J. L. L. ANTONI et al.: 4-TERT-BUTYLBENZOIC ACID-INCORPORATED POLYSTYRENE: AN EFFECTIVE ... 485–490 4-TERT-BUTYLBENZOIC ACID-INCORPORATED POLYSTYRENE: AN EFFECTIVE CATION-EXCHANGE POLYMER MATRIX FOR THE REMOV AL OF METAL IONS FROM TANNERY EFFLUENT ZDRU@ITEV 4-TERC BUTIL-BENZOJSKE KISLINE S POLISTIRENOM: U^INKOVITA ODSTRANITEV KOVINSKIH IONOV V ODPADNIH VODAH Z IZMENJA VO KATIONOV V POLIMERNI MATRICI John Louis Louis Antoni 1* , Senthilkumar Ganapathy 1 , Lekshmi Gangadhar 2 , Mukesh Kumar Dharmalingam Jothinathan 3 , Lourdusamy Emmanuvel 4 1 Department of Civil Engineering, Annamalai University, Annamalai nagar, Chidambaram, TamilNadu – 608002, India 2 Department of Nanotechnology, NanoDot Research Private Limited, Nagercoil, TamilNadu-629001, India 3 Centre for Global Health Research, Saveetha Medical College and Hospitals, Saveetha Institute of Medical and Technical Sciences (SIMATS), Saveetha University, Chennai-602105, India 4 Department of Civil Engineering, Government Polytechnic College, Valangaiman, Tiruvarur, TamilNadu-612804, India Prejem rokopisa – received: 2024-04-23; sprejem za objavo – accepted for publication: 2024-06-24 doi:10.17222/mit.2024.1164 The preparation of a 4-tert-butylbenzoic acid-incorporated polystyrene matrix as the polymer matrix for removing the metal ions present in water is reported. The hydrophobic interaction between the polystyrene and the tert-butyl group of carboxylic acid was exploited to bind the carboxylic acid on polystyrene. Thus prepared polymer matrix was investigated for its ability to ex- change and remove metal ions from water. Better efficiency was obtained with different metal ions, including copper, iron, cal- cium, magnesium, chromium (III), etc., during a batch process as well as a continuous process. The carboxylic acid was not leached out during the process and the hydrophobic force was strong enough to avoid leaching out. Further, it was employed to remove metal ions, particularly chromium, from tannery effluent. Keywords: chromium, hydrophobic interaction, ion exchange, metal removal, tannery treatment V ~lanku avtorji opisujejo pripravo polistirenske matrice zdru`ene z 4-terc butil-benzojsko kislino. Tako izdelana polimerna matrica naj bi delovala kot u~inkovit izmenjevalnik kovinskih ionov, ki so prisotni v odpadnih vodah strojarn `ivalskih ko`. Avtorji so izkoristili hidrofobno interakcijo med polistirenom in terc-butilno skupino karboksilnih skupin za vezavo karboksilne kisline na polistiren. Nato so avtorji raziskovali sposobnost izdelane polimerne matrice za izmenjavo in odstranitev kovinskih ionov iz odpadne vode, uporabljene za strojenje ko`. Avtorji so ugotovili ve~jo u~inkovitost izmenjave za vrsto kovinskih ionov vklju~no z Cu, Fe, Ca, Mg, Cr(III) itd. Izmenjava je potekala u~inkovito tako v {ar`nem kot tudi kontinuirnem procesu. Karboksilno kislino niso izlu`ili med procesom in hidrofobna sila je bila dovolj mo~na, da ni pri{lo do izlu`enja (ekstrakcije). Avtorji so uporabili izdelano matrico posebej uspe{no za odstranitev razli~nih kovinskih ionov, predvsem ionov kroma iz odpadne vode v strojarnah `ivalskih ko`. Klju~ne besede: krom, hidrofobna interakcija, izmenjava ionov, odstranitev kovin, obdelava odpadnih voda strojarn `ivalskih ko` 1 INTRODUCTION The usage of leather for making various products like shoes and boots, belts, apparel, purses, luggage bags, sports materials, etc., has been known since the iron age. 1 The durability and elegant look make leather prod- ucts a symbol of status. Leather production involves hide preparation, tanning and finishing. The tanning process can be carried out either with vegetable tanning or chrome tanning. Chrome tanning is a more preferred technique for the production of large quantities in indus- tries since chrome tanning can be completed in one day while vegetable tanning requires two weeks. 2 In addition, chrome-tanned leather is softer than vegetable-tanned leather; it also exhibits high hydrothermal stability and good dying properties so that better finishing can be achieved. 3,4 The skin from a slaughter house is subjected to several step processes and treated with several organic and inorganic chemicals to get better finished leather products. The chemicals include chromium sulphate, biocides like DDT, formaldehyde, a base like calcium hydroxide, a reducing agent like sodium sulphide, ani- line-based dyes and solvents like dichloromethane, ben- zene, ethanol, etc. 5,6 During chrome tanning, chromium binds to and stabilizes the collagen, a peptide containing glycine, proline and 4-hydroxy proline in major along with other amino acids including aspartic acids and glutamic acids. 7 The carboxylic acid group of collagen becomes bonded with chromium and thus chromium is incorporated into the hide. The chemistry behind this process is complex and it is given in Figure 1. Chromium sulphate in a solution forms [Cr(H 2 O) 6 ] 3+ which is an aqua acid (red violet in colour) and readily deprotonates at a higher pH to give [Cr(H 2 O) 5 OH] 3+ Materiali in tehnologije / Materials and technology 58 (2024) 4, 485–490 485 UDK 577.11:546.3 ISSN 1580-2949 Original scientific article/Izvirni znanstveni ~lanek MTAEC9, 58(4)485(2024) *Corresponding author's e-mail: sllouis1966@gmail.com (John Louis Louis Antoni) (green colour). Further, this complex polymerizes at a higher pH, i.e., the basic condition allowing a polychromium complex. 7 The carboxylic acid residue present in the glutamic acid and aspartic acid of collagen forms carboxylate ions upon treatment with lime (Ca(OH) 2 ). The carboxylate anion displaces the water molecule from the polychromium complex via coordina- tion and thus chromium is incorporated in the hide. 8 The chromium that is bound to the collagen of leather gives softness, flexibility and suppleness to tanned leather. A study shows that 90 % of leather is processed with chrome tanning as it is quick and easy. In spite of its advantages, chrome tanning also poses a serious threat to the environment as chromium salt is not fully absorbed by the collagen and a portion of chromium is discarded in the effluent. 9 Fortunately, Cr(III) is less toxic compared to Cr(IV) as Cr(III) is not readily ab- sorbed by the body. While chromium (III) is essential for the regular operation of human vascular and metabolic systems as well as combating diabetes, too much chro- mium (III) may result in a severe skin rash, or other more serious symptoms. Also, Cr (III) can cause severe envi- ronmental issues and pose a severe threat to aquatic life. 10 Several research efforts have been carried out to re- move chromium (III) from the tannery effluent. 11 The techniques include adsorption 12 (rice husk, pumice, acti- vated carbon from sugar industry, clay, zeolites, peat moss, chitin and agricultural wastes like neem bark, wal- nut shell, rice husk, tea waste, sugar industry waste, ba- nana rachis charcoal, chitin–humic acid, etc.), chemical precipitation (calcium hydroxide [Ca(OH) 2 ], sodium hy- droxide (NaOH), magnesium oxide (MgO), or calcium magnesium carbonate [CaMg(CO 3 ) 2 ], coagulation and flocculation (aluminium sulphate [Al 2 (SO 4 ) 3 ·18H 2 O] and ferric chloride (FeCl 3 ·6H 2 O), calcium carbonate (CaCO 3 ), ammonium aluminium sulphate [NH 4 Al(SO 4 ) 2 ], aluminium sulphate [Al 2 (SO 4 ) 2 ], and so- dium citrate (Na 3 C 6 H 5 O 7 ), ferric chloride and organic polymer), ion exchange 13 (zeolite, ion exchange resin, macroporous carboxylic resin), membrane filtration tech- niques like reverse osmosis (RO), 14 nanofiltration (NF), ultrafiltration (UF), microfiltration (MF) 15 and electrodialysis (ED) electrochemical treatment like elec- tro-deposition, 16 electrocoagulation, 17 electro-disinfec- tion, electro-oxidation, 1 electro-reduction, electro-osmo- sis, and electro-flotation. These are some of the many research methods for removing Cr from the tannery waste. 18 Though several methods for removing metals from water are available, development of new methods that are cheap and carried out with a readily accessible material, is required. In this paper, we report on a simple and cost-effective method for removing transition metals from water, in particular Cr (III) ions from the secondary treated tannery water. This method involves a polysty- rene film incorporated with 4-tert-butylbenzoic acid (TBBA) that binds to the surface of polystyrene through J. L. L. ANTONI et al.: 4-TERT-BUTYLBENZOIC ACID-INCORPORATED POLYSTYRENE: AN EFFECTIVE ... 486 Materiali in tehnologije / Materials and technology 58 (2024) 4, 485–490 Figure 1: Chrome tanning process a hydrophobic interaction and can exchange metal ions with protons. 2 EXPERIMENTAL PART Substrates were purchased from Avra synthesis, SD fine, Spectrochem and Merck. AR grade methanol and CH 2 Cl 2 were used as such without further purification. A rotary evaporator was used for evaporation under a re- duced pressure. A SEM analysis was carried out with a TESCAN VEGA3. The analysis of metal ions was car- ried out following the standard procedure. Double-dis- tilled water was used for preparing a solution of known salts. Complexometric titrations were carried out for the estimation of Cu, Ca, Mg, Zn using suitable indicators and buffer solutions. Fe (II) and Fe (III) were estimated using permanganometry and spectrophotometry, respec- tively. 2.1. General procedure for a TBBA-incorporated poly- mer matrix Commercially available polystyrene (1 g) and 4-tert- butylbenzoic acid (0.1 mmol) were dissolved in 30 mL of CH 2 Cl 2 and the solution was poured onto a Petri dish. Over time, the organic solvents became evaporated, leav- ing back flakes of TBBA-incorporated polystyrene. The flakes were washed with more polar methanol (20 mL) to remove any excess TBBA that was not tightly bound to the polymeric matrix. 2.2. General procedure for the removal of metal ions from the solution A column with sintered disc (20 mm) is tightly packed with 10 g of TBBA-incorporated polystyrene. The height is approximately 8 cm. 20 mL of a metal-salt solution (with a concentration of 1000 ppm or 1 mg/mL) together with NaHCO 3 (0.05 mmol) is poured over the column through the inner walls without disturbing the column packing. The stopcock is partially open and the solution is allowed to flow dropwise and be collected in the conical. Thus collected solution is analysed for the presence of metal ions. 2.3. Batch process A beaker is charged with1go fT B B A-incorporated polystyrene and 20 mL of the metal-salt solution (a con- centration of 1000 ppm) together with NaHCO 3 (0.05 mmol) and a magnetic pellet. The mixture is stirred with the help of magnetic stirrer for 10 minutes and the mixture is decanted. Thus collected solution is analysed for the presence of metal ions. 3 RESULTS Cationic ion-exchange resin was successfully em- ployed to remove the metals like Ca, Mg, Cr, etc., from water. Though the process is promising, the cost of the ion-exchange resin is the major concern. The carboxylic acid incorporated onto the polystyrene through a hydro- phobic interaction, rather than a covalent bond, could play the role in the cationic ion-exchange resin and might also be cost-effective. The choice was TBBA since it has a large lyophilic/hydrophobic part oriented oppo- site to hydrophilic carboxylic acid. Further, the aromatic part can impart rigidity to the whole molecule once it is bound to the polymer matrix. Initially, the carboxylic acid (4-tert-butylbenzoic acid, TBBA)-incorporated polystyrene flakes were prepared by simply dissolving and evaporating. In the Petri dish, the polystyrene solu- tion with 1 mmol of 4-tert-butylbenzoic acid was dried to obtain flakes of a TBBA-incorporated polystyrene film. After drying, the film was washed with more polar meth- anol to remove any TBBA present on the surface and also washed with water before characterization. Upon evaporation of the methanol, 0.07 mmol (12 mg) of TBBA was obtained. This clearly indicated that the ma- jor portion of the TBBA was incorporated in the polysty- rene film. The surface of the polystyrene film was stud- ied with SEM at various magnifications, as shown in Figure 2. The TBBA-polystyrene flakes were soft, hav- ing an irregular shape and surface. Under a high resolu- tion (1 μm), one can observe several tiny humps on the surface which are attributed to the binding of the TBBA to the surface. Further, the sample was analysed with in- frared spectroscopy, i.e., by dissolving the it chloroform and using a NaCl crystal as the sample holder. The J. L. L. ANTONI et al.: 4-TERT-BUTYLBENZOIC ACID-INCORPORATED POLYSTYRENE: AN EFFECTIVE ... Materiali in tehnologije / Materials and technology 58 (2024) 4, 485–490 487 Figure 2: SEM images of 4-tert-butylbenzoic acid-incorporated poly- styrene film carboxylic acid group appears as the intense peak at 1754 cm –1 . As there is no possibility of chemical bonding be- tween the polystyrene and TBBA, it is presumed that the hydrophobic part of TBBA is bound to the hydrophobic polystyrene while the more polar hydrophilic carboxylic acid group is exposed at the surface, as shown in Fig- ure 3. After successful preparation of the TBBA-incorpo- rated polystyrene, focus was given to the exploitation of the ion exchange property of the carboxylic acid group, removing various metal ions from the solution. The effi- ciency in the batch process as well as the continuous pro- cess were studied. As the continuous process required more TBBA polystyrene it was limited to highly toxic copper and chromium. Table 1: Removal of metal ions by TBBA-incorporated polystyrene a S. No. Metal ions b Concentration of metal ions after treatment (gm) c 1 Cu (I) 0.7 (0.8) d 2 Cu (II) 0.8 f 3 Fe (II) 1.1 h 4 Fe (III) 5.0 (4.5) e, g 5 Cr (III) 0.6 (0.8) d 6 Ni (II) 1.0 7 Zn (II) 0.3 f 8 Ca (II) 0.3 f 9 Mg (II) 0.3 f a refers to the experimental section, b metal sulphates with a concentra- tion of 1 ppm/mL were used. c indicates the amount of metal ions after the treatment with a batch process. d 0.1 mol% NaHCO 3 was em- ployed. e indicates a continuous process. f complexometric titration was used to measure the metal ions. g analysed by a spectrophotometer using KSCN. h permanganometry was used. Initially, ion-exchange absorption with several most common metal-ion solutions and without any base (pH 7) was attempted. The absorption was very poor which clearly indicates that –CO 2 H has a poor ligating property with the metal. Inspired by the collagen binding to Cr (III) under the basic condition, absorption with a small quantity of weak base NaHCO 3 (pH 8) was car- ried out. Surprisingly, the absorption increased drastically and only a small amount of metal ions was left unabsorbed in the water after treatment. This absorp- tion property may be attributed to the formation of ben- zoate which coordinates with the metal salt, as shown in Figure 4. Encouraged by this result, several salt solu- tions were prepared from their metal sulphates with a concentration of 1 mg/mL and were studied for effi- ciency of the ion exchange under batch and continuous conditions, as shown in Table 1. From this table, it is clear that the batch process is more effective than the continuous process, which may be attributed to a shorter contact time in the continuous process (the flow time is only 2 min and 25 s). After the batch process, the TBBA-incorporated polystyrene flakes were washed with water, dried and analysed with SEM. The surface had an entirely different nature as compared to the film before the absorption (Figure 5). The metal absorption was confirmed with flame photometry studies of the polystyrene film in CH 2 Cl 2 . Several attempts to increase the absorption pro- cess by increasing the pH (up to 10) were not promising as the concentration of Na ions increased in the waste- water. 4 DISCUSSION Though only a few ppm of Cr were present in tannery wastewater, attempts were made to study the efficiency of the TBBA polystyrene (1 g) by employing the solu- tions with different concentrations (10–70 ppm). At a lower concentration the absorption was greater than J. L. L. ANTONI et al.: 4-TERT-BUTYLBENZOIC ACID-INCORPORATED POLYSTYRENE: AN EFFECTIVE ... 488 Materiali in tehnologije / Materials and technology 58 (2024) 4, 485–490 Figure 4: Metal-ion exchange with TBBA polystyrene Figure 3: Proposed structure for the TBBA incorporation in polysty- rene Figure 5: SEM images of 4-tert-butylbenzoic acid-incorporated poly- styrene film after treatment 90 % and it decreased considerably with higher concen- trations. This is attributed to the decrease in the available CO 2 - Na + sites on the surface (Table 2). Table 2: Absorption of Cr (III) by TBBA polystyrene S. No. Initial Cr (III) concentration (ppm) Cr (III) in the treated water (ppm) Absorbed Cr (III) concentra- tion (ppm) 11 019 22 031 7 33 042 6 44 073 3 55 01 04 0 66 01 64 4 With these promising preliminary results, the re- moval of Cr from the secondary treated tannery waste- water was carried out. The preliminary studies were con- ducted to measure the common parameters like pH, TDS, etc., as shown in Table 3. The tannery effluent was turbid with soil particles and several other chemicals. So it was centrifuged to remove the suspended solids and the supernatant was taken for analysis. A systematic analysis showed that the effluent contained several other chemicals in small quantities (Table 2). The pH of the tannery effluent was 8.7 which was enough for the ben- zoate ions to form during the absorption process. The ab- sorption in the tannery wastewater was complex as there were several chemicals that could interact with the poly- mer matrix. Table 3: Common parameters of the secondary treated effluent S. No. Parameters Measured values with units Permissible val- ues for potable water 18 1 pH 8.8 6.5–8.5 2 Electrical con- ductivity 6.32 mmho/cm 800–2500 μS/cm 3 Colour brown colourless 4 Total dissolved solids (TDS) 4260 mg/L 50–150 ppm 5 COD 1470 mg/L 1–2 mg/L 7 Chromium 7.26 mg/L trace 8 Chloride 1730 mg/L 250 mg/L The tannery effluent (100 mL) was being stirred with the flakes of TBBA-incorporated polystyrene (5 g) and 0.1 mmol of NaHCO 3 for 10 minutes (the batch process). The effluent was then decanted and analysed for Cr(III) ions. The analysis clearly showed that the solution con- tained a negligible amount of chromium. The polymer matrix was not selective towards Cr (III) ions. In addi- tion to chromium, other metals like Ca and Mg were also trapped during this process. The study was not complete without studying the leaching of TBBA from the poly- meric matrix. An HPLC chromatogram of the effluent showed that the organic residues in the effluent were not absorbed by the polymeric matrix. From the HPLC stud- ies of the solution, it was clear that TBBA was not leached out from the polymeric matrix during this opera- tion. 5 CONCLUSIONS In conclusion, the absorption of metal ions from wa- ter using a polystyrene matrix that incorporated TBBA was demonstrated. The benzoic acid derivative bound on the surface via a non-covalent hydrophobic interaction. Hence, the hydrophilic carboxylic acid moiety was ex- posed on the surface and could bind with several metals. The ligation was more facile under the basic condition than in a neutral medium. This polymeric matrix was successfully used in both the continuous and batch pro- cesses to remove metal ions. Further, the scope of this process was extended to the removal of chromium ions from the tannery effluent. 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