Title Science and Technology Indonesia e-ISSN:2580-4391 p-ISSN:2580-4405 Vol. 8, No. 2, April 2023 Research Paper Facile Fabrication of Layered Double Hydroxide-Lignin for Efficient Adsorption of Malachite Green Neza Rahayu Palapa1*, Nur Ahmad2,3, Alfan Wijaya3, Zaqiya Artha Zahara3 1Department of Chemistry, Faculty of Mathematics and Natural Sciences, Universitas Sriwijaya, Ogan Ilir 30662, Indonesia2Graduate School, Faculty of Mathematics and Natural Sciences, Sriwijaya University, Ogan Ilir, 30662, Indonesia3Research Center of Inorganic Materials and Complexes, Faculty of Mathematics and Natural Sciences, Sriwijaya University, Palembang, 30139, Indonesia *Corresponding author: nezarahayu@gmail.com AbstractPreparation of layered double hydroxide-lignin (lignin-Zn/Al) carried out by coprecipitation method. The FTIR spectra of lignin-Zn/Aldisplayed at 3448, 2939, 1620, 1381, 1118, 1041, and 601 cm−1. The characteristic peaks are located at 10.1°, 19.1°, 20.1°, 29.4°, 33.9°,and 60.4°. The lignin-Zn/Al nitrogen adsorption-desorption isotherm showed a Type-IV curve, indicating that it had a mesoporousstructure. The H3 kind of hysteresis loop also provides evidence for the presence of mesopores within the lignin-Zn/Al complex.Lignin-Zn/Al, lignin, and Zn/Al had pHpzc values of 6.09, 3.01, and 6.09, respectively. Lignin-Zn/Al, lignin, and Zn/Al are positivelycharged when the pH of the solution is less than pHpzc, and they are negatively charged when the pH of the solution is more thanpHpzc. The Langmuir and pseudo-second-order model best represented the MG adsorption onto all adsorbents. The lignin-Zn/Al,lignin, and Zn/Al were shown to have maximum Langmuir adsorption capacities of 83.034, 78.740, and 36.364 mg/g, respectively.Zn/Al adsorption capacity increased 2.28 times after being composited with lignin. KeywordsLayered Double Hydroxide, Adsorption, Lignin, Malachite Green Received: 20 January 2023, Accepted: 8 April 2023 https://doi.org/10.26554/sti.2023.8.2.305-311 1. INTRODUCTION The contamination brought on by the wastewater discharge of organic dyes has become a more prominent issue because of the industry’s rapid development (Tang et al., 2022) . In many industries, including papers, tannery, printing inks, clothing, and others, dyes are widely utilized. As a result, a lot of colorful wastewater is produced, and many organic dyes will have a major harmful impact on the environment and human health (Giri et al., 2022; Vigneshwaran et al., 2021). Malachite green (MG), a triphenylmethane cationic dye, is frequently used in the textile industry (Jin et al., 2022) . However, even at low concentrations, MG has been discovered to have numerous toxicological side effects on human bodies, such as mutagenic, teratogenic, and cancerous consequences (Buvaneswari and Singanan, 2022; Sarkar et al., 2021). Several cutting-edge methods, such as extraction (Raval et al., 2022) , photodegradation (Puthukkara et al., 2022) , mem- branes (Iqbal et al., 2022) , oxidation combining ultrasonic and electrochemical (Ren et al., 2021) , and adsorption (Moradi and Panahandeh, 2022) , have been used to remove MG from aqueous medium over the past few decades. Adsorption has garnered the most attention among these due to its straightfor- ward functioning, design flexibility, practical recyclability, and excellent reliability. For the purpose of removing MG from an aqueous solution, numerous sophisticated adsorption materi- als have been developed recently, including Costus woodsonii (Van Tran et al., 2022) , modified metal-organic frameworks (Dahlan et al., 2023) , biowaste garlic peel (Pathania et al., 2022) , and layered double hydroxide (Ahmad et al., 2023a) . Layered double hydroxides (LDHs) are a type of 2D anionic clay that is composed of layers (Nazir et al., 2022) . LDH has a struc- ture similar to brucite with a large surface area, where M(II) is surrounded by six hydroxide ions, for instance, and forms an octahedral array that is connected to form an infinite 2D structure (Ahmed and Mohamed, 2022) . These adsorbents have excellent MG molecule adsorption performance, but for this purpose, sustainable, cost-effective adsorbents made from biomass are still required (Wang et al., 2018) . Also, when compared to several previously described adsorbents, biomass-based adsorbents appear to be more envi- ronmentally friendly, cost-effective, and sustainable (Juleanti et al., 2021) . Designing biomass-derived adsorbents to remove MG from aqueous media is therefore appealing. Lignin, an https://crossmark.crossref.org/dialog/?doi=10.26554/sti.2023.8.2.305-311&domain=pdf https://doi.org/10.26554/sti.2023.8.2.305-311 Palapa et. al. Science and Technology Indonesia, 8 (2023) 305-311 amorphous high-molecular aromatic polymer, is the second most prevalent biomass component on the planet after cellu- lose (Zong et al., 2023) . The pulp and paper industry currently produces about 50 million tons of lignin as a byproduct each year. The vast majority of lignin that has been burned up to this point has been done so to create energy, which has re- sulted in significant lignin resource waste (Du et al., 2023) . The use of inexpensive, readily available industrial waste lignin to produce effective functional materials for environmental re- mediation is a great solution when taking into account greater lignin usage and water remediation (Wang et al., 2022) . A three-dimensional network structure and the abundance of functional groups that include oxygen in lignin give it more potential for functionalization (Hamad et al., 2022) . In this work, the coprecipitation technique was used to pre- pare the lignin-Zn/Al. Many cutting-edge characterization techniques were used to examine the physicochemical charac- teristics of lignin-Zn/Al. Also, the potential of lignin-Zn/Al was examined, as well as its application to simulated textile wastewater. 2. EXPERIMENTAL SECTION 2.1 Materials All chemicals were used without any further purification. Sodium chloride, sodium hydroxide, aluminum nitrate nonahydrate, chloride acid, and zinc nitrate hexahydrate were purchased from Sigma Aldrich and Merck. Lignin and distilled water were purchased from Tokyo Chemical Industry and Brataco, respectively. 2.2 Preparation Lignin-Zn/Al and Characterization Lignin-Zn/Al was prepared by the coprecipitation method. Both 0.25 M aluminum nitrate nonahydrate and 0.75 M zink nitrate hexahydrate were dissolved in 30 mL of distilled water, respectively. The solutions were added sodium hydroxide 2 M to pH 8 and stirred at 70°C for 4 h. Afterward, the Zn/Al added 3 g lignin was under continuous stirring for 3 days, filtered, and dried. The characterization of lignin-ZnAl using Fourier Transfer Infra-Red (FTIR) (Shimadzu), X-Ray Diffractometer (XRD) (Rigaku), and Surface Area Analyzer (Quantachrome). 2.3 Adsorption Process of MG Batch adsorption tests were conducted in a shaker. Investiga- tions were into the effects of temperature (30–60°C), initial dye concentration (60–100 mg/L), contact time (10–180 min), and pHpzc (2–11). Usually, 100 mL of beaker glass was filled with 30 mL of MG solution and 30 mg of lignin-Zn/Al. Liquid aliquots were obtained after adsorption and centrifuged. Then, the supernatant was examined using a UV-Vis spectrophotome- ter set to the maximum wavelength of 617 nm. Equation 1 was used to determine the concentration of MG. q = (C0-C)×V m (1) Where q is adsorption capacity at t time (mg/g); C0 and C are initial concentration and concentration for t time of MG, respectively (mg/L); V is the volume of MG (L); m is the mass of lignin-Zn/Al (g). 3. RESULTS AND DISCUSSION FT-IR spectra of Zn/Al, lignin, and lignin-Zn/Al were pre- sented in Figure 1. The FTIR spectra of lignin-Zn/Al displayed at 3448, 2939, 1620, 1381, 1118, 1041, and 601 cm−1. The stretching vibration of -OH from Zn/Al is responsible for ap- pearing of the broad bandwidth 3448 and 1620 cm−1 (Ahmad et al., 2023b) . The band at 2939 cm−1 is stretching vibration of aliphatic -CH from lignin and the distinctive peak at bandwidth 1381 cm−1 is anion interlayer NO3− from Zn/Al (Zubair et al., 2022) . The peak at 1118 and 1041 cm−1 are ascribable to C-O and C-O-C from lignin, respectively (Sun et al., 2022) . The metal oxide bond vibration is attributed to the band at 601 cm−1 (Chen et al., 2022) . Figure 1. Fourier Transfer Infra-Red Results of Adsorbents The usual Zn/Al XRD pattern can be seen in Figure 2, where the characteristic peaks are located at 10.1° and 20.1°, respectively, and correspond to the basal spacings of d003 and d006, respectively (Yuliasari et al., 2023) . The 101 and 110 planes are responsible for two further linked peaks at 29.4° and 60.4°, respectively. The XRD of the lignin is depicted in Figure 2 and displays the distinctive peak of carbon material at 19.1° and 33.9° (Sturgeon et al., 2014) . The XRD results of the lignin-Zn/Al mixture reveal the presence of distinctive Zn/Al and lignin reflections. When evaluating the lignin-Zn/Al structure, the specific surface area and pore size are important factors. Table 3 quan- titatively displays the lignin-Zn/Al, lignin, and Zn/Al pore’s structure (d), surface area (SBET ), and pore volume (VP). The © 2023 The Authors. Page 306 of 311 Palapa et. al. Science and Technology Indonesia, 8 (2023) 305-311 Table 1. The Surface Area of Adsorbents Adsorbent SBET (m2/g) d (nm) VP (cm3/g) Lignin-Zn/Al 7.125 1.960 0.007 Lignin 4.079 2.255 0.009 Zn/Al 1.968 27.687 0.006 Table 2. Kinetic Data of Adsorbents Pseudo-First-Order Pseudo-Second-Order Adsorbent Qeexp Qecalc k1 R 2 Qecalc k2 R 2 (mg/g) (mg/g) (min−1) (mg/g) (g/mg.min) Lignin-Zn/Al 45.642 17.527 0.024 0.850 47.170 0.002 0.999 Lignin 39.892 29.336 0.036 0.941 44.053 0.002 0.993 Zn/Al 36.148 39.455 0.037 0.995 39.683 0.002 0.996 Figure 2. X-Ray Diffractometer Results of Adsorbents results show that lignin-Zn/Al has an average surface area of 7.125 m2/g and pore sizes of 1.9620 ≈ 2 nm. The surface area of Zn/Al increase after combining with lignin. Our findings demonstrate the presence of mesopores in the lignin-Zn/Al structure, which have IUPAC-recommended diameter ranges of 2–50 nm (Heo et al., 2022) . The N2 adsorption/desorption curves and BJH (Barrett, Joyner, Halenda) pore size distri- butions of lignin-Zn/Al are shown in Figure 2. The lignin- Zn/Al nitrogen adsorption-desorption isotherm, as reported by IUPAC, showed a Type-IV curve, indicating that it had a mesoporous structure. The H3 kind of hysteresis loop also provides evidence for the presence of mesopores within the lignin-Zn/Al complex. The pHpzc of is the point when there is no charge at all. Figure 3. Nitrogen Adsorption-Desorption Results of Adsorbents When the pH of the solution is low, shaking causes H+ to migrate from the solution to the surface of the lignin-Zn/Al, lignin, and Zn/Al, raising the pH. When the solution has a high pH, H+ diffuses into the solution from the surface of lignin- Zn/Al, lignin, and Zn/Al. This reduces the pH of the solution. H+ ions do not migrate at the point where the initial and final pHs meet, indicating that pHpzc is the point of convergence. Lignin-Zn/Al, lignin, and Zn/Al had pHpzc values of 6.09, 3.01, and 6.09, respectively, as illustrated in Figure 4. Lignin- Zn/Al, lignin, and Zn/Al are positively charged when the pH of the solution is less than pHpzc, and they are negatively charged when the pH of the solution is more than pHpzc . Table 2 lists the resulting parameters after the experimental © 2023 The Authors. Page 307 of 311 Palapa et. al. Science and Technology Indonesia, 8 (2023) 305-311 Table 3. Isotherm Data of MG Adsorption Adsorbent T (°C) Freundlich Langmuir n kF R2 Qmax kL R2 Lignin-Zn/Al 30 5.230 1.431 0.828 78.125 0.233 0.994 40 5.959 1.452 0.781 79.365 0.341 0.995 50 7.930 1.490 0.645 83.333 0.723 0.996 60 1.101 1.506 0.668 84.034 1.469 0.999 Lignin 30 1.978 1.228 0.878 67.568 0.076 0.955 40 2.033 1.244 0.882 71.942 0.075 0.917 50 2.439 1.291 0.928 72.464 0.093 0.985 60 2.475 1.309 0.947 78.740 0.102 0.981 Zn/Al 30 0.876 2.037 0.880 23.310 0.121 0.982 40 1.071 1.903 0.763 26.954 0.155 0.954 50 1.388 1.789 0.732 30.675 0.203 0.956 60 1.916 1.684 0.778 36.364 0.342 0.980 Table 4. Several Adsorbents to the Adsorption of MG Adsorbent Qmax (mg/g) References Lignin-Zn/Al 84.034 This study Lignin 78.740 This study Zn/Al 36.364 This study Avena sativa 83 Banerjee et al. (2016) Pine cone 111.1 Kavci (2021) Graphene oxide aminated lignin aerogels 113.5 Chen et al. (2020) Halloysite nanotube 74.95 Altun and Ecevit (2022) Active carbons 58 Hijab et al. (2021) Chitosan-zink oxide 11 Muinde et al. (2020) PACT@𝛾-Fe2O3 62.89 Hasan et al. (2020) Figure 4. pHpzc of Lignin-Zn/Al, Lignin, and Zn/Al Figure 5. Contact Time Between Adsorbents and Adsorbate © 2023 The Authors. Page 308 of 311 Palapa et. al. Science and Technology Indonesia, 8 (2023) 305-311 data are fitted to the kinetics models. The pseudo-second-order equation is the most appropriate one to describe the adsorption kinetics of lignin-Zn/Al, lignin, Zn/Al for MG, as shown by the analysis of correlation coefficients shown in Table 2. All R2 of the pseudo-second-order models are much closer to 1.0 than pseudo-first-order models. This suggests that the process of adsorption involves chemisorption (Rashed et al., 2022) . Isotherm studies were carried out to comprehend the MG adsorption equilibrium distribution between the aqueous and the lignin-Zn/Al, lignin, and Zn/Al phases. Due to their widesp read acceptance and popularity for precisely characterizing ad- sorption processes, the Langmuir and Freundlich models were used to explain the adsorption process in order to achieve that. The parameters obtained after fitting the isotherm research data obtained at various temperatures into these models are shown in Table 3. The Langmuir model best represented the MG adsorption onto all adsorbents, according to the R2 values for the three adsorbents. It follows that monolayer adsorption in nature Meng et al. (2019) would be a more accurate way to characterize the MG solution’s adsorption onto lignin-Zn/Al, lignin, and Zn/Al. The lignin-Zn/Al, lignin, and Zn/Al were shown to have maximum Langmuir adsorption capacities of 83.034, 78.740, and 36.364 mg/g, respectively. Zn/Al ad- sorption capacity increased 2.28 times after being composited with lignin. Several adsorbents for the adsorption of MG are displayed in Table 4. 4. CONCLUSION Preparation lignin-Zn/Al is successful by the coprecipitation method. The characterization by FTIR, XRD, and BET shows the physicochemical characteristics of lignin-Zn/Al. The ad- sorption process showed better results after Zn/Al and lignin were combined. This can be seen from the increase in the ad- sorption capacity of Zn/Al lignin by 2.28 times. Thus, lignin- Zn/Al can be one of the adsorbents for the malachite green adsorption process. 5. ACKNOWLEDGMENT The authors acknowledge to Research Center of Inorganic Materials and Complexes, FMIPA Universitas Sriwijaya for the support of this work. REFERENCES Ahmad, N., F. S. Arsyad, I. Royani, and A. Lesbani (2023a). Charcoal Activated as Template Mg/Al Layered Double Hy- droxide for Selective Adsorption of Direct Yellow on Anionic Dyes. Results in Chemistry, 5(1); 100766 Ahmad, N., F. S. Arsyad, I. Royani, P. M. S. B. N. Siregar, T. Taher, and A. Lesbani (2023b). 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Page 311 of 311 INTRODUCTION EXPERIMENTAL SECTION Materials Preparation Lignin-Zn/Al and Characterization Adsorption Process of MG RESULTS AND DISCUSSION CONCLUSION ACKNOWLEDGMENT