Formulation of Synthesized Zinc Oxide Nanopowder into Hybrid Beads for Dye Separation

Abstract

The sol-gel prepared zinc oxide nanopowder was immobilized onto alginate-polyvinyl alcohol polymer blend to fabricate novel biocomposite beads. Various physicochemical characterization techniques have been utilized to identify the crystalline, morphological, and chemical structures of both the fabricated zinc oxide hybrid beads and their corresponding zinc oxide nanopowder. The thermal stability investigations demonstrate that ZnO nanopowder stability dramatically decreased with its immobilization into the polymeric alginate and PVA matrix. The formulated beads had very strong mechanical strength and they are difficult to be broken up to 1500 rpm. Moreover, these hybrid beads are chemically stable at the acidic media (pH < 7) especially within the pH range of 2-7. Finally, the applicability of the formulated ZnO hybrid beads for C.I. basic blue 41 (BB41) decolorization from aqueous solution was examined.

(ProQuest: ... denotes non-US-ASCII text omitted.)

H. Shokry Hassan 1 and M. F. Elkady 2, 3 and A. H. El-Shazly 2 and Hisham S. Bamufleh 4

Academic Editor:Shao-Wen Cao

1, Electronic Materials Researches Department, Advanced Technology and New Materials Researches Institute, City of Scientific Researches and Technological Applications, New Borg El-Arab City, Alexandria 21934, Egypt
2, Chemical and Petrochemical Engineering Department, Egypt-Japan University of Science and Technology, New Borg El-Arab City, Alexandria 21934, Egypt
3, Fabrication Technology Department, Advanced Technology and New Materials Research Institute (ATNMRI), City of Scientific Research and Technology Applications, Alexandria 21934, Egypt
4, Department of Chemical & Materials Engineering, Faculty of Engineering, King Abdulaziz University, P.O. Box 80204, Jeddah 21589, Saudi Arabia

Received 11 December 2013; Revised 11 February 2014; Accepted 28 February 2014; 9 April 2014

This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

1. Introduction

The huge increment in pollution level urges scientific community to research with more and more dedication in environmental remediation. One of the important classes of the pollutants is dyes; dyes have been extensively used in industries, such as textile, paper, printing, cosmetics, plastics, and rubber, for the coloration of products [1, 2]. They usually have a synthetic origin and are based on complex aromatic structures which make them stable and difficult to be biodegraded [1]. A small quantity of dyes can color large water bodies, which not only affects aesthetic merit but also reduces light penetration and photosynthesis. Moreover, many dyes are toxic in nature with suspected carcinogenic and mutagenic effects that affect aquatic biota and also human beings [3, 4]. Therefore, the decolorization of dye-containing effluents is considered compulsory prior to discharge by the environmental regulations in most of the countries [5, 6]. In this respect, C.I. basic blue 41 (BB41) is a mono-azo-basic dye of bright blue hue; it is particularly suitable for dyeing acrylic substrates and can also be applied to some polyamide and polyester types, viscose, cotton, and wool. It is also effective as strainer for the identification of avian leukocytes and blood and bone-marrow cells [7]. This basic dye may be considered as one of the most toxic substances. It can cause eye burns which may be responsible for permanent injury to the eyes of human and animals. On inhalation, it can give rise to short periods of rapid or difficult breathing while ingestion through the mouth produces a burning sensation and may cause nausea, vomiting, profuse sweating, mental confusion, and methemoglobinemia [8, 9]. Consequently, BB41 is selected as one of the simulated dye pollutants to assess its sorption behavior to be eliminated from polluted wastewaters.

Different techniques have been reported by various investigations for the removal of dyes from water and wastewater, including biological processes, combined chemical and biochemical processes, chemical oxidation, adsorption, coagulation, and membrane treatments; each of these has specific advantages and disadvantages. Among these several conventional chemical and physical methods, the adsorption process is one of the effective techniques that have been successfully employed for dye removal from wastewater. Adsorption is a classical technique which involves a variety of highly porous adsorbents to ensure adequate surface area for adsorption [10]. Accordingly, many porous adsorbent materials have been tested on the possibility for dye removal such as activated carbon [11], peat, chitin, and silica [12]. However, intraparticle diffusion associated with porous adsorbents may reduce the adsorption rate and capacity [13]. Consequently, there is a need to develop alternative novel adsorbents with both large surface area and small diffusion resistance characteristics. Recent advances in the field of nanotechnology offer a class of promising adsorbents that are ultrafine and characterized by their large surface area. Nanosized metal oxide nanoparticles have received considerable attention due to the simple procedure involved in synthesis with low capital cost compared to commercially available activated carbon. Diverse inorganic metal oxides may serve as good adsorbents, due to their relatively high surface area and thermal and chemical stabilities. Among these metal oxide nanopowders, Zinc oxide was distinguished by its significant sorption properties toward the polluted harmful ions presence in wastewater [14].

A wide number of methods have been used to prepare ZnO nanopowders, including homogeneous precipitation in aqueous solution of Zn²⁺ cations, hydrothermal synthesis, microwave synthesis, solution combustion, pulsed laser deposition, emulsion precipitation, ultrasonic atomization, spray pyrolysis, freeze-drying, and sol-gel processes [15-17]. Regarding the various stated preparation techniques, sol-gel represents one of the fastest growing fields of contemporary chemistry. Accordingly, this preparation technique was utilized for synthesis of ZnO nanoparticles. This is due to the fact that this preparation technique offers several advantages such as being easy, fast, and able to deform materials into complex geometries in a gel state with high purity [18]. Consequently, zinc oxide nanoparticles can be easily prepared using sol-gel technique. In spite of the prepared zinc oxide nanopowder having good adsorbent for dyes, however it is difficult to be handled in the adsorption techniques due to its small size and hydrophobic nature. In order to overcome this limitation of zinc oxide nanopowder, incorporation of a polymer material with the inorganic metal oxide provides an innovative class of hybrid materials [19]. Many investigators have introduced organic-inorganic hybrid changers consisting of inorganic sorbent materials and organic binding matrices [20, 21]. These materials have conjugated the mechanical properties of the organic polymers with the intrinsic properties of the inorganic compound creating a new class of hybrid organic-inorganic materials with improvement in mechanical properties, chemical inertness, high temperature and radiation stability, reproducibility, and high selectivity for harmful ions. Consequently, inorganic zinc oxide sorbent material may be encapsulated into porous polymeric matrices through the immobilization technique. The porous structure of polymer matrices allows the harmful ions to diffuse into the internal pores and be adsorbed into the internal sorbent materials. So, the major focus was to select a suitable support polymeric material for the immobilization of the synthesized ZnO nanopowder. Various polymer matrices have been employed as immobilized matrix such as alginate, agar, polyacrylamide, chitosan, carrageenan, cellulose acetate, and polyvinyl alcohol (PVA) [22]. PVA may be considered as the largest synthetic water soluble polymer produced in the world and its application as an immobilized polymer matrix was initiated about 20 years ago [23, 24]. PVA is a polymer of great interest because of its desirable characteristics specifically for various pharmaceutical and biomedical applications [23]. PVA offers various advantages over the conventional alginate hydrogels including lower cost, higher durability, and chemical stability and its nontoxicity to viable cells [25]. However, the agglomeration problem that is associated with PVA gel beads is still the main drawback for utilizing PVA as immobilizing polymer matrix. Nevertheless, it is still used by many researchers through adding sodium alginate; thus the agglomeration of PVA gel beads can be reduced [26]. The combination of sodium alginate and PVA has already been reported in PVA-boric acid method, but usually the concentration of sodium alginate was below 0.4%. Generally, sodium alginate used at such low concentration would prevent the agglomeration of PVA gel beads [27]. In the present investigation, we are concerned with formulation of the synthesized zinc oxide nanopowder into innovative biocomposite beads, through the incorporation of ZnO into polymer blend of alginate and PVA. According to our best knowledge, this is the first report that deals with ZnO nanoparticles immobilized into mixed polymer matrices composed of alginate and PVA. So, the main focus of this study is to investigate the physicochemical properties of the fabricated zinc oxide biocomposite beads and their corresponding zinc oxide nanopowder. The feasibility of the formulated hybrid beads towards dye decolorization will be assigned. The variation in the operational parameters that affect behavior of the fabricated biocomposite beads will be examined.

2. Materials and Methods

2.1. Materials

The selected polluted dye model is the azo dye C.I. basic blue 41 (BB41) that was provided by Ciba Specialty Chemicals Inc. and was utilized without further purification; its characteristics and molecular structure are investigated in Table 1. A stock solution of 1000 mg/L was prepared by dissolving 1 g of dye powder in distilled water to prevent and minimize possible interferences and then used for further studies by diluting as required. Zinc chloride, sodium alginate, polyvinyl alcohol, hydrochloric acid, sodium hydroxide, ethanol, and other reagents used in this work were all A.R. grade reagents.

Table 1: Chemical properties of C.I. basic blue 41 dye.

Molecular structure	Molecular formula	C.I. number	Chemical class	Molecular weight (g/mol)
	C20H26N4O6S2	11105	azo	482.57

2.2. Synthesis of ZnO Nanopowder Using Sol-Gel Precipitation Technique

An ammonium hydroxide solution (1 M) was added dropwise into a solution of 0.2 M zinc chloride in the presence of polyvinylpyrrolidone (PVP) with constant stirring till the solution pH is adjusted at 10. The reaction temperature of the solution mixture was maintained at 70°C under constant stirring overnight. The formed fine powder was separated and washed several times with distilled water and ethanol. The washed precipitate was then dried by gentle heating at 50°C. Then the product is ground into fine powder to be immobilized into the polymer matrix.

2.3. Fabrication of ZnO Hybrid Beads (ZOHB)

25 g of PVA has been dissolved in 250 mL of distilled water in the presence of known weight of sodium alginate until attaining clean aqueous solution. After complete dissolution of polymer matrix, 20 g from the synthesized zinc oxide nanopowder has been dispersed into the previous solution. The suspended ZnO slurry was stirred continuously using the homogenizer to ensure the complete nano-zinc oxide dispersion into the polymeric solution mixture. The resultant ZnO polymeric slurry was pumped into the cross-linker solution mixture composed of 3% CaCl₂ and 5% boric acid to be formulated into microbeads. The formed spherical beads were maintained under gentle stirring overnight to complete their gelation. The formulated beads were separated from the cross-linker solution and washed several times with distilled water and then dried at 40°C.

2.4. Characteristic Features of Fabricated ZnO Hybrid Beads and Their Corresponding Nano-Zinc Oxide

Various physicochemical characterization techniques have been utilized to identify the crystalline, morphological, and chemical structures for both the fabricated zinc oxide hybrid beads and their corresponding zinc oxide nanopowder.

In order to identify the main functional groups responsible for the dye sorption process, FT-IR spectra (Shimadzu FTIR-8400 S) of synthesized zinc oxide before and after its fabrication into hybrid beads were examined using KBr disc technique over the wide wavelength range 500-4000 cm^-1 .

The morphological structures of the synthesized nano-zinc oxide and its polymeric hybrid beads were detectable using JEOL JSM 6360LA scanning electron microscope (SEM). Chemical elemental analyses of these two samples were performed using the energy-dispersive X-ray spectroscopy (EDX) unit that combined with SEM equipment.

The crystal structures of both zinc oxide nanopowder and its polymeric hybrid were determined using X-ray diffractometry (Shimadzu-7000 diffractometer) with Cu K α radiation beam ( λ = 0.154060 nm).

The thermal properties of both zinc oxide nanopowder and its polymeric hybrid were investigated over temperature range from ambient condition up to 800°C with a heating rate of 20°C/min in flowing N₂ using Thermal Gravimetric Analysis (Shimadzu TGA-50).

The BET surface area of nano-zinc oxide and its polymeric hybrid was calculated from the nitrogen gas adsorption using the Chemisorption-Physisorption analyzer (Beckman Coulter AS3100, USA).

The chemical stability of the prepared zinc oxide polymeric hybrid toward the hydrogen ion concentration was determined. Different acidic solutions in pH range 1-5 were prepared using hydrochloric acid. On the other hand, different alkaline solutions in pH range 8-12 were prepared using sodium hydroxide. The synthesized hybrid beads were immersed into these different acidic and alkaline solutions for 48 h. After this period the wetted beads were separated and then rinsed with distilled water and dried at 60°C until reaching constant weight [28].

The mechanical stability of the prepared zinc oxide polymeric hybrid beads was assigned using mechanical strength test. This test was performed using homemade designed plexiglass beaker divided into 4 equal segments through baffles (1 cm width). The cylindrical dimension of the beaker was 11 cm in diameter and 13 cm in height. One gram from zinc oxide hybrid beads was added to the beaker followed by 200 mL distilled water. The hybrid beads were agitated in the beaker for 72 h at different controlled mixing speed that varied from 500 rpm to 3000 rpm. The turbidity measurements were detected after the mixing period for each mixing speed. The remaining beads after mixing were counted and then dried in a desiccator until no further change in weight was detected. Each run was performed in triplicate and the average measurements were recorded.

2.5. Evaluation of the Decolourization Behaviour of Fabricated ZnO Hybrid Beads

The decolourization availability of BB41 dye onto the fabricated ZOHB was evaluated through the batch adsorption technique using shaking incubator. Stock solution of BB41 dye (100 mg/L) was prepared. In a typical experiment, a known amount of dry ZnO hybrid beads was mixed with 25 mL of dye solution with specific concentration at conical flask and kept under constant agitation of 400 rpm for 60 minutes in the shaker incubator at different temperatures. After finishing the mixing period, the residual dye concentration was determined calorimetrically through measuring the absorbance of the dye solution at 610 nm using a UV-vis double beam spectrophotometer (Labomed model). The corresponding dye concentration in the supernatant solution was obtained using a previously constructed calibration graph. All the experiments measurements were carried out in duplicate and mean values are presented. The percentage decolourization efficiencies were then obtained using the following equation: [figure omitted; refer to PDF] where _{C 0} is the initial dye concentration (mg/L) and C is the final dye concentration in aqueous solution after phase separation (mg/L).

The ZOHB adsorption capacities were evaluated using the following mass balance equation: [figure omitted; refer to PDF] where Q is the stain uptake capacity (mg/g), _{C 0} and C are the initial and final dye concentrations (mg/L), V is the volume of dye solution (mL), and M is the ZOHB mass (g).

The equilibrium behavior of the basic dye adsorption process onto the fabricated beads was established using Langmuir and Freundlich equilibrium isotherm models. Moreover the kinetic of dye adsorption process was tested using the pseudo-first- and pseudo-second-order kinetic models.

3. Result and Discussion

3.1. Characteristic Features of Fabricated ZnO Hybrid Beads and Their Corresponding Nano-Zinc Oxide

Comparable investigation was established between the fabricated zinc oxide polymeric hybrid and its corresponding zinc oxide nanopowder to declare their characteristic properties.

3.1.1. Crystalline Structure Identification Using XRD

The XRD patterns of pure zinc oxide nanopowder (Figure 1(A)) clearly demonstrated that all the diffraction peaks of the formed ZnO nanoparticles can be indexed to the hexagonal wurtzite structure with high degree of crystallinity [29], which is in good agreement with the value obtained by JCPDS (card number 01-089-1397). Comparing this spectrum with the ZnO reference card, no impurity phase was detected in the XRD pattern of the synthesized ZnO. The main ZnO characteristic diffraction peaks and their orientation planes for the prepared ZnO and its polymeric hybrid were indexed in Figure 1.

Figure 1: XRD spectrums of synthesized pure zinc oxide and its corresponding polymeric hybrid.

[figure omitted; refer to PDF]

However, after immobilizing the prepared nano-zinc oxide onto the polymeric matrix composed of alginate and PVA blend to fabricate the hybrid beads, a new broad peak at 2 θ = 19.6 ° has appeared (Figure 1(B)) beside the previous identified ZnO peaks. The broadening of this peak illustrates the amorphous nature of alginate/PVA polymer blend. This amorphous behaviour may be due to any weak interaction that happened between the two polymers on blending [30]. In fact, PVA structure is collapsed during the complex formation generating the small crystallites and hence an increase in interconnection between two phases leads to the broadening of the peak. This characteristic peak confirms alginate and PVA blending, where if the two polymers have not blended properly, all the respective peaks of both the polymers would have been seen separately which is not present at this case study [31]. Noticeable peak intensities decayed at the fabricated hybrid beads for all ZnO characteristic peaks compared with that presented at the pure zinc oxide nanopowder. This reduction in peaks intensities for the fabricated ZnO hybrid beads was associated with XRD spectrum distortions. This may be attributed to the introduction of the amorphous polymer blend shell matrix that immobilized the nanopowder zinc oxide [32].

3.1.2. Chemical Structure Identification Using FTIR

FTIR analysis technique is utilized to recognize the materials chemical bonding. It is used to identify the elemental constituents of a material. The characteristic peaks exhibited by FTIR spectrums of both zinc oxide hybrid beads and their corresponding nano-zinc oxide were investigated in Figure 2.

Figure 2: FTIR analysis of synthesized pure zinc oxide and its corresponding polymeric hybrid.

[figure omitted; refer to PDF]

All zinc oxide characteristic peaks appeared at the ZnO polymeric hybrid with slight peaks shifting due to presence of the polymer blend matrix that confirm ZnO immobilization onto the polymeric matrix. Where the two FTIR spectrums of ZnO nanoparticles and their polymeric hybrid showed identical characteristic peaks at about 551 cm^-1 in case of pure ZnO which corresponds to the Zn-O bond stretching vibration that shifted to about 505 cm^-1 for the polymeric hybrid [33]. Moreover the medium to weak bands at 889 cm^-1 for pure ZnO and 852 cm^-1 at ZnO polymeric hybrid are assigned to the vibrational frequencies due to the change in the microstructural features into Zn-O lattice [34]. The weak peaks sited at 1165 cm^-1 and 1383 cm^-1 for pure ZnO that shifted to 1064 cm^-1 and 1392 cm^-1 for polymeric hybrid were regarding presence of C-O and C-H vibration modes of PVP, which acts as a capping agent for synthesis of nano-zinc oxide [35]. The remaining ZnO characteristic peaks around 1600 cm^-1 and 3400 cm^-1 are due to normal polymeric O-H stretching vibration of the H₂ O small amount inside the ZnO nanocrystals [36]. Considering the difference between the two spectrums of ZnO and its polymeric hybrid, two new peaks appear at 3100 cm^-1 and 1850 cm^-1 for the ZnO polymeric hybrid that assigned the interaction between alginate and PVA in its polymer blend matrix [31]. It is worth mentioning that the bands appearing in the region of 3100 cm^-1 belong to all types of hydrogen bonded OH groups at the polymer blend and the bands appearing at 1850 cm^-1 belong to all carboxylate groups present at the polymer matrix [37]. This FTIR analysis strongly supports the idea that hydrogen bonding could be formed between the hydroxyl groups of PVA and that group of alginate that composes the immobilized polymer matrix [37].

3.1.3. Morphological Structure Identification Using SEM

SEM imaging is one of the promising techniques for the topography study of the prepared samples, where it gives important information regarding the shape and size of the synthesized particles. The surface morphology of the prepared zinc oxide and its corresponding polymeric hybrid beads is illustrated in Figures 3(a)-3(c). The first entire SEM picture (Figure 3(a)) clearly showed that the as-prepared zinc oxide produced from the sol-gel technique composed of agglomerated nanoparticles with spherical shapes.

The SEM micrographs of (a) pure ZnO nanopowder, (b) cross-section of ZnO polymeric hybrid bead, and (c) internal structure ZnO polymeric hybrid beads.

(a) [figure omitted; refer to PDF]

(b) [figure omitted; refer to PDF]

(c) [figure omitted; refer to PDF]

The average size of these sphere particles is of nanometer size order with average diameter equivalent to 40 nm. The incorporation of these ZnO nanoparticles onto the polymeric hybrid matrix beads was explored in the beads cross-section image (Figure 3(b)). The small lighted spots presence in the bead cross-section area is repressive for ZnO nanoparticles that immobilized onto alginate and PVA polymeric matrix. The homogeneity and uniform distribution of ZnO nanoparticles onto the polymeric matrix were observed from this image. Also, this image investigated clearly the porous structure of the formulated ZnO polymeric hybrid beads. The macroporous structures of the formulated ZnO hybrid beads were obviously clear from Figure 3(c). This micrograph investigates the open pores and cavities that are present inside the hybrid polymeric chains, which serve as host places for dye molecules entrapment during the dye sorption process onto the ZnO hybrid beads. In order to confirm the main constituents of the prepared hybrid beads, quantitative elemental of these beads were performed using EDX analysis. Table 2 investigates the atomic percentages of the hybrid beads elemental composition. It was indicated from this table that the beads are composed mainly of C, O, and Zn and traces from Ca, Na, and B ions. This is confirming that the main components of the hybrid beads are the host mixed polymer matrix of alginate and PVA and the immobilized ZnO nanoparticles.

Table 2: EDX elemental analysis of formulated zinc oxide hybrid beads.

Elements	% atomic
C	29.75
O	51.4
Zn	13.86
Na	2.51
Ca	1.38
B	1.1

3.1.4. Surface Area Identification Using BET

The nitrogen adsorption-desorption isotherms of zinc oxide nanopowder and its corresponding hybrid beads distinguish that both prepared materials are characterized by their high surface area. However, the calculated specific surface area of the formulated ZnO beads that is equal to 22.8 m² /g is comparatively less than that of the free ZnO nanopowder that is equivalent to 64.9 m² /g. Also, the calculated pore volume of 0.132 cm³ /g value for the free powdered ZnO is much higher than that of its corresponding hybrid beads that record 4.64 * ^{10 - 2} cm³ /g. These results may be respective to the conversion of ZnO nanopowder from nanoscale particles into microscale polymeric beads.

3.1.5. Thermal Profile Identification Using TGA

The thermal profiles of both as-prepared ZnO nanopowder and its corresponding polymeric hybrid beads were explored in Figure 4. It was evident from this figure that the thermal stability of ZnO nanopowder was decreased with its immobilization into the polymeric alginate and PVA matrix.

Figure 4: Thermal profiles of synthesized pure zinc oxide and its corresponding polymeric hybrid.

[figure omitted; refer to PDF]

Zinc oxide nanopowder thermal profile shows one degradation step that begins at 180^{[composite function]} C and finishes at 360^{[composite function]} C that represent the surface adsorbed water molecules and the decomposition of traces remaining PVP polymeric matrix that utilized as stabilizing agent during its synthesizing process. After this temperature range ZnO showed high thermal stabilities up to 600°C, which is the characteristic property of all metal oxides. However, the thermal stability of ZnO polymeric beads is comparatively less than its parent ZnO nanopowder, where its thermal profile showed three main degradation steps. The first degradation step at 40-200°C represented the physical water adsorbed onto the polymeric beads. The second degradation step at 200-460°C is due to the thermal degradation of the immobilized polymer matrix that is composed of PVA and alginate [31]. The final degradation step may be corresponding to the byproduct formation of PVA during the TGA thermal degradation process. According to Holland and Hay's observations [38], thermal degradation could lead to the production of aldehyde and alkene end groups in the molten state, which could lead to the formation of vinyl ester by the rearrangement [37]. This result obvious that the ZnO hybrid beads were less thermally stable compared with their parent ZnO nanopowder, which is the leak property of the polymeric materials compared with inorganic compounds.

3.1.6. Chemical and Mechanical Stabilities of ZnO Hybrid Beads

The hybrid beads chemical stability at the acidic media (pH < 7) especially within the pH range of 2-7 indicated that the number of beads remains constant throughout the period of experiment that is confirmed from Figure 5, where this figure investigated that there are no significant weight losses for the hybrid beads at the acidic pH range. This suggested the higher cross-linking inside the hybrid beads. Moreover, their physical appearance remains constant except that their diameter varied due to the water swelling for the porous polymeric hybrid. Accordingly, the hybrid beads were very stable within the acidic pH range. In contrast, regarding the alkaline media (pH > 7), Figure 5 showed notable weight losses for the hybrid beads after drying. These results decided that the excess OH ions that are present in the solution media may act as a chelating agent leading to the decross-linking of the hybrid beads and leaching their immobilized zinc oxide nanopowder that declines their weight. These results are in accordance with the other researchers' founding [39].

Figure 5: Chemical stability of prepared ZnO polymeric hybrid beads at various pH values.

[figure omitted; refer to PDF]

The mechanical properties of the prepared ZnO hybrid beads were elucidated to determine their availability for the column operations. Figure 6 shows evidence that the formulated beads had very strong mechanical strength and they are difficult to be broken, where slight decline in weight losses was noticeable as the mixing speed improved above 1500 rpm. This is due to the rubber-like elastic properties of ZnO hybrid beads, where PVA contributed strength and durability to the beads while alginate improved the surface properties that reduced the tendency to agglomerate [40]. These good mechanical properties were confirmed from the turbidity measurements after the stirring period. Slight observed turbidity was noticed as the agitation speed incremented above 2000 rpm (Figure 6). Accordingly, these hybrids beads are suitable to be packed into the treatment column to be utilized for continuous treatment operation.

Figure 6: Mechanical stability of prepared ZnO polymeric hybrid beads at various mixing speeds.

[figure omitted; refer to PDF]

3.2. Dye Decolorization Properties of Zinc Oxide Polymeric Hybrid Beads

The feasibility of the formulated ZnO polymeric hybrid beads for C.I. basic blue 41 dye decolorization from synthetic waste streams was examined. The applicability of the synthesized microbeads for dye removal was tested as a function of the different factors that affect the dye sorption process including the variation in contact time (0-120 min), initial dye concentration (1-100 ppm), dosage of ZnO hybrid beads (1-10 g/L), dye solution pH (1-9), and dye solution temperature (25-80°C).

3.2.1. Effect of Contact Time on the Dye Sorption Process onto ZnO Hybrid Beads

The effect of contact time on the adsorption of the basic blue dye onto zinc oxide hybrid beads was investigated over 120 minutes of time intervals. It can be noticed from Figure 7 that the removal of dye by adsorption onto ZOHB was found to be rapid at the initial period of contact time and then to slow down with time until reaching a constant value where no more dye was removed from the solution. At this point, the amount of dye being adsorbed onto the adsorbent was in a state of dynamic equilibrium with the amount of dye desorbed from the adsorbent. The time required to attain this state of equilibrium was termed the equilibrium time and the amount of dye adsorbed at the equilibrium time reflected the maximum dye adsorption capacity of the adsorbent under these particular conditions [41]. Figure 7 investigates that the equilibrium time of dye sorption onto ZOHB was recorded within 60 minutes.

Figure 7: Effect of contact time on dye sorption process (pH = 6, initial dye concentration = 10 ppm, agitation speed = 400 rpm, ZOHB dosage = 5 g/L, and temperature = 22°C).

[figure omitted; refer to PDF]

3.2.2. Effect of ZnO Hybrid Beads on the Dye Sorption Process

The effect of ZOHB dosage on both the percentage dye removal and the beads sorption capacity was examined after 60 minutes. Figure 8 indicated that the percentage of dye decolorization was enhanced from 78.5 to 98.8% as ZOHB improved from 1 to 10 g/L as well as an emphasized decrease being noticeable for the beads sorption capacity with increasing their concentrations. The decrease in unit adsorption with increasing beads concentration is basically due to adsorption sites remaining unsaturated during the adsorption reaction [41, 42]. Meanwhile, the improvement in the ZOHB dosage increases the adsorbent surface and the availability of more adsorption sites for dye removal. The optimum ZnO hybrid beads dosage that achieved the optimum dye decolourization percentage of 94.9% has been recorded from Figure 8 to be equal to 5 g/L.

Figure 8: Effect of ZnO hybrid beads dosage on both the percentage of dye decolourization and dye uptake capacity (pH = 6, initial dye concentration = 10 ppm, agitation speed = 400 rpm, contact time = 60 min, and temperature = 22°C).

[figure omitted; refer to PDF]

3.2.3. Effect of Initial pH on Dye Adsorption Process

The pH of the dye solution plays an important role in the whole adsorption process. The dye adsorption process is highly pH dependent especially for the cationic dye adsorption [43]. The adsorption of these positively charged dye groups onto the adsorbent surface is primarily influenced by the surface charge of the adsorbent which in turn is affected by the pH of solution. Many oxide surfaces create a surface charge (positive or negative) [44]. Zinc oxide as most of metal oxide materials has an amphoteric character in aqueous medium; that is, it has hydroxyl groups only in acidic solutions (pH 4 and 6) and is converted into an anion-exchanger as the solution pH improved above 6 [45]. In this regard, the initial pH of the dye solution was studied within pH range from 1 to 9 and all other parameters were kept constant. Figure 9 investigates that, at the high acidic dye solution (low pH value), the percentage dye sorption removal was increased but with low limitations from 18% to 45.5% as the dye pH value increased from 1 to 3. Thereafter, the decolorization process increases rapidly and reaches a maximum level of 94.9% at the pH of 6. As the dye solution pH incremented above value 6, the dye sorption removal dramatically decreased. These three different dye sorption behaviours may be explained as, at low pH value, the lower dye sorption onto ZOHB may be due to the presence of excess H⁺ ions competing with the positive groups on the dye for the beads adsorption sites. As the solution pH increased (above 3), the active surface sites of the immobilized ZnO onto the hybrid beads are deprotonated and the competition between H⁺ and dye cationic for the adsorption sites lessens, which increase the dye adsorption amount. So, the higher dye uptake values obtained at higher pH (above 3) values are due to the electrostatic attractions between the positively charged dye anions and the immobilized negatively charged ZnO [46]. As the solution pH incremented above 6, the immobilized ZnO nanospecies were positively charged and converted into an anionic-exchanger; accordingly, electrostatic repulsion forces between the ZOHB and the dye anions will be induced that decrease the dye uptake onto the hybrid beads.

Figure 9: Effect of dye solution pH on the percentage of dye decolourization (initial dye concentration = 10 ppm, ZOHB dosage = 5 g/L, agitation speed = 400 rpm, contact time = 60 min, and temperature = 22°C).

[figure omitted; refer to PDF]

3.2.4. Effect of Initial Dye Concentration Process

The effect of initial dye concentration on the equilibrium adsorption capacity ( _{q e} ) was carried out in the range of 1-100 mg/L at pH 6 using 5 g/L from the ZOHB for 1 h. The effect of initial dye concentration on the basic dye equilibrium adsorption capacity ( _{q e} ) and removal efficiency were illustrated in Figure 10. This figure explores that there is linear enhancement in the dye sorption capacity as the initial concentration of the dye is increased from 1 to 100 mg/L, which is in accordance with the previous studied researches [47]. The improvement in the dye sorption capacity as the initial dye concentration incremented was companied with a lower removal efficiency of the basic blue dye. This may be due to the saturation of the adsorption sites on the ZnO beads as the concentration of the dye increases. According to these results, the formulated zinc oxide hybrid beads are effectively capable of removing the C.I. basic blue 41 dye in solutions of a wide region of dye concentration completely.

Figure 10: Effect of initial dye concentration on both the percentage of dye decolourization and dye uptake capacity (pH = 6, ZOHB dosage = 5 g/L, agitation speed = 400 rpm, contact time = 60 min, and temperature = 22°C).

[figure omitted; refer to PDF]

3.2.5. Effect of Solution Temperature on Dye Adsorption Process

Temperature is well known to play an important role during the adsorption processes. It can affect several aspects of adsorption, for example, dye solubility, the swelling capacity of the sorbent, and the equilibrium position in relation to the endo- or exothermicity of the adsorption phenomenon [48]. So, the effect of temperature on the equilibrium basic blue dye adsorption onto the synthesized ZOHB was investigated in the temperature range of 25-80°C. The increment in the dye solution temperature has a negative effect on the dye adsorption process onto the prepared material as predicted from Figure 11. This indicated that the adsorption of the basic blue dye onto the synthesized ZOHB is an exothermic process. The decrease in the rate of adsorption with the increase in temperature may be attributed to the tendency of dye molecules to escape from the solid phase to bulk phase with the improvement in solution temperature [49]. Accordingly, it was reliable that the dye sorption process onto the fabricated composite beads is not favorable at the elevated dye solution temperature (above 25°C). This result may be explained by the deactivation of the zinc oxide polymeric beads surface or the destruction of some polymeric active sites on the adsorbent surface due to bond rupture [50].

Figure 11: Effect of dye solution temperature on the percentage of dye decolourization (initial dye concentration = 10 ppm, ZOHB dosage = 5 g/L, agitation speed = 400 rpm, contact time = 60 min, and pH = 6).

[figure omitted; refer to PDF]

Temperature dependence of the dye adsorption process onto ZOHB is associated with various thermodynamic parameters. To study the thermodynamics of the adsorption process, the standard Gibbs free energy of the process was evaluated by [51] [figure omitted; refer to PDF] The equilibrium constant _{k c} was evaluated at each temperature using the relationship [figure omitted; refer to PDF] where _{C Be} and _{C Ae} represent the equilibrium concentrations of dye on the ZOHB adsorbent and solution, respectively. Standard enthalpy ( Δ ^{H °} ) and entropy ( Δ ^{S °} ) were determined from the Van't Hoff equation: [figure omitted; refer to PDF] where ^{Δ H °} and ^{Δ S °} were obtained from the slope and intercept of the plot of ln _{k c} versus 1/T as shown in Figure 12 and listed in Table 3. Values of free energy changes ^{Δ G °} are negative, confirming that the dye adsorption process onto ZOHB is spontaneous and thermodynamically favorable. The decline in the negative values of ^{Δ G °} with the improvement in temperature decreases the driving force at the adsorption process. Accordingly, the improvement in temperature has negative impact on the dye sorption process. The value of ^{Δ H °} is negative, indicating that the adsorption process is exothermic in nature, while the negative value of entropy change ( ^{Δ S °} ) shows a decreased disorder at the solid/liquid interface during dye sorption. As the temperature increases, the mobility of dye ions increases causing the ions to escape from the solid phase to the liquid phase. Therefore, the amount of dyes that may be adsorbed will be decreased [51].

Table 3: Thermodynamic parameters for dye adsorption onto ZOHB.

T (K)	Δ G ° (kJ mol-1 )	Δ H ° (kJ mol-1 )	Δ S ° (J mol-1 K-1 )
298	-7.24	-2.07	-4.199
308	-6.08
318	-5.53
338	-4.62
353	-3.15

Figure 12: Arrhenius plot for dye sorption onto ZOHB at different solution temperatures (initial dye concentration = 10 ppm, ZOHB dosage = 5 g/L, agitation speed = 400 rpm, contact time = 60 min, and pH = 6).

[figure omitted; refer to PDF]

3.3. Equilibrium Isotherm Analysis of Dye Adsorption Process

Equilibrium data, commonly known as adsorption isotherms, are basic requirements for the design of adsorption systems [52]. In this regard, the equilibrium data for BB41 on the fabricated hybrid beads were modeled using the well-known isotherm models of Langmuir and Freundlich models. The plot of _{C e} / _{q e} versus _{C e} (Figure 13) indicates a straight line with low value of the correlation coefficient ( ^{R 2} = 0.8017 ) for the linearized plot of the equation that is represented as [53] [figure omitted; refer to PDF] where _{q e} is the amount adsorbed (mg/g), _{C e} is the equilibrium concentration of the adsorbate ions (mg/L), and _{q m} and K are Langmuir constants related to maximum adsorption capacity (monolayer capacity) (mg/g) and energy of adsorption (L/mg), respectively. Accordingly, the Langmuir isotherm model may be not adequate to describe the dye sorption process onto the fabricated zinc oxide hybrid beads.

Figure 13: Langmuir isotherm for BB41 dye adsorption onto ZOHB.

[figure omitted; refer to PDF]

Consider that Langmuir isotherm model assumes a monolayer coverage and uniform activity distribution on the adsorbent surface, which represent unexpected behavior for the decolorization of studied case onto the fabricated beads. However, the adsorption of basic blue dye onto ZOHHB beads suggested being a quite complex process, probably through forming multilayers and even closing some of the available pores at the bead surfaces [54]. Also, a variation of sorption activity is expected with surface coverage. So it can be expected that the Freundlich isotherm model was more suitable to describe the experimental data compared with Langmuir model. The linearized form of the Freundlich equation may be expressed as [41] [figure omitted; refer to PDF] where _{K F} and _{n f} are Freundlich constants related to adsorption capacity and adsorption intensity, respectively. The Freundlich constants are related to the surface heterogeneity. Figure 14 investigates the Freundlich linear fit for the dye sorption process onto the fabricated hybrid beads. It is obvious that the correlation coefficient value ( ^{R 2} = 0.991 ) obtained through Freundlich isotherm is higher than that of the Langmuir fitting. So, Freundlich model was more appropriate for the prediction of the isothermal profiles for the basic dye sorption process onto the zinc oxide polymeric hybrid beads. This observation suggested that the sorption process is heterogeneous in nature and accomplished with a nonuniform distribution of heat of adsorption. The calculated _{n f} value that is equal to 1.45 was greater than unity and indicated that the dye sorption process onto ZOHB was favorable.

Figure 14: Freundlich isotherm for BB41 dye adsorption onto ZOHB.

[figure omitted; refer to PDF]

3.4. Kinetic Model of Dye Adsorption Process

The rate at which dissolved dye is removed from the aqueous solution by solid sorbents is essential to evaluate the adsorption kinetics using theoretical models in order to design and control the sorption process units. So, the applicability of the pseudo-first-order and pseudo-second-order models was tested for the adsorption of BB41 onto ZOHB. The best-fit model was selected based on the linear regression correlation coefficient, ^{R 2} , values. The Lagergren first-order equation is given as [55] [figure omitted; refer to PDF] where _{q e} and _{q t} are amounts of dye ions sorbed (mg/g) at equilibrium and at time t (min), respectively. _{k 1} (min^-1 ) is the first-order reaction rate constant. If the pseudo-first-order kinetics is applicable to the experimental data, a plot of ln( _{q e} - _{q t} ) versus t should present a linear relationship, as investigated in Figure 15; the calculated values of _{k 1} and _{q e} can be determined from the slope and intercept of the plot, respectively. The values of ^{R 2} for the sorption of different initial concentrations of basic blue dye ions onto ZOHB are tabulated in Table 4.

Table 4: Kinetic parameters of dye adsorption onto ZOHB at different dye concentrations.

Kinetic model	( q e )exp (mg/g)	Pseudo-first order	Pseudo-second order
Dye concentration (mg/L)	( q e )cal (mg/g)	K 1 (min-1 )	R 2	( q e )cal (mg/g)	K 2 (g/mg min)	R 2
1	0.193	0.19	-0.052	0.99	0.34	0.089	0.958
10	1.89	1.88	-0.0053	0.98	2.56	0.018	0.967
25	4.35	4.3	-0.0053	0.98	5.87	0.0079	0.985
50	8.5	8.9	-0.006	0.966	11.67	0.0041	0.975
75	12.54	18.9	-0.076	0.94	22.98	0.00114	0.917
100	16.25	19.1	0.078	0.94	25.2	0.0012	0.93

Figure 15: Pseudo-first-order kinetic model for BB41 dye adsorption onto ZOHB.

[figure omitted; refer to PDF]

On the basis of linear regression values from this table ( ^{R 2} ), it may be predicted that the kinetics of dye sorption onto ZOHB be described well by the first-order kinetic model. Comparing the values of _{q e} calculated from the reaction kinetic curves (Table 4) with the experimental data, it is noticeable that the calculated _{q e} values that were obtained from the first-order kinetic model were compatible with the experimental _{q e} values. Thus, the first-order rate expression fits the data most satisfactorily. This gives prediction that the dye sorption process may take place basically through the physical sorption [56].

Moreover, the experimental kinetic data were further analyzed using the pseudo-second-order kinetic model that may be expressed in the following form [54]: [figure omitted; refer to PDF] where _{k 2} is the second-order reaction rate equilibrium constant (g/mg min). The plotting of t/qt against t for different initial BB41 concentrations (Figure 16) investigated straight lines with low values of correlation coefficients compared with the first-order rate model (Table 4) for the different studied dye concentrations especially for the high dye concentrations. Also, the estimated values of _{q e} calculated from the equation differed from the experimental values. Accordingly, the first-order rate model is more appropriate to describe the dye sorption process onto the zinc oxide hybrid polymer compared with the second-order rate model.

Figure 16: Pseudo-second-order kinetic model for BB41 dye adsorption onto ZOHB.

[figure omitted; refer to PDF]

4. Conclusion

A novel fabricated microbead was successfully prepared from immobilization of the sol-gel synthesized zinc oxide nanopowder onto the PVA and alginate polymer matrix. The XRD and SEM results strongly support the physical interactions between zinc oxide nanoparticles and the polymer blend matrix. Furthermore, SEM examination and EDX analysis of the formulated hybrid beads confirm the incorporation of ZnO nanoparticles onto the polymeric hybrid matrix. Incorporation of polymeric matrix at the prepared zinc oxide hybrid beads decreases its thermal stability relatively compared with its immobilized pure zinc oxide. However, this polymer matrix has not any significant effect in the chemical and mechanical stabilities of the zinc oxide hybrid beads, where it is characterized by its good chemical and mechanical properties. The formulated hybrid beads have high dye adsorption performance for the C.I. 41 basic blue dye. The maximum dye sorption capacity was recorded as 16.5 mg/g using 100 ppm initial dye concentration. The improvement in the beads dosage has positive impact on the percentage dye removal. Meanwhile, the increment in both initial dye concentrations and dye solution temperature has negative impact on the dye sorption process onto the fabricated beads. The experimental results and Van't Hoff equation plot confirm that the dye adsorption process is exothermic. The equilibrium isotherm data of the dye sorption process was described well using the Freundlich isotherm model. However, the kinetics of basic dye sorption process onto the fabricated hybrid beads obeys the pseudo-first-order kinetic model, indicating that the dye sorption process may take place basically through the physical sorption.

Acknowledgment

This work was funded by the Deanship of Scientific Research (DSR), King Abdulaziz University. Jeddah, under grant No. (135-021-D1434). The authors, therefore, acknowledge with thanks DSR technical and financial support.

Conflict of Interests

The authors declare that there is no conflict of interests regarding the publication of this paper.

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