in a volume ratio of 2.4. The geopolymer composites were synthesized by mixing pozzolan powders initially substituted by varying proportions of 0, 7.5 and 10 wt% charcoal powder with 25.8 g alkaline activator solution. The different paste formulations resulting from homogenization after 10 minutes were moulded in cylindrical PVC tubes (10 × 20 mm), left to rest for 30 minutes and dried in an oven at 60 °C to promote the polymerization/polycondensation process for 4 days.16 The geomaterial samples labelled GP0 (pristine), GP7.5-CP and GP10-CP, corresponding to the different proportions of charcoal, were ground, sieved and washed for 2 hours with demineralized water to remove excess alkali. The samples were then dried for 6 hours in an oven at 105 °C then stored in plastic containers for characterization and adsorption tests.
2.3 Material characterization
The mineralogical composition and crystallinity of the precursors and geomaterials was determined using the Bruker D8 Discovery X-ray diffraction apparatus in the 2θ range from 6° to 80° with a step size of 0.02° for a scan rate of 1 s per step and CuKα radiation at 27.5 kV and 25 mA. The functional groups present in the samples were obtained using Fourier transform infrared (FTIR) spectroscopy. The IR spectra were recorded between 4000 and 400 cm−1 with a resolution of 2 cm−1 and 32 scans on an infrared spectrometer (Perkin 156 Elmer, Shelton, CT, USA) using the KBr method. Microporosity and mesoporosity of samples from iodine and methylene blue index tests following the protocol described by Dzoujo et al.21 The isotherms resulting from the adsorption–desorption of N2 at 77 K using a Quantachrome Autosorb AS6AG Station 3 instrument (Quantachrome, Odelzhausen, Germany) were used to calculate the values of the specific surface areas based on the Brunauer–Emmett–Teller (BET) analysis method. The morphology and internal microstructure were visualized by scanning electron microscopy (SEM, Hitachi Ltd, Japan). The PH at which the surface charge of the geomaterials is zero (pHPZC) was determined using the protocol described by Dzoujo et al.24 Here, various 20 mL solutions of NaCl (0.1 M) were initially adjusted to pH (pHi) values between 2 and 10. A mass of 0.1 g of geoadsorbents was then brought into contact with the various initial NaCl solutions and the whole was left at room temperature for 8 hours. After filtration, the final pH (pHf) of each solution was carefully measured using a HANNA pH meter. The pHPZC was obtained from the x-axis intercept of the curve of ΔpH versus pHi.
2.4 Batch adsorption study
Single and binary adsorption tests of crystal violet (CV) and hexavalent chromium (Cr(VI)) by the geoadsorbents were performed in duplicate in a batch reactor at 25 °C. The effect of the contact time in single solute or bi-component system on adsorption was carried out by contacting 0.1 g of each adsorbent with 40 mL of 120 mg L−1 solutions of CV and/or Cr(VI) for time intervals of 10, 20, 30, 60, 90 and 120 minutes. The residual adsorbate concentrations were determined using a UV-visible spectrophotometer at 595 and 540 nm for CV and Cr(VI), respectively. The effect of the initial concentration of the pollutants in single and binary adsorption was also examined by immersing 0.1 g of each adsorbent with 40 mL of CV and/or Cr(VI) solution of different concentrations (10, 30, 60, 90 and 120 mg L−1). The suspensions were kept under stirring until equilibration and then the residual content of each adsorbate was determined. The influence of pH was examined by varying the pH of the CV or/and Cr(VI) solution from 2 to 10 using 0.1 N solutions of HCl and NaOH depending on the desired pH. The variance of the mean residual concentrations was analyzed by one-way ANOVA using SAS software at a confidence level of 95%. The amount adsorbed at any time t(qt), the equilibrium adsorbed amounts (qe) and percent removal (%R) were obtained from eqn (1)–(3) respectively. | | (1) |
| | (2) |
| | (3) |
where Ci (mg L−1), Ct (mg L−1) and Ce (mg L−1) are respectively the initial, time t and equilibrium concentrations of CV or Cr(VI). V (L) and m (g) represent the volume of the CV or Cr(VI) solution and the mass of the geomaterials, respectively.
3. Results and discussion
3.1 Mineralogical analysis
Fig. 1 shows the diffractograms of the CP and Pz precursors and the GP0 and GP7.5-CP geomaterials. The CP coal powders consist mainly of amorphous phases (98.65%) and a few traces of quartz (COD_901-3321). Pozzolan (Pz) consists of minerals such as albite (COD_9009663), andesine (COD_900-1031), augite (COD_900-9665), diopsides (COD_900-5280) and hematite (COD_901-5965) and 52.97% amorphous phases. These minerals, originally present in the pozzolan, are still observed after alkalinisation, indicating the low level of their dissolution in the activating solution during the geopolymerisation process. The activation and incorporation of CP led to an increase in the proportion of amorphous phases from 52.97% to 58.44% and 58.44% to 72.47% for GP0 and GP7.5-CP, respectively. These changes suggest a restructuring of the geopolymer network with concomitant modification of the textural properties.
|
| Fig. 1 PXRD patterns of raw material (CP and Pz) and geomaterial (GP0 and GP7.5-CP). | |
3.2 Functions groups analysis
Fig. 2 highlights the FTIR spectrum of CP charcoal powders, pozzolan and GP0, GP7.5-CP and GP10-CP geopolymer composites. In the CP spectrum, the vibrational bands observed between 3896–3743 cm−1 and around 3436 cm−1 are attributable to the C–H bond elongation of vinyl and the O–H bond elongation of alcohols and carboxylic acids, respectively.25,26 The bands located near 2921 cm−1 and centered at 1739 and 1645 cm−1 are attributed to C–H bond stretching in aliphatic hydrocarbons and carbonyl stretching, respectively.27 The peaks located between 1122 and 1037 cm−1 are attributable to the C–O stretching vibrations of the carboxylic groups and these derivatives.28 Those observed at 871, 799, 743, 588 and 422 cm−1 reflect the presence of aromatic units within CP structure. In addition, the incorporation of CP during the preparation of GP7.5-CP and GP10-CP geopolymer composites is responsible for the appearance of new bending vibration bands of C–H of vinyl groups and O–C–O of carbonates observed at 3745–3776 cm−1 and 1424–1440 cm−1, respectively, compared with the pristine GP0 geopolymer. However, a structural reorganization during geopolymerization and the integration of CP into the network is also observed due to the shift in the vibrational bands of the aluminosilicates from 1025 to 1005 cm−1.29,30 These notable changes corroborate the results of the XRD analysis and could significantly improve the affinity for Cr(VI) and textural properties of the resulting composites.
|
| Fig. 2 FTIR spectrum of coal powders, pozzolan and geopolymer composites. | |
3.3 Textural analysis
Table 1 shows the results relating to the specific surface areas and iodine and methylene blue indices used to assess the porosity of geomaterials. Geopolymerization and the incorporation of 7.5% CP favored the formation of a microporous rather than mesoporous geopolymeric structure. Above 7.5% CP, the excess dose reduces this microporosity. Furthermore, the increase and reduction in specific surface area of ∼19% and ∼22% respectively for GP7.5-CP and GP10-CP compared with GP0 corroborate the microporosity of these geocomposites. Although the specific surface areas of these geopolymer composites are lower than those of the functionalized polymers (63.17 m2 g−1 for PAN/ZnO-PNC and 65.40 m2 g−1 for iron oxide-PANI-PNC respectively) reported in the work by Deb et al.,31 Deb et al.,32 the density of the functional group provided by the CPs will be able to compensate for this deficit during the adsorption process.
Table 1 Specific surface area, microporosity and mesoporosity indices values
Adsorbents |
Iodine index (mg g−1) |
Methylene blue index (mg g−1) |
Specific surface area (m2 g−1) |
CP |
659.88 |
14.28 |
133.86 |
GP0 |
794.50 |
15.63 |
13.35 |
GP7.5-CP |
805.47 |
15.93 |
15.89 |
GP10-CP |
748.71 |
15.65 |
10.40 |
Fig. 3 shows the micrographs of CP (a) charcoal powders and GP0 (b), GP7.5-CP (c) and GP10-CP (d) geoadsorbents. It can be seen that CP has a heterogeneous and very porous microstructure (Fig. 3a), unlike the GP0 microstructure (Fig. 3b), which is dense and heterogeneous as a result of the polymerization/polycondensation process and the low dissolution of aluminosilicate phases in the alkaline solution.33 The microstructures of GP7.5-CP and GP10-CP (Fig. 3c and d) show that the addition of CP to the geopolymeric network leads to an increase in porosity, which evolves with the specific surface area. These structural changes are consistent with the results of the XRD and FTIR analyses. However, the increase in specific surface area and functional groups is one of the advantages that could favor the simultaneous sequestration of CV and Cr(VI).
|
| Fig. 3 Micrographs of CP (a) and geoadsorbents GP0 (b), GP7.5-CP (c) and GP10-CP (d). | |
3.4. Effect of pH in single and binary systems
Fig. 4 and 5 show the pHPZC of the different geopolymers and the evolution of adsorption capacities linked to pH variation in single and bi-component adsorption of CV and Cr(VI). The pH at the zero charge point of the geoadsorbents is between 8 and 9 due to the activating agent used during synthesis. The slight decrease in the pHPZC values of the geopolymer composites compared with the pristine geopolymer denote changes in distribution of the acidic Lewis and Brønsted sites with the incorporation of CP.12 Furthermore, at pH < pHPZC, single solute retention of CV is unfavorable (Fig. 5a) due to repulsive interactions between the positive surface charges of the geoadsorbents and CV. This is also attributed to increase in Lewis acidic sites at pH < pHPZC which is detrimental for CV uptake.12 At very pH (>8), the excess Na+ ions compete for the same binding sites with CV, reducing the number of available adsorption sites with concomitant repulsion between the adsorbed CV molecules and those in bulk solution. In contrast, monocomponent adsorption of Cr(VI) is favored since at 2 < pH < 6 (Fig. 5b), since hexavalent chromium exists as an anionic hydrogen chromate (HCrO4−) favoring attractive interactions with the positive surface charge of the geomaterials with maximum adsorption at pH 6. However, at low pH, it is conceivable that the high concentration of H+ affect the second hydration shells surrounding the Cr(VI) ions hindering effective adsorbent–adsorbate interactions. Additionally, competition between the chloride ions from HCl and the anionic Cr(VI) ions also account for the decreased adsorption at low pH. At pH > pHPZC, the geomaterials carry a negative surface charge that favors the retention of CV and hinders the fixation of Cr(VI), which is in the form of CrO42− at pH > 6. A similar phenomenon was observed during the bicomponent sequestration of CV and Cr(VI) on the surface of the geoadsorbents (Fig. 5c), with the exception of the strong competition between the adsorbates, which favored an increase in the quantities adsorbed and was later confirmed by the adsorption isotherms. The studies show that the adsorption of Cr(VI) provides new energetically favorable sites for adsorption of additional CV molecules. These results do not corroborate the work of Fang et al.19 which reported that the adsorption capacity of MGP geopolymer microspheres for MB and Cr(VI) in the binary system decreased when the pH increased compared to a single solute system.
|
| Fig. 4 Point of zero charge of geomaterials. | |
|
| Fig. 5 Influence of pH in single (a), (b) and binary (c) retention of CV and Cr(VI) on geomaterials. Experimental conditions (mGP = 0.1 g, V = 40 mL, T = 25 ± 1 °C, Ci = 120 mg L−1 and t = 60 min). | |
3.5. Effect of contact time in single and binary systems
Fig. 6 shows the evolution of the quantities of CV and Cr(VI) adsorbed over time. In a monocomponent system (Fig. 6a and b), rapid fixation of CV or Cr(VI) is observed during the first 10 minutes, followed by moderate and slow adsorption beyond the 10th minute. These observations respectively reflect an external and internal mass transfer of CV or Cr(VI) from the solution to the plentiful vacant active sites and mark the progressive saturation of these sites and migration of the adsorbates to the inner pores. However, the slight desorption observed within the GP0 and GP7.5-CP geoadsorbents (Fig. 6b) around 10–30 minutes is due to the electrostatic repulsion between the Cr(VI) ions in solution and those in solid phase before equilibration. On the other hand, in the binary system (Fig. 6c), CV binds preferentially before Cr(VI) within the geoadsorbents due to the more hydrophobic nature of CV compared with Cr(VI). However, the desorption phenomena observed at the surface of the geoadsorbents are due to the competitive effect between CV and Cr(VI) for the same active site. However, this phenomenon is more pronounced on the surface of the GP0 geopolymer due to its fewer sites than those of the GP7.5-CP and GP10-CP geocomposites.
|
| Fig. 6 Effect of contact time on CV and Cr(VI) fixation performance of geomaterials in single (a), (b) and binary (c) systems. Experimental conditions (mGP = 0.1 g, V = 40 mL, T = 25 ± 1 °C and Ci = 120 mg L−1). | |
3.6. Effect of initial concentration of adsorbates in single and binary systems
Fig. 7 shows the influence of the initial concentration of the single and binary systems on the quantities of adsorbate adsorbed and the removal rate. It was found that the concentration gradient accelerated the process of diffusion and fixation of both CV and Cr(VI) on the geoadsorbents, and consequently an increase in the quantities adsorbed in single and binary systems. Furthermore, at the maximum concentration of 120 mg L−1, an improvement in CV and Cr(VI) adsorption performance was observed in the binary regime (2.15 and 17.97% for GP0, 3.25 and 34.29% for GP7.5-CP, 4.24 and 7.95% for GP10-CP respectively) compared with the single solute system. In the mixed system, an increase in the rate of elimination of CV (from 73.60 to 95.76% for GP0, from 93.86 to 96.06% for GP7.5-CP and from 91.26 to 95.76% for GP10-CP respectively) and Cr(VI) (from 5.88 to 67.83% for GP0, from 6.86 to 70.17% for GP7.5-CP and from 5.88 to 70.17% for GP10-CP respectively) was also observed with the initial concentration of adsorbates. The increased adsorption in bi-component system is attributed to the clouding effect of CP to the acidic sites thus improving the uptake of CV with concomitant generation of new adsorption sites for the adsorption of Cr(VI). The adsorbed Cr(VI) ions are also thought to create new surfaces for adsorption of CV.
|
| Fig. 7 Effect of initial concentration on single (a), (b) and binary (c) adsorption of CV and Cr(VI) on geomaterials. Experimental conditions (mGP = 0.1 g, V = 40 mL, T = 25 ± 1 °C and t = 60 min). | |
3.7 Single and binary adsorption kinetics
To elucidate the phenomena governing mono and bi-component adsorption kinetics, non-linear kinetic models of pseudo-first-order,34 pseudo-second-order35 and intraparticle diffusion36 defined by eqn (4), (5) and (7), respectively, were correlated with the experimental contact time data. | Pseudo first order (PFO): qt = qe(1 − e−k1t) | (4) |
| | (5) |
| | (6) |
| Intraparticle diffusion (ID): qt – Kidt1/2 + C | (7) |
where: qt and qe are, respectively, the adsorbed amount (mg g−1) at time t (min) and at equilibrium, respectively. k1 (min−1) and k2 (g mg−1 min−1) represents the PFO and PSO rate constants, respectively. t1/2 is the half adsorption time. Kid is the intraparticle diffusion rate constant (mg g−1 min−1/2), C (mg g−1) is the boundary layer effect index, which provides information about the thickness of the boundary layer.
The coefficients of determination R2 (Tables 2 and 3), which converge towards unity, show that the PFO, PSO and ID models correlate perfectly with the experimental data for the two systems studied. However, the values of t1/2 calculated from eqn (6), which decrease drastically as a function of the CP incorporation rate in single and binary solute adsorption, indicate the increased availability of new functional sites for co-adsorption of CV and Cr(VI). The non-zero values for boundary layer C indicate that diffusion of CV and Cr(VI) into the pores of the geoadsorbents is not the only process governing the rate of adsorption in the two systems studied, which corroborates the results of the work by Deb et al.37 on the sono-assisted adsorption of a binary mixture of dyes (MO and EY) on hematite-PANI-NC. However, the very low Kid values and the increase in the Cr(VI) diffusion boundary layer in mixed solution compared with that in monocomponent solution indicate an increase in the mass transfer into the internal pores induced by the presence of CV.
Table 2 Parameters resulting from kinetic models of CV and Cr(VI) adsorption in a single system
Models |
Parameters |
GP0 |
GP7.5-CP |
GP10-CP |
CV |
Cr(VI) |
CV |
Cr(VI) |
CV |
Cr(VI) |
PFO |
k
1 (min−1) |
2.00 |
1.60 |
1.99 |
0.32 |
0.47 |
1.27 |
q
e (theor) (mg g−1) |
44.85 |
24.60 |
44.06 |
23.48 |
43.83 |
23.43 |
q
e (exp) (mg g−1) |
45.55 |
27.61 |
44.67 |
25.08 |
44.33 |
27.43 |
R
2
|
0.99 |
0.96 |
0.99 |
0.99 |
0.99 |
0.96 |
|
PSO |
k
2 (g mg−1 min−1) |
2.39 |
8.00 |
0.14 |
1.00 |
0.09 |
7.99 |
q
e (theor) (mg g−1) |
45.97 |
24.60 |
44.37 |
23.37 |
44.29 |
23.46 |
q
e (exp) (mg g−1) |
45.55 |
27.61 |
44.67 |
25.08 |
44.33 |
27.43 |
t
1/2 (min) |
0.003 |
0.32 |
0.003 |
0.04 |
0.002 |
0.34 |
R
2
|
0.99 |
0.96 |
0.99 |
0.99 |
0.99 |
0.96 |
|
ID |
K
id (mg g−1 min−1/2) |
0.09 |
0 |
0.01 |
0 |
0.13 |
0 |
C (mg g−1) |
44.16 |
24.60 |
43.98 |
23.31 |
42.99 |
23.43 |
R
2
|
0.99 |
0.96 |
0.99 |
0.99 |
0.99 |
0.96 |
Table 3 Parameters resulting from kinetic models of CV and Cr(VI) adsorption in a binary system
Models |
Parameters |
GP0 |
GP7.5-CP |
GP10-CP |
CV |
Cr(VI) |
CV |
Cr(VI) |
CV |
Cr(VI) |
PFO |
k
1 (min−1) |
1.60 |
1.60 |
0.33 |
0.94 |
0.14 |
0.22 |
q
e (exp) (mg g−1) |
45.97 |
32.56 |
46.51 |
33.54 |
46.16 |
29.89 |
q
e (theor) (mg g−1) |
43.95 |
30.01 |
45.76 |
31.56 |
46.21 |
28.91 |
R
2
|
0.99 |
0.99 |
0.99 |
0.99 |
0.99 |
0.99 |
|
PSO |
k
2 (g mg−1 min−1) |
2.39 |
79.25 |
0.26 |
0.12 |
0.01 |
0.03 |
q
e (exp) (mg g−1) |
45.97 |
32.56 |
46.51 |
33.54 |
46.16 |
29.89 |
q
e (theor) (mg g−1) |
43.96 |
30.02 |
45.44 |
31.84 |
48.68 |
29.55 |
t
1/2 (min) |
0.05 |
2.64 |
0.01 |
0.003 |
0.0001 |
0.001 |
R
2
|
0.99 |
0.99 |
0.99 |
0.99 |
0.97 |
0.99 |
|
ID |
K
id (mg g−1 min−1/2) |
0.16 |
0 |
0.07 |
0 |
1.05 |
0.28 |
C (mg g−1) |
42.87 |
30.01 |
44.81 |
31.56 |
36.26 |
26.33 |
R
2
|
0.99 |
0.99 |
0.99 |
0.99 |
0.94 |
0.99 |
Furthermore, the values of the parameter 1/n > 1 and Gibb's free energy ΔG < 20 kJ mol−1 from the isotherms (Tables 4 and 5) succinctly demonstrated later that physisorption is the rate-determining step governing the fixation of CV and Cr(VI) in binary system.
Table 4 parameters resulting from CV and Cr(VI) adsorption isotherms in a single system
Isotherms |
Parameters |
GP0 |
GP7.5-CP |
GP10-CP |
CV |
Cr(VI) |
CV |
Cr(VI) |
CV |
Cr(VI) |
Langmuir |
Q
max (mg g−1) |
1803 |
784 |
2803 |
3659 |
1632 |
1164 |
K
L (L mg−1) |
0.01 |
0.0006 |
0.01 |
0.0001 |
0.01 |
0.0004 |
R
L
|
0.74 |
0.93 |
0.99 |
0.99 |
0.97 |
0.98 |
R
2
|
0.89 |
0.95 |
0.98
|
0.97 |
0.86 |
0.86 |
|
Freundlich |
1/n |
1.19 |
1.19 |
0.58 |
1.01 |
1.44 |
1.92 |
K
F(L mg−1) |
3.38 |
0.23 |
12.05 |
0.43 |
2.59 |
0.01 |
R
2
|
0.94
|
0.96 |
0.53 |
0.97 |
0.27 |
0.95 |
|
Flory Huggens |
K
FH
|
0.79 |
0.55 |
0.82 |
0.53 |
0.82 |
0.52 |
ΔG (kJ mol−1) |
−16.54 |
−15.63 |
−16.62 |
−15.54 |
−16.62 |
−15.50 |
n
FH
|
0 |
0 |
0 |
0 |
0 |
0 |
R
2
|
0.92 |
0.99 |
0.99 |
0.99 |
0.99 |
0.97 |
Table 5 parameters resulting from CV and Cr(VI) adsorption isotherms in a binary system
Isotherms |
Parameters |
GP0 |
GP7.5-CP |
GP10-CP |
CV |
Cr(VI) |
CV |
Cr(VI) |
CV |
Cr(VI) |
Langmuir |
Q
max (mg g−1) |
6773 |
1866 |
4056 |
1749 |
2274 |
1851 |
K
L (L mg−1) |
0.001 |
0.0004 |
0.002 |
0.0005 |
0.004 |
0.0003 |
R
L
|
0.90 |
0.95 |
0.99 |
0.98 |
0.98 |
0.98 |
R
2
|
0.57 |
0.84 |
0.97 |
0.87 |
0.97 |
0.92 |
|
Freundlich |
1/n |
3.80 |
1.49 |
1.25 |
1.29 |
1.03 |
1.05 |
K
F (L mg−1) |
0.10 |
0.15 |
6.85 |
0.35 |
9.01 |
0.56 |
R
2
|
0.98 |
0.93 |
0.99 |
0.91 |
0.97 |
0.92 |
|
Flory Huggens |
K
FH
|
0.95 |
0.67 |
0.96 |
0.70 |
0.96 |
0.63 |
ΔG (kJ mol−1) |
−16.98 |
−16.13 |
−17.01 |
−16.25 |
−17.01 |
−15.96 |
n
FH
|
0 |
0 |
0 |
0 |
0 |
0 |
R
2
|
0.99 |
0.98 |
0.99 |
0.98 |
0.99 |
0.98 |
3.8 Single and binary adsorption isotherms
To understand the observed synergistic effect and mechanisms associated with the retention of CV or Cr(VI) in single or binary regimes, experimental equilibrium data were correlated with Langmuir, Freundlich and Flory Huggins isotherm models.
3.8.1 Langmuir isotherm.
Langmuir's isotherm is an empirical model designed to describe monolayer-binding mechanisms inducing a uniform distribution of adsorbates on homogeneous active sites on the surface of the adsorbent.38 The Langmuir model equation and the related separation factor are defined by eqn (8) and (9) respectively: | | (8) |
| | (9) |
where qe and Qm are respectively the equilibrium adsorbate quantity (mg g−1) and the maximum Langmuir sequestration capacity (mg g−1), Ce is the equilibrium adsorbate content in solution (mg L−1) and KL is the Langmuir constant (L g−1).
The effect of the simultaneous presence of CV and Cr(VI) on the sequestration efficiency of the bi-component on geomaterials was assessed by calculating the equilibrium adsorption capacity ratio (Rq), defined according to the work of Shikuku et al.39 as follows:
| | (10) |
where
qb,i and
qs,i are the equilibrium adsorption densities (
qe) of the pollutant i in the bi-component and single solute solutions, respectively. If
Rq,i > 1, the binding of adsorbate i is enhanced by the presence of another adsorbate in a binary system (synergistic adsorption), if
Rq,i = 1, the retention of adsorbate i is unaffected by the presence of the other pollutant in the binary system and if
Rq,i < 1, the presence of the other adsorbate in the binary system exacerbates the sequestration of pollutant i (antagonistic adsorption).
With reference to R2 > 0.90, the Langmuir isotherm is appropriate for describing the retention mechanisms of CV and Cr(VI) on the GP7.5-CP geocomposite in a single system (Table 4) and on GP10-CP in a binary system (Table 5). The RL values indicate that the adsorption of these adsorbates is favorable on the surface of these geopolymer composites, whatever the system. However, the maximum adsorption capacity of CV or Cr(VI) adsorbed predicted in a single system from this model for the GP7.5-CP geocomposite are respectively ∼2 to ∼5 times greater than those of the pristine geopolymer. This is due to the threefold positive contributions of higher specific surface area, the new binding sites provided by the incorporation of CP and shielding effect of CP to the acidic sites that negatively impact the adsorption of CV. In addition, a 45% increase in the maximum adsorption density of CV adsorbed on GP7.5-CP and a 59% increase in the quantity of Cr(VI) adsorbed on GP10-CP was observed in the binary system compared with the single system, revealing that adsorption performance is not solely dependent on specific surface area and surface functional groups. In addition, the values of the equilibrium adsorption capacity ratio Rq for CV and Cr(VI) (Table 6) are greater than unity, indicating an increase (synergism) during co-adsorption in the binary system. This supports the hypothesis that adsorbed Cr(VI) provides new adsorption sites for removal of CV and the steric hindrance from adsorbed molecules shield CV molecules from the acidic sites. This phenomenon implies, mechanisms for attaching CV and Cr(VI) to the surface of the composites are different. The ultrahigh maximum adsorption capacities for CV exceed those reported for CV adsorption by geopolymers indicating the incorporation of CP was beneficial.
Table 6 Single and binary adsorption of CV and Cr(VI) on geomaterials
|
GP0 |
GP7.5-CP |
GP10-CP |
CV |
Cr(VI) |
CV |
Cr(VI) |
CV |
Cr(VI) |
q
b,i
|
45.97 |
32.56 |
46.51 |
33.54 |
46.16 |
29.89 |
q
s,i
|
45.55 |
27.61 |
44.67 |
25.08 |
44.33 |
27.43 |
R
q,i
|
1.01 |
1.18 |
1.04 |
1.34 |
1.04 |
1.10 |
3.8.2 Freundlich isotherm.
The Freundlich isotherm usually describes the multilayer adsorption of adsorbates on heterogeneous and non-energetically equivalent active sites.40 The expression of this model is defined by eqn (11).where, KF (L g−1) is the Freundlich constant and n is the Freundlich coefficient.
The values of R2 > 0.90 (Table 5) attest to the adaptability of the Freundlich model in correlating equilibrium data for the mixed adsorption of CV and Cr(VI) for all geoadsorbents. However, values of the Freundlich coefficient 1/n greater than unity reflect cooperative sequestration inducing multiple mechanisms relating to the S-type adsorption isotherm describing strong competition between adsorbates in solution for active sites.41 The cooperative adsorption further supports the postulate that adsorbed Cr(VI) provide new surfaces for adsorption of CV. Furthermore, the higher KF values for CV than for Cr(VI) indicate the high affinity of geocomposites to bind CV in the CV-Cr(VI) system. This difference is linked to four factors; incorporation of CP provided new functional group density and distribution, increased surface area increased accessibility to the active sites, CP clouded the acidic sites that diminish CV adsorption and adsorbed Cr(VI) provided new surfaces for cooperative adsorption of CV. It is further postulated that the presence of Cr(VI) decreased the equilibrium solubility of CV increasing the distribution of CV between the adsorbent and the bulk solution.
3.8.3 Flory Huggins model.
The Flory Huggins isotherm was developed to define the feasibility and spontaneity of adsorbate attachment mechanisms to the adsorbent surface.42 The mathematical expression of this isotherm is given by eqn (12). | | (12) |
where KFH (L g−1) is the Flory Huggens equilibrium constant, ΔG (kJ mol−1) is the Gibbs free energy (eqn (13)) calculated from KFH and the density of water φW (1000 g L−1). | ΔG = −RTlnKFHφW | (13) |
The relatively high coefficients of determination (Tables 4 and 5) show that the Flory Huggens model adjusts the data to equilibrium during the sequestration of CV and Cr(VI) on geoadsorbents in both single and binary systems. Furthermore, the negative values and ΔG < 20 kJ mol−1 indicate respectively that the CV and Cr(VI) fixation process is thermodynamically spontaneous, and that physical-type interactions are predominant at the geomaterial surface favoring PFO kinetics.
3.9 Adsorption mechanism and comparison with other adsorbents
Table 7 compares the adsorption performance of the geopolymer adsorbents in this study in single and binary systems with other adsorbents in the literature. It was observed that the binding performance of the eco-adsorbents in this study for CV and Cr(VI) was ultrahigh compared with that reported by other adsorbents for both single and binary systems. This difference is linked to the synergistic effect of the adsorbents and the high active functional groups density.
Table 7 Comparative data on CV and Cr(VI) sequestration capacities between the geoadsorbents studied and those from previous work
Adsorbent |
CV |
Cr(VI) |
Ref. |
Adsorption capacity in single system (mg g−1) |
Adsorption capacity in binary system (mg g−1) |
Adsorption type |
Adsorption capacity in single system (mg g−1) |
Adsorption capacity in binary system (mg g−1) |
Adsorption type |
NR: not reported. |
Ni/Al@PAB |
— |
— |
— |
271.50 |
NR |
Synergistic |
43
|
CTAB modified geopolymers |
— |
— |
— |
61.30 |
95.30 |
Synergistic |
20
|
LDH/MOF HNC |
— |
— |
— |
787 |
733 |
NR |
44
|
S-nZVI@ZSM-5 |
— |
— |
— |
52.16 |
19.26 |
Antagonistic |
45
|
FeYBC |
— |
— |
— |
24.37 |
NR |
NR |
46
|
Microsphere |
— |
— |
— |
26.80 |
27.12 |
Antagonistic |
19
|
Surfactant modified alumina |
254.30 |
200.44 |
Antagonistic |
— |
— |
— |
47
|
Surfactant modified Spirulina sp. |
101.87 |
4.55 |
Antagonistic |
— |
— |
— |
48
|
NMWNS |
123.20 |
96.01 |
Antagonistic |
— |
— |
— |
49
|
BDHMP-Vt |
956.20 |
NR |
Antagonistic |
— |
— |
— |
50
|
Magnetized polypeptidylated-Hb composites |
NR |
14.8 |
Antagonistic |
— |
— |
— |
51
|
CsTC1 composite |
37 |
NR |
NR |
— |
— |
— |
52
|
GP0 |
1803 |
6773 |
Synergistic |
784 |
1866 |
Synergistic |
This study |
GP7.5-CP |
2803 |
4056 |
Synergistic |
3659 |
1749 |
Synergistic |
This study |
GP10-CP |
1632 |
2274 |
Synergistic |
1632 |
1851 |
Synergistic |
This study |
Taking into account the effect of pH and adsorption isotherms, the probable mechanisms (Fig. 8) linked to the ultrahigh performance of GP-CP eco-geocomposite for CV and Cr(VI) in bi-component system include:
|
| Fig. 8 Probable mechanism for simultaneous fixation of CV and Cr(VI) on the GP-TA eco-composite. | |
– The reduction of HCrO4− to Cr3+ by the electron-donating groups of the geopolymeric chain, favoring respectively the electrostatic attraction of CV and Cr3+ (1) and the exchange of ions (2) on the acid sites of the GP-TA.
– The reduction of HCrO4− to Cr3+ by the electron-donating groups of CP combined with electrostatic attraction (3).
– Electrostatic attraction of HCrO4− to the basic sites of GP-CP (4).
– The formation of hydrogen bonds between CV and the composite surface (5).
These mechanisms are not similar to those reported in the work of Fang et al.19 The authors mentioned that the adsorption of MB in the binary system is controlled mainly by diffusion in the pores, the formation of hydrogen bonds and electrostatic interactions, whereas the fixation of Cr(VI) is governed by diffusion in the pores and redox reactions. The mechanisms controlling the attachment of adsorbates in a mixed system to the surface of the adsorbent depend not only on the composition and textural properties of the geoadsorbent but also on the interactions produced by these adsorbates.
4. Conclusion
This study evaluated single solute and bi-component adsorption of crystal violet (CV) and hexavalent chromium (Cr(VI)) on pozzolan-charcoal powder (CP) waste based geopolymer composites. Physicochemical characterization revealed a 72.47% amorphisation of the geopolymeric structure with the incorporation of 7.5% CP, resulting in a 19% increase in the specific surface area and densification of the functional groups of the resulting GP7.5-CP composite. The adsorption performance of both CV or Cr(VI) were 45 and 59% higher in binary system than in unary system, respectively, denoting synergistic cooperative adsorption (Rq and 1/n > 1). In the single solute system, ultrahigh maximum monolayer adsorption capacity of 2803 and 3659 mg g−1 was observed for CV and Cr(VI) respectively. Adsorption energies supported the physisorption-mediated pseudo-first-order model a better model to describe the adsorption rates in single and binary systems. This study opens up new questions on the mechanisms involved in the adsorption of pollutants in multicomponent systems.
Author contributions
All authors contributed to the review conception, writing sections of the original manuscript, and reviewing of manuscript. All authors read and approved the final manuscript.
Data availability
The data used to support the findings of this study are included within the article.
Conflicts of interest
The authors have no relevant financial or non-financial interests to disclose.
Acknowledgements
The authors declare that no funds, grants, or other support were received during the preparation of this manuscript.
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