Abstract

Developing bio-based adsorbents for efficient removal of heavy metal ions from water has attracted increasing attention due to their abundance, low cost, and sustainability. However, most of these adsorbents are in powdered or granular forms, suffering from difficult regeneration and poor recyclability. Here, we report a highly porous three-dimensional amino-functionalized wood aerogel for efficient heavy metal adsorption. The amino-functionalized wood aerogel was prepared from natural balsa wood via a delignification treatment, followed by TEMPO-mediated oxidation of the delignified wood and then grafting polyethylenimine (PEI) onto the oxidized cellulose skeleton. The obtained amino-functionalized wood aerogel possessed a unique porous lamellar structure with a low bulk density of 77.2 mg/cm3 and high porosity of 94.9%. Benefiting from its high porosity and the introduced amino groups on the cellulose skeleton, the amino-functionalized wood aerogel exhibited a maximum Cu(II) adsorption capacity of 59.8 mg·g−1, which was significantly higher than those of the TEMPO-oxidized wood aerogel and natural balsa wood. The adsorption process can be well described by the pseudo-second-order and Langmuir isotherm models, indicating that the Cu(II) adsorption by the PEI@wood aerogel was dominated by a monolayer chemisorption process. The developed amino-functionalized wood aerogel provides new insights for the design of efficient and low-cost monolithic absorbents for heavy metal remediation.

1. Introduction

Heavy metal ions (e.g., Cu(II), Pb(II), and Cd(II)) discharged from industrial wastewater have become one of the major sources of water pollution worldwide, causing harmful impacts on the water environment and human health due to their high toxicity and nondegradability [1]. To date, various approaches, including ion exchange, membrane filtration, chemical precipitation, flocculation, bioremediation, and adsorption, have been adopted to remove heavy metal ions from wastewater [2]. Among these methods, adsorption is considered as one of the most promising approaches due to its advantages of low cost, high efficiency, and simple operation [3, 4]. Some commonly used adsorbents, such as activated carbon, clay, synthetic polymers, and metal oxides, suffer from low adsorption capacity, high cost, and nondegradability, making them less attractive in practical applications [5]. Bio-based adsorbents, including sawdust, bark, straw, and cellulose, have attracted increasing interest as cheap and sustainable alternatives in wastewater treatment due to their abundance, low cost, and ecofriendliness [6, 7]. However, most of these adsorbents are in powdered or granular forms, often causing separation and reuse difficulties in actual wastewater treatment. Therefore, developing monolithic adsorbents based on low-cost biomass resources for efficient heavy metal ion removal is highly desirable given their easy separation and recovery in the practical application.

As a renewable, sustainable, and ecofriendly natural material, wood represents a 3D hierarchical structure composed of numerous aligned hollow fibers along its growth direction. The hydrophilic and porous structure (e.g., tracheids, vessels, and pits) of natural wood provides multichannels for water and ion transport to support photosynthesis and transpiration in living trees [8]. Meanwhile, the main cell wall components of wood (i.e., cellulose, hemicelluloses, and lignin) contain a large number of functional groups (e.g., hydroxyl and carboxyl groups) that have the potential to be further functionalized to introduce metal-binding sites [9]. However, the natural wood lacks strong binding sites for heavy metal ions, resulting in limited adsorption capacity. Recently, bulk beech wood was functionalized with carboxyl groups (−COOH) by esterification using anhydrides as a bioadsorbent for the remediation of copper ions from water [10]. The COOH-modified wood adsorbent could remove up to 95% of copper ions from low-concentration aqueous solutions. However, the poor accessibility of carboxyl groups located deep inside the wood cell walls limits the adsorption capacity of the modified beech wood. Therefore, it is necessary to increase the wood porosity and introduce more efficient functional groups to improve the adsorption capacity of natural wood toward heavy metal ions.

In this study, we developed a highly porous three-dimensional amino-functionalized wood aerogel as an efficient bioadsorbent for copper (II) removal. The natural balsa wood was first delignified to remove lignin and hemicelluloses from the cell walls to enhance the porosity and specific surface area of the wood scaffold, thus increasing the contact area between adsorbents and heavy metal ions. In a subsequent step, the cellulose skeleton of the wood scaffold was oxidized to introduce carboxyl groups using the TEMPO/NaClO/NaBr system and polyethylenimine (PEI) was then grafted onto the oxidized cellulose skeleton to introduce amino groups, which could serve as strong binding sites for chelating copper ions in aqueous solutions. The structure, morphology, chemical composition, and Cu(II) adsorption capacity of the amino-functionalized wood aerogel were investigated. Moreover, the adsorption mechanism was explored by adsorption kinetics and isotherm models. The proposed strategy opens up a new avenue for developing cost-effective wood-based monolithic absorbents for heavy metal remediation.

2. Materials and Methods

2.1. Materials

Balsa wood (Ochroma pyramidale) was cut into samples with the dimension of (). Sodium chlorite (NaClO2) (80%), acetic acid, sodium hydroxide (NaOH), hydrochloric acid (HCl) (37%), sodium bromide (NaBr), sodium hypochlorite (NaClO), 2,2,6,6-teramethyl-1-piperdinyloxy radical (TEMPO), polyethylenimine (PEI) (molecular weight of 75000 Da), n-hydroxysuccinimide (NHS), 1-ethyl-3 (3-dimethylaminopropyl) carbodiimide hydrochloride (EDC), and copper sulfate pentahydrate (CuSO4·5H2O) were purchased from Aladdin Chemistry Co. Ltd. (Shanghai, China). All of the chemicals were used as received without further purification. Deionized (DI) water was used throughout the experiments.

2.2. Preparation of Delignified Wood Scaffold

Wood aerogel was prepared according to our previously reported method [11]. Briefly, the balsa wood samples were first treated with an aqueous solution of 2 wt% NaClO2 buffered with acetic acid at pH 4.6 for 6 h at 80°C for the removal of lignin. The delignified wood samples were then transferred into an aqueous solution of 8 wt% NaOH and kept at 80°C for 8 h to further remove hemicelluloses. Finally, the samples were carefully rinsed with DI water to remove the chemical residues and stored in DI water.

2.3. Preparation of PEI@Wood Aerogel

To graft PEI onto the cellulose skeleton, the as-prepared delignified wood scaffold was oxidized using the TEMPO/NaClO/NaBr system to introduce carboxyl groups. Typically, the delignified wood samples (10 g) were immersed in 200 ml of aqueous solution containing 0.2 g of TEMPO and 1.5 g of NaBr. Then, 80 ml of NaClO solution was added dropwise to the solution to initiate the oxidization reaction. The pH value of the solution was maintained at 10.0 by adding 0.1 M NaOH. The reaction was terminated after 8 h by adding 0.5 M HCl to adjust the pH value to neutral. The resulting TEMPO-oxidized wood scaffolds were then washed with DI water for subsequent PEI grafting. Specifically, the TEMPO-oxidized samples (10 g) were soaked in 30 ml of aqueous solution containing 15 wt% of branched PEI for 12 h. Then, the soaked samples were transferred into an aqueous solution containing 500 mg of NHS and 500 mg of EDC and kept for 8 h at room temperature to initiate the amidation reaction. The obtained samples were washed three times with DI water and freeze dried at −56°C for 36 h using a freeze dryer (Scientz-10N, Ningbo Scientz Biotechnology Co. Ltd., China), resulting in the formation of amino-functionalized wood aerogel (PEI@wood aerogel). The TEMPO-oxidized wood aerogels were also prepared by freeze drying for comparison.

2.4. Characterization

The surface morphology and structure of the samples were examined by field emission scanning electron microscopy (Hitachi SU-8010, Tokyo, Japan) equipped with an energy-dispersive X-ray spectroscopic detector for mapping. Fourier transform infrared (FT-IR) spectra were recorded on a Nicolet 6700 spectrometer (Thermo Scientific, Waltham, MA, USA) equipped with an ATR module over the scan range of 400–4000 cm−1. The X-ray photoelectron spectroscopy (XPS) measurements were performed on a Thermo ESCALAB 250Xi spectrometer (Thermo Scientific, USA) with a monochromatic Al Kα X-ray source. The specific surface area was calculated using the Brunauer-Emmett-Teller (BET) method by a nitrogen adsorption apparatus (ASAP 2460, USA). The concentration of Cu(II) in the aqueous solutions was determined by ICP-MS (Agilent 7500ce, USA).

The apparent density () of the sample was determined from the ratios of mass to volume and calculated according to the following equation: where (g) and (cm3) represent the mass and volume of the sample, respectively. The porosity of the sample was calculated according to the following equation: where represents the cell wall density (1.5 g·cm−3).

2.5. Adsorption Experiment

The Cu(II) adsorption experiments were conducted at room temperature. Firstly, an aqueous solution of Cu(II) with a concentration of 200 ppm was prepared using CuSO4·5H2O and the initial pH of the solution was controlled at 5.0. Then, the wood aerogel adsorbents were soaked in the solution for 12 h until the color of the sample turned dark blue. After adsorption, the Cu(II) concentrations of the solution were measured by ICP-MS and the Cu(II) adsorption capacity was calculated using the following equation: where (mg·l−1) and (mg·l−1) represent the Cu(II) concentrations in the initial and after adsorption, respectively; (mg·g−1) represents the equilibrium adsorption amount, (l) is the volume of the solution, and (g) represents the dosage of the adsorbents.

2.5.1. Adsorption Kinetics Study

50 mg wood aerogel adsorbents were immersed in 50 ml Cu(II) solutions with a concentration of 150 ppm until the adsorption reached equilibrium. The initial pH of the solution was controlled at 5.0. At a predetermined time interval, the solution was collected to determine its Cu(II) concentration by ICP-MS. The adsorption data were fitted using the pseudo-first-order and the pseudo-second-order models as follows: where (mg·g−1) and (mg·g−1) represent the Cu(II) adsorption capacity at the equilibrium and time (min), respectively, and (min−1) and (g·mg−1·min−1) are the rate constants for the pseudo-first-order pseudo-second-order equations, respectively.

2.5.2. Adsorption Isotherm Study

50 mg wood aerogel adsorbents were immersed in 50 ml Cu(II) solutions with a concentration ranging from 20 to 200 ppm to study the adsorption isotherm. The adsorption experiments were carried out at room temperature with an initial pH of 5.0. The Cu(II) adsorption behavior was described by Langmuir and Freundlich isotherm models as follows: where (mg·g−1) and (mg·g−1) represent the equilibrium and the maximum adsorption of samples, respectively, (mg·l−1) is the equilibrium concentration of Cu(II), and (l·mg−1) is the Langmuir constant. (g·mg−1) is the Freundlich constant and represents the empirical parameter.

3. Results and Discussion

3.1. Preparation and Characterization

The preparation process of the PEI@wood aerogel is illustrated in Figure 1(a). Natural balsa wood was used as starting materials to prepare the aerogel due to its low density (~220 mg·cm−3) and high porosity (~85.6%). To further enhance the porosity and specific surface area of the natural wood, lignin and hemicelluloses were removed from the cell walls by the aqueous solutions of NaClO2 and NaOH, respectively. To improve the affinity of the natural wood towards heavy metal ions, the cellulose skeleton of the delignified wood was oxidized to introduce carboxyl groups via TEMPO-mediated oxidation. PEI was then grafted onto the cellulose skeleton via an amidation reaction of the introduced carboxyl groups with the amino groups of PEI [12]. The grafted PEI within the wood aerogel possesses large amounts of amino groups, which are expected to provide strong binding sites for Cu(II) adsorption.

The morphologies and structures of the natural wood, TEMPO-oxidized wood aerogel, and PEI@wood aerogel are shown in Figures 1(b)1(d). The natural balsa wood has a honeycomb-like porous structure with thin cell walls. After chemical treatment and TEMPO oxidation, the natural wood changed its color from yellowish to white and the original honeycomb-like porous structure evolved into a lamellar structure (Figures 1(b) and 1(c)). This unique architecture was formed by the breakage of the thin cell walls during the chemical treatment and the eventual release of the broken cell walls during the freeze drying process [11]. Due to the removal of the cell wall matrix, the TEMPO-oxidized wood aerogel exhibited a low density of ~58.1 mg·cm−3, high porosity of ~96.1%, and high BET surface area of ~17.3 m2·g−1 (Table 1). The aligned cellulose nanofibers in the cell walls were fully exposed after the removal of cell wall matrix, which was beneficial for the subsequent functional modification. After grafting with PEI, the lamellar structure of the PEI@wood aerogel was well preserved and the color of the wood aerogel was changed from white to yellow (Figure 1(d)). Note that the density, porosity, and BET surface area of the wood aerogel varied slightly after PEI grafting. Energy dispersive X-ray spectroscopy (EDX) analyses were performed to examine the distribution of PEI within the wood aerogel. Elemental mapping images of the PEI@wood aerogel revealed the uniform distribution of nitrogen (green) on both cross and radial sections, indicating that PEI was successfully grafted onto the cellulose skeleton of the wood aerogel (Figures 1(e) and 1(f)).

FT-IR analysis was performed to confirm the compositional changes in the wood samples subjected to different chemical treatments. Figure 2(a) shows the FT-IR spectra of the natural wood, wood aerogel, TEMPO-oxidized wood aerogel, and PEI@wood aerogel. The characteristic peaks of lignin at 1462, 1505, and 1593 cm−1 and hemicelluloses at 1235 and 1736 cm−1 in the FT-IR spectrum of the wood aerogel vanished after the chemical treatment, confirming the successful removal of lignin and hemicelluloses from the wood cell walls [11]. After TEMPO oxidation, the TEMPO-oxidized wood aerogel showed two distinct and intense peaks at 1400 cm−1 and 1600 cm−1, indicating that the primary hydroxyl groups of cellulose skeleton were successfully oxidized into carboxylic groups [13, 14]. After further grafting with PEI, new characteristic peaks appeared at 1460 cm−1 and 1642 cm−1 in the spectrum of the PEI@wood aerogel, which can be associated with the formation of amide bond (−NH−CO−) [12]. Besides, the intensity of the peak at 815 cm−1 increased, which is assigned to the N-H wagging vibration of −NH2 [15]. All these results demonstrated that PEI was successfully grafted onto the cellulose skeleton of the wood aerogel.

The surface compositional changes of the wood samples were further analyzed by XPS. As shown in Figure 2(b), the XPS spectra of the natural wood and TEMPO-oxidized wood aerogel show two characteristic peaks of 1s and 1s and the ratio was increased after TEMPO oxidation. After grafting with PEI, the binding energy peaks of 1s at 397–403 eV appeared in the spectrum of PEI@wood aerogel, further confirming the successful introduction of PEI into the wood aerogel. The deconvolution of the narrow 1s peak revealed three splitting peaks of binding energy at 398.78, 399.46, and 401.09 eV, which could be assigned to the primary amino, secondary amino, and tertiary amino groups, respectively (Figure 2(c)) [16].

3.2. Cu(II) Adsorption Experiments

We compared the adsorption capacity of the natural wood, TEMPO-oxidized wood aerogel, and PEI@wood aerogel for Cu(II). As shown in Figure 3(a), the natural wood exhibited a poor Cu(II) adsorption capacity of only 4.1 mg·g−1 due to its compact cell wall structure and limited chelating ability of hydroxyl groups towards Cu(II). The delignification and TEMPO oxidation treatment resulted in a higher Cu(II) adsorption capacity (15.0 mg·g−1) of the TEMPO-oxidized wood aerogel. This might be attributed to the increased porosity and specific surface area of the wood aerogel, allowing full infiltration of the Cu(II) solution into the porous structure of wood, which enhanced the accessibility of Cu(II) to the binding sites of the adsorbent. On the other hand, the carboxyl groups formed on the cellulose skeleton during TEMPO oxidation could absorb Cu(II) in the solution due to the electrostatic attraction effect. In contrast, the PEI@wood aerogel exhibited a high Cu(II) adsorption capacity of 48.4 mg·g−1, which can be attributed to the large amounts of amino groups introduced after PEI grafting, providing more binding sites for Cu(II) adsorption. Figure 3(b) shows that when a small piece of PEI@wood aerogel was placed in the Cu(II) solution, it rapidly absorbed the Cu(II) in the solution and gradually turned dark-blue, indicating its desirable adsorption performance, which is better than that of the previously reported COOH-modified beech wood [10]. The interaction between amino groups and Cu(II) was investigated by FT-IR. As shown in Figure 3(c), a new intense peak appeared at 620 cm−1 in the spectrum of the PEI@wood aerogel after Cu(II) adsorption, which might be attributed to the complexation between amino groups and Cu(II) [17]. In addition, the peaks at 1642 cm−1 assigned to N-H bending vibration disappeared, further indicating the chelation of Cu(II) to the amino groups.

The initial pH of the Cu(II) solution has a critical effect on the adsorption performance of the adsorbents. Figure 3(d) shows the Cu(II) adsorption capacity of the PEI@wood aerogel at different pH levels. When the pH was low, the high H+ concentration caused strong electrostatic repulsive force between positively charged PEI and copper ions, leading to a low adsorption capacity [18]. With an increase of pH value from 3.0 to 5.0, the Cu(II) adsorption capacity of the wood aerogel demonstrated a rapid rising trend. This phenomenon could be attributed to the deprotonation of the amino groups with increasing pH, which facilitates the formation of chelates between amino groups and copper ions. However, when the initial pH was increased to 6.0, the Cu(II) adsorption capacity decreased dramatically due to the precipitation of copper ions forming Cu(OH)2 [17]. Therefore, the initial pH of 5.0 could be regarded as the optimal pH for Cu(II) adsorption.

To further evaluate the adsorption process of Cu(II) by the adsorbents, the adsorption kinetics was investigated at a constant pH value of 5.0 under room temperature. Figure 4(a) shows the equilibrium adsorption capacity of the PEI@wood aerogel for Cu(II) as a function of adsorption time. It can be seen that the adsorption efficiency increased rapidly at the beginning 6 h of the experiment due to the large numbers of binding sites (amino and carboxyl groups) on the surface of the PEI@wood aerogel for Cu(II) adsorption. The adsorption capacity tended to be stabilized and reached equilibrium after 10 h, indicating that adsorption sites were almost saturated.

Both the pseudo-first-order and pseudo-second-order kinetic models were used to fit the experimental data, and the fitting results and kinetic parameters are shown in Figure 4(a) and Table 2. The linear correlation coefficient () values for the pseudo-first-order and pseudo-second-order kinetic models are 0.9560 and 0.9921, respectively. The fitting results suggested that the adsorption process of the PEI@wood aerogel for Cu(II) could be better described by the pseudo-second-order kinetic model, indicating that the adsorption process was dominated by chemical adsorption. For the synthesized PEI@wood aerogel, the abundant amino and carboxyl groups on the cellulose skeleton could capture Cu(II) effectively via surface complexation and electrostatic interactions [19, 20].

To reveal the interactions between the adsorbent and adsorbate, as well as the theoretical maximum adsorption capacity of the PEI@wood aerogel for Cu(II) [21], we investigated the effect of initial Cu(II) concentration on the equilibrium adsorption capacity of the PEI@wood aerogel. Clearly, the equilibrium adsorption capacity increased rapidly at low Cu(II) concentration and then increased slowly when the concentration was above 100 ppm. The adsorption process was further fitted using the Langmuir and Freundlich isotherm models, and the fittings results and isotherm parameters are shown in Figure 4(b) and Table 3. Obviously, the Langmuir isotherm model better described the adsorption data with a higher correlation coefficient (), demonstrating that the adsorption sites were homogeneously distributed in the PEI@wood aerogel and the adsorption was a monolayer sorption process [22]. The Langmuir isotherm model was also used to calculate the maximum adsorption capacity of the PEI@wood aerogel for Cu(II), yielding a value of 59.8 mg·g−1, which exceeds the experimental value of 48.4 mg·g−1.

4. Conclusions

In summary, highly porous 3D amino-functionalized wood aerogel for Cu(II) adsorption was prepared from natural balsa wood by delignification treatment and subsequent grafting of PEI onto the cellulose skeleton of the wood aerogel. The as-prepared PEI@wood aerogel possessed a unique porous lamellar structure with a low bulk density (77.2 mg·cm−3) and high porosity (94.9%). The introduced amino groups of PEI serve as the predominant active sites for Cu(II) adsorption, and the maximum adsorption capacity of the PEI@wood aerogel for Cu(II) was calculated to be 59.8 mg·g−1 based on the Langmuir isotherm model. The adsorption kinetics follows the pseudo-second-order model, and the adsorption process was dominated by chemical adsorption. The Langmuir isotherm model fits the adsorption data better than Freundlich model, suggesting that the Cu(II) adsorption by the PEI@wood aerogel was a monolayer adsorption process. This study provides a novel strategy for developing low-cost, efficient, and eco-friendly monolithic absorbents based on natural wood for removal of heavy metal ions from wastewater.

Data Availability

The data used to support the findings of this study are available from the corresponding author upon request.

Conflicts of Interest

The authors declare no conflict of interest.

Acknowledgments

This work was financially supported by the Fundamental Research Funds for the Central Non-profit Research Institution of CAF (CAFYBB2020QA004).