Industrial heavy metal-contaminated wastewater is one of the main water pollution problems. Adsorbents are a promising method for the removal of heavy metal contaminants. Herein, polyaspartic acid/carboxymethyl poplar sawdust hydrogels (PASP/CMPP) and ascorbic acid/carboxymethyl poplar sawdust hydrogels (VC/CMPP) were prepared by aqueous polymerization using alkalized poplar sawdust (CMPP) as the substrate and PASP and vitamin C (VC) as modifiers. The effective results, provided by the characterization analysis of SEM and BET, indicate that the surface of the PASP/CMPP hydrogel has a larger number of loose pores and a larger pore volume than the VC/CMPP hydrogel. The treatment effects of the two hydrogels on simulated wastewater containing Cd(II) were investigated by a batch of experiments. The results showed that PASP/CMPP had a better adsorption effect than VC/CMPP under the same adsorption conditions. Interestingly, the solid concentration effect was found in the process of sorption kinetics and sorption isotherms. The sorption kinetic curves of Cd(II) on PASP/CMPP were well-fitted by the quasi-second-order kinetics under different adsorbent concentrations. The adsorption conforms to Langmuir and Freundlich adsorption isotherm models. More importantly, PASP/CMPP composites are expected to be used as a new kind of environmental adsorbent for wastewater treatment.

  • Hydrogels of PASP/CMPP were prepared.

  • The hydrogels of PASP/CMPP exhibit enhanced sorption capacities for Cd(II).

  • The hydrogels of PASP/CMPP are potential sorbents for wastewater treatment.

  • The solid concentration effect was found in the process of sorption kinetics and sorption isotherms.

  • The synthesis of PASP/CMPP hydrogels provides a win-win strategy.

Rapid industrialization and improvement of people's living standards have caused many environmental pollution problems. In reality, heavy metal ions usually coexist in environmental and industrial wastewater. Heavy metals in industrial wastewater are one of the major pollutants (Tchounwou et al. 2012; Shafiq et al. 2018; Hefny et al. 2020; Khan et al. 2021; Liu et al. 2022). Untreated sewage is discharged into rivers, lakes, and seas, causing serious deterioration of water quality. Heavy metals are difficult to biodegrade. Among them, cadmium (Cd), a toxic heavy metal, can be enriched in the human body through the biological diffusion effect of the food chain (Amin et al. 2022). Cadmium not only interacts vigorously with proteins, enzymes, and other substances in the human body, making them lose their vitality, but also accumulates in some organs of the human body, leading to slow poisoning and death (Anwar et al. 2010; Verma et al. 2018). Briefly, heavy metal water pollution not only harms human health but also reduces crop yield and quality and accelerates the degradation and destruction of the ecological environment. Heavy metal water pollution prevention and control is an urgent matter (Arumugam & Jongsung 2018; Musa et al. 2020).

To cope with this situation, various water treatment technologies have been explored and applied to the treatment of water pollution. The commonly used treatment methods include absorption, ion exchange, extraction, and membrane chromatography. The adsorption method is superior to other technologies in terms of initial cost, flexibility, design difficulty, operation method, and toxicity (Li et al. 2018; Liu et al. 2019; Musa & Zurina 2020; Shirell et al. 2020; Alharby et al. 2021; Tipplook et al. 2021; Lin et al. 2022). Common adsorbents are active white clay, bleaching powder, diatomaceous earth, and other natural mineral products, as well as active carbon, organic silicon, activated alumina, zeolite molecular sieve, adsorption resin, and humic acid. The use of these adsorbents has been greatly limited due to their limited adsorption capacity or difficult biodegradation.

Recently, hydrogels, as a new adsorbent, have attracted much attention (Alharby et al. 2021; Ma et al. 2021; Rahman & Rimu 2020; Wang et al. 2021; Weerasundara et al. 2021). Hydrogel is a kind of highly hydrophilic three-dimensional (3D) network structure gel (Tie et al. 2022). It expands rapidly in water and can hold a large volume of water without dissolving in this swelling state. Several new types of gels with excellent mechanical properties have been developed, such as topological hydrogels, double-network hydrogels, composite hydrogels, macromolecular microsphere composite hydrogels, hydrophobic association gels, and homogeneous chain hydrogels. Among them, composite hydrogels have attracted extensive attention due to their high strength and diversified composite methods. It is worth noting that the various active functional groups on the gel polymer skeleton and the 3D network structure ensure that more sites are involved in the adsorption process. These advantages of gels make them widely used as adsorbents in the field of environmental protection. The removal of heavy metal ions by hydrogels mainly depends on the presence of a large number of functional groups (such as –OH, –COOH, –NH2, and –SO3H) in hydrogels for adsorption, ion exchange, and chelation of heavy metal ions. The adsorption of heavy metal ions on hydrogels shows the advantages of high adsorption capacity, fast adsorption, and recycling, so the adsorption of heavy metal ions on hydrogels has become a hot spot in recent years (Wang et al. 2020; Kim et al. 2022; Muhammad et al. 2022; Peng et al. 2022; Qiu et al. 2022).

In order to prepare biodegradable and environmentally friendly adsorbents, it is very important to select biodegradable and environmentally friendly raw materials or environmentally friendly preparation methods (Musa et al. 2019; Sabet & Kamran 2019). Poplar is a kind of renewable resource in nature, which contains abundant cellulose and lignin. Cellulose and lignin contain a large number of hydroxyl, carboxyl, and other active functional groups, which play an important role in the process of adsorption (Yu et al. 2000; Abia et al. 2003; Abdić et al. 2018). Polyaspartic acid (PASP) belongs to a group of polyamino acids (Yang et al. 2019). PASP is easily broken by microorganisms and fungi because of the peptide bonds in its structural backbone, and the final degradation products are ammonia, carbon dioxide, and water, which are harmless to the environment (Jv et al. 2019). Therefore, it is widely used (Ye & Wang 2016; Hao & Li 2019). It can be used in water treatment, medicine, agriculture, daily chemical, and other fields. As a new green water treatment agent, it can chelate calcium, magnesium, copper, and other multivalent metal ions. Vitamin C (VC) is a polyhydroxyl compound. The molecular structure of VC has an enediol structure, a lactone ring, and two chiral carbon atoms. Therefore, it is not only active in nature but also has an optical rotation.

In this study, PASP/CMPP hydrogels and VC/CMPP hydrogels were prepared by using glutaraldehyde as a cross-linking agent, and used for the treatment of wastewater containing Cd(II), in order to understand the removal behavior of Cd(II) by hydrogels. Therefore, the main objective is to compare the removal efficiencies and adsorption capacities between PASP/CMPP and VC/CMPP on the adsorption properties of Cd(II).

Reagents

NaOH and KMnO4 were purchased from Tianjin Damao Chemical Pharmacy Factory. PASP, glutaraldehyde, Cd(NO3)2, and VC were purchased from Aladdin Reagent (Shanghai) Co., Ltd, China. Anhydrous ethanol was purchased from Tianjin Kermel Chemical Reagent Co., Ltd, China. Potassium bromide, HNO3, and CH3COOH were purchased from Sinopharm Chemical Reagent Co., Ltd, China. All chemicals were used without further purification. The poplar was collected from the north side of the comprehensive experimental building on the campus of Heze University. Water was purified with a Hitech-Kflow water purification system (Hitech, China).

Preparation of CMPP, PASP/CMPP, and VC/CMPP composites

First, the collected poplar was washed with water to remove the dust and dried in an electric thermostatic air-blowing drying oven. Second, it was pulverized with a pulverizer, sifted through a 100-mesh sieve, and then set aside. Third, 2 g of poplar sawdust was weighed and immersed in 100 mL of 15% NaOH solution for 12 h. Fourth, the mixture was centrifuged, washed, and then transferred to a round-bottom flask. Finally, 20 mL of ethanol and 2 mL of acetic acid were added and the mixture was stirred using a magnetic stirrer for 30 min at room temperature. The final sample obtained is denoted as CMPP.

0.1 g CMPP was weighed and added to 50 mL of 0.06 mol/L KMnO4 solution, and the mixture was stirred using a magnetic stirrer at 50 °C for 15 min. Under the conditions of continuous magnetic stirring at 70 °C for 3.5 h, 1.5 g of PASP and 1 g of glutaraldehyde were measured and added to the above solution. The sample was frozen and lyophilized in a freeze dryer for 72 h. The material obtained after freeze-drying is denoted as the PASP/CMPP hydrogel. For comparison, VC/CMPP was prepared in the same way by substituting PASP for VC.

Characterization

The sample morphology was analyzed using a JSM-6700F scanning electron microscope (SEM, JEOL, Japan) under the conditions of 1 kV acceleration voltage and gold spraying. Fourier transform infrared spectra (FTIR) (Nicolet 5700 Spectrometer, USA) of samples were recorded in the range of 500–3,900 cm−1. The N2 adsorption–desorption isotherms were determined using a Autosorb IQ-MP system (Quantachrome Instruments, USA), and the test samples were degassed at 120 °C for 5 h under vacuum before measurement. The specific surface area (As) and pore volume (Vp) of the samples were calculated using the Brunauer–Emmett–Teller (BET) and Barrett–Joyner–Halenda (BJH) methods, respectively.

Sorption experiments

The heavy metal ion, Cd(II), was used as the target to test the adsorption capacity. The cadmium removal test was carried out at room temperature. The initial concentrations of Cd(II) from 30 to 300 mg/L were prepared by dissolving Cd(NO3)2 in deionized water. A certain amount of adsorbent was weighed and put into a polyethylene tube containing a certain volume of the above solution and oscillated at 150 r/min in a thermostatic oscillator until the specified time. The initial pH values of the solutions were adjusted to 5.5 with 1 mol/L of HCl and 1 mol/L of NaOH solution. Then, an appropriate amount of the solution was filtered through a 0.45-μm filter membrane, and the concentration of cadmium ions present in the filtrate was tested by an atomic absorption spectrophotometer (AAS) (AAS-3600, Shanghai Metash Instruments Co., Ltd, China) equipped with an air-acetylene flame.

In order to investigate the time required to reach adsorption equilibrium, samples were taken at the following times: 5 min,10 min, 15 min, 20 min, 30 min, 40 min, 60 min, 90 min, 2 h, 3 h, and 5 h, respectively. The adsorption amounts (Γt) at different times were calculated as follows:
(1)
where the C0 (mg L−1) is the initial concentration and Ct is the concentration of the solution at time t. Cs (g L−1) is the sorbent dosage.
To ensure sorption equilibrium, the adsorption time (t) was selected as 24 h in the equilibrium sorption tests. The equilibrium adsorption amount (Γe) and the removal efficiency in this study were calculated as follows:
(2)
(3)
where the Ce refers to the concentration of solution at adsorption equilibrium.

The tests shall be conducted three times and the average of overall measurements was taken as the final value, with a relative error less than 5.2%.

Characterizations

SEM analysis

Figure 1 presents the SEM images of samples. As Figure 1(a) shows, there is a lot of interlacing cellulose in poplar. After the reaction of alkalized poplar wood with absolute ethanol and acetic acid, the structure of cellulose in poplar wood changed obviously, and the CMPP appeared granular (Figure 1(b)). The surface of PASP/CMPP hydrogel has a large number of loose pores (Figure 1(c)), while the VC/CMPP hydrogel shows a bulk structure (Figure 1(d)). This indicates that PASP and VC play an important role in the process of gel formation. Although both of them are polyhydroxyl compounds, the presence of PASP makes the samples more porous and loose.
Figure 1

SEM images of the following samples: (a) poplar; (b) CMPP; (c) PASP/CMPP; (d) VC/CMPP.

Figure 1

SEM images of the following samples: (a) poplar; (b) CMPP; (c) PASP/CMPP; (d) VC/CMPP.

Close modal

FTIR analysis

Figure 2 presents FTIR spectra of the following samples: poplar, CMPP, VC/CMPP, PASP/CMPP. Poplar only had a characteristic peak at 1,038 cm−1, which was assigned to O–H bending vibration and C–O–C stretching vibration (Ye & Wang 2016). However, the modified poplar wood showed more characteristic peaks, and the characteristic peaks at 799; 1,410; 1,025; and 1,547 cm−1 were designated as the –OH, –CH, –COOH, and –CH2OH tensile vibrations of CMPP. After CMPP copolymerizes with VC and PASP, the position of each characteristic peak changes significantly. The absorption peaks at 799 and 1,547 cm−1 move to high wave numbers 808 and 1,628 cm−1, respectively. Also, the absorption peaks at 1,025 and 1,410 cm−1 disappear and are replaced by 1,310 and 1,361 cm−1, respectively. In the sample of PASP/CMPP, there are only absorption peaks at 1,398 and 1,548 cm−1. The above results implied that VC and PASP have successfully combined with CMPP.
Figure 2

FTIR spectra of the following samples: poplar; CMPP; VC/CMPP; PASP/CMPP.

Figure 2

FTIR spectra of the following samples: poplar; CMPP; VC/CMPP; PASP/CMPP.

Close modal

BET analysis

Figure 3 shows the N2 adsorption–desorption isotherms of CMPP, VC/CMPP, and PASP/CMPP samples. The surface area (As), average pore size (Dp), and pore volume (Vp) of the samples are listed in Table 1. The specific surface areas of VC/CMPP and PASP/CMPP are 0.54 and 9.96 m2g−1, respectively. The curves of all samples showed that the adsorption line rose gently and the desorption line fell gently. This indicates that the pore structure in the sample is made up of pores, which are formed by plates that are tilted to each other. In addition, the average pore size (Dp) and pore volume (Vp) of samples are 4.37 nm and 0.009 cm3g−1 for PASP/CMPP, and 5.80 nm and 0.0.0008 cm3g−1 for VC/CMPP, respectively. By comparison, it is found that the PASP/CMPP sample has a larger pore volume, which is also conducive to adsorption. What's more, the CMPP sample has a smaller specific surface area and pore volume, which are not conducive to adsorption.
Table 1

Specific surface area, average pore size, and pore volume of samples

SamplesAs (m2/g)Dp (nm)Vp (cm3/g)
PASP/CMPP 9.96 4.37 0.009 
VC/CMPP 0.54 5.80 0.0008 
CMPP 0.30 8.06 0.004 
SamplesAs (m2/g)Dp (nm)Vp (cm3/g)
PASP/CMPP 9.96 4.37 0.009 
VC/CMPP 0.54 5.80 0.0008 
CMPP 0.30 8.06 0.004 
Figure 3

N2 adsorption–desorption isotherms of CMPP, VC/CMPP, and PASP/CMPP samples.

Figure 3

N2 adsorption–desorption isotherms of CMPP, VC/CMPP, and PASP/CMPP samples.

Close modal

The results on Cd(ΙΙ) adsorption

The removal efficiency of CdΙΙ) by different adsorbents of CMPP, VC/CMPP, and PASP/CMPP were investigated at C0 = 50 mg/L, Cs = 1.0 g/L, pH = 5.5, and 25 °C (Figure 4). The removal efficiency of PASP/CMPP was 93.69%, which was the best among the three sorbents for Cd(II) removal. The removal efficiency of CMPP and VC/CMPP were 8.84 and 3.96%, respectively. The specific surface area of PASP/CMPP is the largest among the three, which may be one of the reasons for the highest removal efficiency. Although some pores exist in VC/CMPP hydrogels, they hardly play a role in the adsorption process. Moreover, the addition of VC destroys part of the pore structure in CMPP, and results in the lowest removal effect. The above results are consistent with the results of BET analysis (see Section 3.1.3).
Figure 4

The removal efficiency of Cd(II) by different adsorbents of CMPP, VC/CMPP, and PASP/CMPP samples (C0 = 50 mg/L, Cs = 1.0 g/L, pH = 5.5, and 25 °C).

Figure 4

The removal efficiency of Cd(II) by different adsorbents of CMPP, VC/CMPP, and PASP/CMPP samples (C0 = 50 mg/L, Cs = 1.0 g/L, pH = 5.5, and 25 °C).

Close modal
The solid concentrations are an important factor affecting the adsorption effect (O'Connor & Connolly 1980; Voice & Weber 1985). It is of great theoretical and practical significance to study the effect of sorbent dosage on adsorption performance. Figure 5 shows the sorption kinetic curves and sorption isotherms of PASP/CMPP adsorbing Cd(II) at different solid concentrations under conditions of 25 °C and pH = 5.5. The adsorption results show that the adsorption amount decreases with the increase of the amount of adsorbent. The Cs dependence of the sorption isotherms is a well-known solid (or sorbent concentration) effect (Cs effect) (Zhao & Hou 2012; Zhao et al. 2013).
Figure 5

Cd(II) adsorbed on PASP/CMPP at different sorbent concentrations: (a) sorption kinetics curves and (b) sorption isotherms. (The dots represent experimental data, the solid lines represent Langmuir model fits, and the dashed lines represent Freundlich model fits. 25 °C, pH = 5.5.)

Figure 5

Cd(II) adsorbed on PASP/CMPP at different sorbent concentrations: (a) sorption kinetics curves and (b) sorption isotherms. (The dots represent experimental data, the solid lines represent Langmuir model fits, and the dashed lines represent Freundlich model fits. 25 °C, pH = 5.5.)

Close modal
Langmuir and Freundlich isotherms were used to fit the adsorption data of different Cs values with nonlinear regression. The Langmuir model can be expressed in a nonlinear form as,
(4)
or in a linear form as,
(5)
The Freundlich model can be expressed in a nonlinear form as,
(6)
or in a linear form as,
(7)
The sorption data for the various composites were fitted using the Langmuir and Freundlich isotherms using nonlinear and linear regressions. All of the nonlinear model plots coincided with the experimental data (Figure 5(b)), and the linear model plots were straight lines (Figure 6). Table 2 and Table 3 list the best-fit values of the model parameters, Γm, KL, KF, nF, and R2. Higher R2 values for the various model-fitting plots indicated that the Langmuir and Freundlich models adequately described the sorption isotherms for any given Cs value. Furthermore, Table 2 and Table 3 show that the Γm values decreased with increasing Cs. Similar results were reported in our previous studies (Zhang et al. 2015, 2019, 2021).
Table 2

Nonlinear-fit data of model parameters for Cd(II) sorption on PASP/CMPP at different Cs values

Cs (g/L)Langmuir isotherm
Freundlich isotherm
Γm (mg/g)KL (L/mg)R2KF LnF (mg1−nF/g)nFR2
1.00 56.8 0.168 0.987 22.4 0.175 0.989 
2.00 42.3 0.230 0.903 17.7 0.163 0.988 
4.00 32.5 0.234 0.982 11.3 0.194 0.909 
Cs (g/L)Langmuir isotherm
Freundlich isotherm
Γm (mg/g)KL (L/mg)R2KF LnF (mg1−nF/g)nFR2
1.00 56.8 0.168 0.987 22.4 0.175 0.989 
2.00 42.3 0.230 0.903 17.7 0.163 0.988 
4.00 32.5 0.234 0.982 11.3 0.194 0.909 
Table 3

Linear-fit data of model parameters for Cd(II) sorption on PASP/CMPP at different Cs values

Cs (g/L)Langmuir isotherm
Freundlich isotherm
Γm (mg/g)KL (L/mg)R2KF (LnF·mg1−nF/g)nFR2
1.00 58.6 0.104 0.996 21.2 0.188 0.947 
2.00 42.9 0.176 0.998 16.9 0.176 0.977 
4.00 32.5 0.204 0.999 9.34 0.248 0.809 
Cs (g/L)Langmuir isotherm
Freundlich isotherm
Γm (mg/g)KL (L/mg)R2KF (LnF·mg1−nF/g)nFR2
1.00 58.6 0.104 0.996 21.2 0.188 0.947 
2.00 42.9 0.176 0.998 16.9 0.176 0.977 
4.00 32.5 0.204 0.999 9.34 0.248 0.809 
Figure 6

Linear correlation plots of (a) Langmuir and (b) Freundlich isotherms for Cd(II) sorption on PASP/CMPP at different Cs values.

Figure 6

Linear correlation plots of (a) Langmuir and (b) Freundlich isotherms for Cd(II) sorption on PASP/CMPP at different Cs values.

Close modal
When describing the adsorption phenomenon at the solid–liquid interface, the quasi-first-order rate equation (Ho 2004) and quasi-second-order rate equation (Ho & McKay 1999) can be expressed as the following equations:
(8)
(9)
where k1 (1/h) and k2 (g/(mg·h)) are the quasi-first-order and quasi-second-order rate equation adsorption rate constants, respectively. All of the linear model plots coincided with the experimental data (Figure 7). Table 4 lists the best-fit values of the quasi-first-order rate equation and quasi-second-order rate equation. Higher R2 values for the various model-fitting plots indicated that the quasi-second-order rate equation adequately described the sorption kinetics curves for any given Cs value, which is better than the quasi-first-order rate equation.
Table 4

Quasi-first-order kinetic fit and quasi-second-order kinetic fit data of model parameters for Cd(II) sorption on PASP/CMPP at different Cs values

Cs (g/L)Quasi-first-order kinetic fit
Quasi-second-order kinetic fit
Γe,1(mg/g)k1(min−1)R2Γe,2(mg/g)k2(gmg−1min−1)R2
1.00 19.2 0.0205 0.9783 49.8 0.0027 0.9999 
2.00 3.35 0.0146 0.8289 29.0 0.0166 0.9999 
4.00 1.46 0.0193 0.9647 15.3 0.0469 0.9999 
Cs (g/L)Quasi-first-order kinetic fit
Quasi-second-order kinetic fit
Γe,1(mg/g)k1(min−1)R2Γe,2(mg/g)k2(gmg−1min−1)R2
1.00 19.2 0.0205 0.9783 49.8 0.0027 0.9999 
2.00 3.35 0.0146 0.8289 29.0 0.0166 0.9999 
4.00 1.46 0.0193 0.9647 15.3 0.0469 0.9999 
Figure 7

Cd(II) adsorbed on PASP/CMPP at different sorbent concentrations: (a) quasi-first-order kinetic fitting and (b) quasi-second-order kinetic fitting (25 °C, pH = 5.5).

Figure 7

Cd(II) adsorbed on PASP/CMPP at different sorbent concentrations: (a) quasi-first-order kinetic fitting and (b) quasi-second-order kinetic fitting (25 °C, pH = 5.5).

Close modal

The PASP/CMPP hydrogel was successfully synthesized by using alkalized poplar sawdust (CMPP) as the substrate and PASP as the modifier. The effective results, provided by the characterization analysis of SEM and BET, indicate that the surface of the PASP/CMPP hydrogel has a large number of loose pores and a larger pore volume, which are conducive for adsorption. Under the same adsorption conditions, the adsorption capacity of the PASP/CMPP hydrogel was higher than that of the VC/CMPP hydrogel. The sorption kinetics for Cd(II) follow a pseudo-second-order, and sorption isotherms follow the Langmuir and Freundlich models. There is an obvious effect of solid concentrations on the sorption kinetic curves and sorption isotherms. The PASP/CMPP hydrogel has a promising application in the removal of Cd(II) in water. This research provides insights into the synthesis of an efficient and biodegradable functional adsorbent for the simultaneous removal of heavy metal pollutants in wastewater.

This work is supported financially by the Science and Technology Program for Colleges and Universities of Shandong Province (No. J18KA104).

F.Z. conceived and designed the experiment. She performed the experiments and carried out the data analysis. J.T. and D.H. carried out characterization experiments on the samples. L.W., C.Z., and W.H. have polished the grammar of the manuscript. All authors have read and agreed to the published version of the manuscript.

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

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