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The influence of crystalline structure of cellulose in chitosan-based biocomposites on removal of Ca(II), Mg(II), Fe(III) ion in aqueous solutions

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  • 14.05.2021
  • Original Research
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Abstract

Der Artikel untersucht die Auswirkungen der kristallinen Struktur von Cellulose in Chitosan-basierten Biokompositen auf die Entfernung von Ca (II), Mg (II) und Fe (III) -Ionen aus wässrigen Lösungen. Es wird der Mercerisierungsprozess zur Umwandlung von Cellulose I in Cellulose II und seine Auswirkungen auf Partikelgröße und Kristallinität diskutiert. Die Studie umfasst experimentelle Methoden wie Röntgenbeugung, Partikelgrößenanalyse und Atomabsorptionsspektroskopie, um die Adsorptionseigenschaften verschiedener Cellulose-Chitosan-Verbundstoffe zu analysieren. Die Ergebnisse zeigen, dass Verbundwerkstoffe mit nanometrischer Cellulose II die höchste Adsorptionseffizienz aufweisen, was die Bedeutung der polymorphen Form und Partikelgröße von Cellulose für die Adsorptionseigenschaften unterstreicht. Der Artikel enthält auch FTIR-Analysen und Benetzbarkeitsstudien, die ein umfassendes Verständnis des Adsorptionsmechanismus und des Einflusses der Zellulosestruktur auf die Verbundleistung liefern.

Supplementary Information

The online version contains supplementary material available at https://doi.org/10.1007/s10570-021-03899-3.

Publisher's Note

Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Introduction

Metal contamination of the environment is a serious problem because metals can be toxic, even in small amounts. Moreover, metals are non-biodegradable, they accumulate in living organisms and pose a great threat to health and life (Crini 2005).
Even metals such as magnesium and calcium, which are moved into the groundwater together with fertilizers, can limit the adsorption of other, needful elements. Thanks to water treatment processes it is possible to decrease the amount of Ca(II), Mg(II), and Fe(III) ion in water. However, diverse composition of industrial wastewater requires a variety of treatment methods, e.g. precipitation, oxidation and reduction, filtration, centrifugation, reverse osmosis, sedimentation, solvent extraction, evaporation, reverse osmosis flotation, electro-chemical removal, evaporative recovery, adsorption, etc. (Chong and Volesky 1995; Bhattacharyya and Gupta 2008; Mahvi 2008; Peijnenburg et al. 2015). Also ion exchange and sorption methods are eagerly used. The adsorption process is considered as one of the best water treatment methods due to the wide availability of different types of adsorbents. Popular adsorbents include: activated carbon (Hu et al. 2003), zeolites (Bosso and Enzweiler 2002), clays (Abollino et al. 2003), silica (Ghoul et al. 2003), biomass (Loukidou et al. 2003).
Unfortunately, it should be emphasized that main limitation of sorption methods is economic, due to high costs of adsorbents, as well as high costs of the sorbent regeneration process (Cestari et al. 2004; Alade et al. 2012). Thus, newly developed adsorbent should be not only effective but also relatively cheap.
There are some biopolymers such as chitin, chitosan, sodium alginate that are characterized by good adsorption of heavy metals. A particularly interesting biopolymer is chitosan, which is a biodegradable, biocompatible, and antibacterial material. There are many reports reporting its application for sorption of various metals, e.g. Cr(VI) (Aydin and Aksoy 2009), Pb(II) (Leusch et al. 1995), Cu(II) (Negm et al. 2015), Hg(II) (Allouche et al. 2014), Cd(II) (Kyzas et al. 2014), Ni(II) (Heidari et al. 2013), Zn(II) (Milosavljevic et al. 2011), Co(II) (Minamisawaa et al. 1999), Mn(II) (Al-Wakeel et al. 2015). Sorption properties are a result of the formation of coordination bonds between amine groups of chitosan and heavy metal ion. It has been shown that the sorption activity of chitosan depends on the degree of crystallinity, the degree of deacetylation, and the content of amine groups. However, membranes made from pure chitosan are very brittle (Chatterjee et al. 2009), have low acid resistance (Zhou et al. 2009), low thermal stability (Cirini and Badot 2008), as well as low porosity and specific surface (Vakili et al. 2014). To eliminate these drawbacks and increase the efficiency of metal ion binding, a number of chemical or physical modifications of chitosan were carried out (Yang and Yuan 2001; Zhang and Chen 2002; Varma et al. 2004; Crini 2005; Bhatnagar and Sillanpaa 2009; Miretzky and Cirelli 2009; Boamah et al. 2015; Kumar et al. 2019).
Methods of chemical modification rely mainly on grafting and cross-linking reactions. Since cross-linking agents form covalent bonds with amine groups in chitosan the effect of this type of modification is an increase in the mechanical strength and chemical stability of chitosan membranes (Guibal 2004). Another method to increase sorption capacity is functionalization of chitosan by introducing new functional groups (Jayakumar et al. 2005; Vakili et al. 2014). Modification of chitosan properties can also be obtained by adding plasticizing compounds, e.g. polyethylene glycol, polyvinylpyrrolidone (Zeng and Fang 2004).
Recently, adsorption of heavy metals and dyes from wastewater with use of chitosan composites have aroused great interest. To date, many different fillers have been used, such as silica (Kalapathy et al. 2000), montmorillonite (Wang and Wang 2007), and kaolinite (Zhu et al. 2010). The introduction of fillers often results in increased porosity, specific surface, swelling and diffusivity (Zhang et al. 2016). Vijaya et al. (2008) dealt with the removal of Ni(II) ion using chitosan coated calcium alginate and chitosan coated silica. Also Ghaee et al. (2010) noted that increasing the silica content in chitosan resulted in increased porosity and at the same time copper ion adsorption efficiency. There are several work in which chitosan and perlite composites were used to adsorb metals such as Co(II), Cu(II), and Ni(II) (Kalyani et al. 2009). Composites of chitosan and cotton that were reported to remove Au(II), Pb(II), Ni(II), Cd(II), and Cu(II), too (Zhang et al. 2008; Qu et al. 2009).
Particularly interesting material in terms of production of adsorbents is cellulose, a biopolymer containing β-1,4 glycosidic linked D-glucose units. It is insoluble in water and organic solvents that has a large number of functional groups, enabling its functionalization. There are several studies that used cellulose immobilization on chitosan. Sun et al. (2009) observed that the adsorption efficiency of chitosan was almost three times higher than that of chitosan and cellulose composite systems, although the polymer composite was more stable. Li and Bai (2005) noted that the crosslinking reaction between chitosan and cellulose improves acid resistance. Urbina et al. (2018) obtained chitosan membranes with bacterial cellulose for removing copper ion from aqueous wastewater. They found that composites had better mechanical properties as well as greater copper ion removal efficiency. Vinodhini et al. (2017) proved that a higher content of chitosan in chitosan/cellulose acetate material is responsible for achieving greater efficiency in removing metal ion, what is a result of higher content of amorphous phase.
Our previous research has shown that the mechanical properties of chitosan/cellulose composites depend on the content of the nanometer fraction of fillers. As a result of the design and synthesis of ionic liquids and their use for cellulose modification, it is possible to obtain composite materials with controllable strength properties, e.g. composites with high elasticity and at the same time high breaking stress (Grząbka-Zasadzińska et al. 2019). These strength characteristics are extremely important in terms of designing new adsorbents.
The most popular polymorphic form of cellulose is so called native cellulose (cellulose I). However, some chemical processes, like mercerization, are known to be responsible for change of polymorphic from of cellulose I into cellulose II. The dissimilarity of cellulose II may exert a beneficial effect on some properties of fillers. It is known that the mechanical, dispersive, and morphological properties of composites are related to the polymorphic form of the cellulosic filler (Grząbka-Zasadzińska et al. 2018). We have shown many times, that the type of cellulose polymorph is a factor that not only determines the mechanical properties of composites, but also affects the supermolecular structure, morphology, phase transformation processes and topography of polymer composites (Borysiak 2012, 2013a).
The main purpose of this work was to analyze the influence of polymorphic form of cellulose and its particle size in chitosan matrix on the effectiveness of selected metal ion removal. To the best of our knowledge, these relationships have not yet been studied. Analysis of these issues is important to understand the relationship between supermolecular structure and the adsorption and mechanical properties of composite materials. This relationship is also believed to help to understand the mechanism of the adsorption process in biocomposites.

Experimental

Materials

Two types of cellulose were used in this work – Avicel PH-101 and Arbocel UFC 100 BRIGHT. Avicel PH-101 was purchased from Sigma-Aldrich and Arbocel UFC 100 BRIGHT was supplied by J. Rettenmaier and Söhne. High molecular weight chitosan from crab shells (degree of deacetylation 75–85%) was purchased from Sigma-Aldrich. Pure sodium hydroxide, provided by Chempur, was used for preparation of 16% solution and subsequently used as mercerizing agent. Acetic acid 80%, purchased from POCH S.A., was diluted to 2% (v/v) solution and used for composite formation.
Salts (Ca(NO3)2 · 4H2O, Mg(NO3)2 · 6H2O, FeCl3 · 6H2O) used to prepare of aqueous solution of Ca(II), Mg(II) and Fe(III), respectively, were purchased from Avantor Performance Materials. Nitric acid and standard solutions of metals for AAS determination were purchased from Sigma-Aldrich. Native cellulose materials, before mercerization process, were named accordingly: Avicel PH-101 as cellulose I (C I) and Arbocel UFC 100 BRIGHT as nanocellulose I (CNC I).

Chemical modification of cellulose

Cellulose I was treated with 16% NaOH at room temperature. After 5 min of continuous stirring an excess of water was added to stop the mercerization process. The suspension was centrifuged at 10,000 rpm for 10 min. Finally, the produced cellulose II (C II) was washed with the excess of distilled water to remove NaOH and then dried in the air at 70 °C for 6 h. The same mercerization procedure was carried out for nanocellulose I. In result material named CNC II was obtained.

Preparation of cellulose/chitosan composites

Chitosan/(nano)cellulose composites were produced by solvent casting method. Firstly, chitosan was dissolved in 2% (v/v) CH3COOH. Secondly, suspension of (nano)cellulose (5% (w/w) of filler, in relation to dry mass of chitosan) in acetic acid was slowly added to chitosan solution, stirred for 5 min at 3000 rpm, and then homogenized using ultrasonic bath (30 min at 40 kHz, 100% power without heating). Mixtures were applied on Petri dishes and dried for 12 h at 35 °C. Obtained films were homogenous, no holes or big agglomerates were present.
Samples were named for ease of experiments and film characterization such as CHT/CNC I where stands for chitosan composite with 5% loading of nanocrystalline cellulose I.

Metal ion adsorption process

The sorption properties of chitosan membrane and cellulose/chitosan composites were performed using aqueous solutions of individual ion – magnesium(II), calcium(II) and iron(III) at a concentration 0.1 mM. The membrane samples at weight of 0.1 ± 0.0001 g were put into glass vials containing 10 mL of metal solution. The pH value during experiment was 5. The studies by Mahatmanti et al. (2016) showed that ion adsorption by chitosan is most effective for pH in the range 5–6. The choice of this pH solution is also confirmed by Gedam et al. (2018), in which the influence of the pH of solution on the adsorption process was studied. On the basis of a review of work of Mahatmanti et al (2016) and Gedam et al. (2018), it was assumed that at the chosen pH 5 the adsorption process occurs under optimal conditions for most elements. Based on the results of the study on the kinetics of the adsorption process, described in the paper Kaveeshwar et al. (2017), and Wu et al. (2010), in this paper aqueous solutions of nitrate (V) salts of alkali metals Ca(II), Mg(II) and sulphate (VI) heavy metal Fe(III), at the lowest concentration were studied.
After 1 h, the membranes were removed from metal solutions, put on Petri dishes and dried for 2 h at 95 °C.

Characterization of cellulosic fillers and composite materials

X-ray diffraction (XRD)

Before characterization samples were freeze-dried at – 50 °C, vacuum 0.33 mbar (Christ, model Alpha 1–2 LDplus). Materials were analyzed by means of X-ray diffraction using CuKα radiation at 30 kV and 25 mA anode excitation. The X-ray diffraction patterns were recorded for the angle range of from 5 to 40° in the step of 0.05°/3 s. Deconvolution of peaks was performed by the method proposed by Hindeleh and Johnson (1971), improved and programmed by Rabiej (1991).

Particle size

Zetasizer Nano ZS (Malvern Instruments Ltd.) employing the laser diffraction technique in the range of 0.6–6000 nm was applied to determine particle size and the dispersive properties of (nanometric) celluloses.

Flame atomic absorption spectrometry—FAAS

The samples of chitosan membrane and cellulose/chitosan composites at weight 0.5 g were mineralized with nitric acid (8 mL) in a semi-closed microwave mineralization MARSXpress system (CEM Corporation). After mineralization process, solutions were filtered and diluted of deionized water to 50 mL. The content of Mg, Ca, Fe in the samples was analyzed by means of FAAS, using a Spectra 280 AA spectrometer (Agilent Technologies). The calibration curve was prepared from the serial dilutions of standard solutions of examined elements. The final results were average values of three simultaneous measurements.

FTIR spectroscopy—attenuated total reflection (ATR)

Spectra were registered using a Nicolet iS5 spectrophotometer by Thermo Fisher Scientific with Fourier transform at a range of 4000–500 cm−1 at a resolution of 4 cm−1, registering 32 scans.

Wettability angle

Measurements of contact angle (CA) with water were carried out using Dataphysics OCA 200 instrument. All measurements were carried out at 298 ± 0.1 K. A drop of 0.2 µL was automatically pushed out of the capillary and deposited on a solid surface of the sample.

Tensile properties

Tensile properties of produced composite films were defined using Zwick and Roell Allround-Line Z020 TEW testing machine. Samples of 10 mm width and thickness ca.100 µm were tested with speed 5 mm/min and initial force 0.2 N in accordance to standard ISO 527–3. The arithmetic mean of seven replicate determinations was taken into consideration in each case.

Results and discussion

Supermolecular structure of fillers

WAXS technique was used to assess supermolecular structure of cellulosic fillers. An analysis of patterns shown in Figs. 1 and 2. confirm that the polymorphic conversion from C I into C II and CNC I into CNC II was successful. Deconvolutions of all XRD patterns are presented in Supplementary Materials.
Fig. 1
WAXS patterns for cellulose before and after mercerization
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Fig. 2
WAXS patterns for nanocellulose before and after mercerization
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Figures 1 and 2 show diffractograms of samples with peaks assigned to respective crystallographic planes. The X-ray patterns for C I and CNC I samples indicate the occurrence of peaks at angles of 2Ө = 15°; 16.5°; 22.5° and 34.5° (French 2014).
After mercerization (C II and CNC II samples) the diffraction patterns have changed. Theoretically, in mercerized samples the first peak, coming from (-110) plane, should be located at 2Ө = 12.5°(French 2014). Although, in this study we observed only a very broad peak at ca. 14°. This was quite surprising and unfortunately, we found no fully convincing reason for that. It seems possible that this one, broad peak is a result of overlapping two peaks from (1-10) and (110) planes, originating from cellulose I that was not fully converted to cellulose II. However, if that was a case, we should also observe peak at 2Ө = 22.5°, which was not present. Thus, this issue remains unsolved.
For C II and CNC II all other peaks were in line with literature data (French 2014). The crystalline peak at 2Ө = 23° disappeared and instead two weaker peaks at 2Ө = 20° and 2Ө = 22° were observed. These peaks came from the lattice planes (110) and (200) or (020), respectively. That indicates formation of (nano)cellulose II and proves that the use of 16% aqueous NaOH solution allowed for conversion of cellulose I into cellulose II. This is consistent with literature reports which show that the use of NaOH with a concentration higher than 10% allows for effective conversion of native cellulose into cellulose II (Yue et al. 2013).
Another aspect, in addition to the polymorphic conversion that occurs during the mercerization process, is the reduction in the degree of crystallinity. This is due to the conversion of some crystalline regions into amorphous ones. The results of the research show also that mercerization was responsible for some reduction in the degree of crystallinity. For micrometric cellulose I and cellulose II it was ca. 70% and 47%, respectively. For nanometric cellulose I it was 68% versus 43% for nanometric cellulose II. The existence of a similar relationship was also demonstrated in other publications (Yue et al. 2013). What is interesting, polymorphic conversion was slightly more efficient in nanometric samples.
X-ray studies confirmed the polymorphic conversion of cellulose, which allowed in the next stage for analysis of the effect of crystal structure of cellulose on efficiency of removal of metals ion, which effect has not been studied so far.

Particle size of fillers

Studies on the size distribution of particles showed a relationship between the crystallographic modification and the size of cellulose particles. Particle size distributions of cellulose I and cellulose II were already presented in our previous studies (Grząbka-Zasadzińska et al. 2018). It showed that mercerization process caused the decrease in particle sizes from ~ 48 µm for C I up to ~ 40 µm for C II.
Results obtained for CNC I and CNC II are given in Fig. 3.
Fig. 3
Distribution of particle size for fillers
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For CNC I a significant amount of the micrometer fraction was noted. Particles were also characterized with wide distribution of particle size (78.8–4800 nm). However, particles with diameter between 78.8 nm and 142 nm accounted for 58.6% of the sample. It should also be emphasized that according to the accepted IUPAC nomenclature, nanofillers are materials in which at least one dimension does not exceed 100 nm. However, in the presented work Arbocel UFC 100 BRIGHT was named as CNC I. The adopted nomenclature resulted from significant disproportions in the particle size of the analyzed materials, and its introduction primarily served to distinguish particles with a size close to 100 nm from cellulose with a clearly micrometric dimension ≥ 2670 nm.
The obtained results of particle size distribution for CNC II showed that the mercerization process led to the reduction of particle size and the obtained filler was characterized by a much narrower range of particle diameters (50.8–142 nm). It is worth emphasizing that no micrometer fraction was found for this filler. The mercerization process of CNC I resulted in both polymorphic conversion of cellulose and also obtaining only the nanometric fraction (below 150 nm).

Sorption process

The concentration of magnesium, calcium, and iron adsorbed by chitosan film and cellulose/chitosan composites determined by means of FAAS is presented in Table 1.
Table 1
Concentration of the adsorbed magnesium, calcium and iron by chitosan film and cellulose/chitosan composites
Samples
Concentration (mg/g)
Mg(II)
Ca(II)
Fe(III)
CHT
1.1385 ± 0.0105
2.5962 ± 0.2464
0.2655 ± 0.0097
CHT/C I
1.2446 ± 0.0262
3.3707 ± 0.0462
0.6637 ± 0.0088
CHT/C II
0.5597 ± 0.0189
2.7668 ± 0.0917
0.9775 ± 0.0128
CHT/CNC I
0.5001 ± 0.0197
2.8254 ± 0.1001
0.8147 ± 0.0588
CHT/CNC II
4.5434 ± 0.0255
4.9689 ± 0.0386
1.2729 ± 0.0261
The results given in Table 1 prove that all tested samples demonstrated ability of sorption of Ca(II), Mg(II) and Fe(III) from aqueous solutions. The most effective sorption was observed for calcium ion. Among tested samples, the most effective sorption ability with regard to all metal ion was observed for CHT/CNC II. The sorption efficiency of this composite was higher than for chitosan membrane about four, two, and five times as regard to Mg(II), Ca(II), and Fe(III), respectively. Satisfactory results of Ca(II) sorption were observed also for chitosan with cellulose I (CHT/C I). Moreover, all tested composites were characterized with higher sorption of Ca(II) and Fe(III) than chitosan membrane itself. Materials containing cellulose I (CHT/C I) showed higher sorption properties as regard to Ca(II) and Mg(II) than composite with cellulose II (CHT/C II). On the contrary, composite containing nanocellulose I (CHT/CNC I) adsorbed less of Ca(II) and Mg(II) than composite with nanocellulose II (CHT/CNC II). These results indicated that crystal form of cellulose influences on its sorption properties.
Sorption properties of chitosan-based composites depend on the type of the filler used. The sorption ability of chitosan membrane blended with rice hull ash silica and polyethylene glycol as regard to Ca(II) was reported to be lower than to Mg(II) (Mahatmanti et al. 2016). On the other hand, the sorption properties of chitosan-alginate membrane were found to be higher as regard to Ca(II) than Mg(II) (Cahyaningrum and Herdyastuti 2011).
The sorption of Fe(III) by cellulose/chitosan composites was lower than sorption of Ca(II) and Mg(II), but it was more effective than for chitosan. Sorption of Fe(III) for composites was 2.5 and 4.8 times higher, for CHT/C I and CHT/CNC II, respectively, than chitosan membrane. The results obtained by Radomski et al. (2014) indicated that chitosan/aspartic acid copolymer cured with ethylene glycol showed lower sorption ability as regard iron ion (0.140 mg g−1) than chitosan (0.240 mg g−1). It is worth emphasizing that all composites examined in this paper have achieved higher concentration of adsorbed iron. CHT/CNC II composite adsorbed over five times more iron than materials tested by Radomski et al. (2014).
The FTIR spectra of pure chitosan sample (A) and metal loaded forms (B-F) shown in Figs. 4, 5 and 6 confirm AAS results presented in Table 1.
Fig. 4
FTIR spectra in the 4000–400 cm−1 wave number range for chitosan CHT (A) before sorption process, chitosan and cellulose/chitosan composites after Mg(II) sorption: CHT (B), CHT/C I (C), CHT/C II (D), CHT/CNC I (E), CHT/CNC II (F)
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Fig. 5
FTIR spectra in the 4000–400 cm−1 wave number range for chitosan CHT (A) before sorption process, chitosan and cellulose/chitosan composites after Ca(II) sorption: CHT (B), CHT/C I (C), CHT/C II (D), CHT/CNC I (E), CHT/CNC II (F)
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Fig. 6
FTIR spectra in the 4000–400 cm−1 wave number range for chitosan CHT (A) before sorption process, chitosan and cellulose/chitosan composites after Fe(III) sorption: CHT (B), CHT/C I (C), CHT/C II (D), CHT/CNC I (E), CHT/CNC II (F)
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The interpretation of FTIR spectrum of pure chitosan based on literature data are presented in Table 2 (Silva et al. 2012; Soundarrajan et al. 2013; Zhao et al. 2014; Okoya and Adeodun 2017).
Table 2
The interpretation of FTIR spectrum
Band position
[cm−1]
Characteristic of the band—assignment of vibration
3345
Stretching vibration of O–H and N–H2
2927, 2876
Stretching vibration of C–H
1635
Vibration of N–H in 1° amides
1538
Bending vibration of N–H in 2° amides
1405
Stretching vibration of C-H
1380
Deformation vibration of N–H
1338
Vibration of N–H in 3° amides
1256
Stretching vibration of C–O–H
1153
C–O stretching vibrations of the glycoside linkage
1064
Stretching vibration of C-O and N–H
1019
Vibration of C–C-C skeletal
898
CH3–C–OH stretching vibration
650
Bending vibration of –OH
558
Bending vibration of C–C
Figures 4, 5 and 6 (B-F) show the FTIR spectra of cellulose/chitosan composites loaded with Ca(II), Mg(II), and Fe(III) ion. An interesting phenomenon is the shift in the position and intensity of the bands after metal binding. The FTIR spectra of CHT/CNC II biosorbent indicate the presence of predominant peaks at 3355 cm−1 (–OH and –NH stretching vibrations), 2927 cm−1 (–CH stretching vibration), 1538 cm−1 (–NH bending vibration), 1380 cm−1 (–NH deformation vibration), and 1064 cm−1 (–CO stretching vibration). This reveals that all functional groups originally present in chitosan and its composites are still present, even after interaction with Ca(II), Mg(II), and Fe(III) ion (Vijaya et al. 2008).
The FTIR spectra of the cellulose/chitosan composites after adsorption were very similar to the spectra of unfilled chitosan after adsorption. However, some noticeable differences have been observed in the intensity of bands. Namely, the peak at 3355 cm−1, corresponding to the stretching vibrations of –OH and –NH2 became broader and of higher intensity, indicating some interaction between these groups and Ca(II), Mg(II), and Fe(III) ion. Bands near 1064 cm−1 in pure chitosan are usually attributed to the C–O and C–N stretching vibrations. The intensity of these characteristic bands significantly decreased in the spectrum of the CHT/CNC II complex with calcium, magnesium, and iron, indicating that C–O and C–N groups are involved in coordination of these ion. Moreover, bands appearing in spectra in the range of 615 and 558 cm−1 can be attributed to the stretching vibrations of N–Ca, Mg or Fe and O–Ca, Mg or Fe (Perelshtein et al. 2013).
In Mahatmanti’s paper (Mahatmanti et al. 2016) a mechanism of binding various metal ion by chitosan was proposed. In comparison to zinc, calcium and magnesium ion were adsorbed less effectively. The authors explain that ionic bond between calcium and magnesium ion and hydroxyl and amino groups in chitosan is unstable and breaks easily, especially in a polar solvent, e.g. water. However, the other work (Piątkowski et al. 2010) showed that magnesium and calcium do not react with chitosan or these interactions are too weak to stabilize the resulting complex. During the adsorption, due to the cationic nature of chitosan, negative charge residues compete with metal ion. In addition, differences in the efficiency of iron, magnesium and calcium ion adsorption may also result from their different valence that has an impact on the mechanism of chelate formation.
The sorption results clearly indicate a significance of the type of cellulose filler used for filling chitosan. It was shown that composites containing cellulose II with nanometric sizes (CHT/CNCII) adsorbed metal ion the best.
On the basis of the results obtained in this paper, it follows that the efficiency of metal ion adsorption in composites is a result of two factors: crystal structure of cellulose and particle size of cellulose fillers. The first factor to consider is polymorphism of cellulose. Quillin et al. (1993) maintain that the pyranose rings on the face of cellulose II are not aligned in a "flat" manner as is the case with cellulose I (Quillin et al. 1993). The importance of matching the cellulose crystal structure to other components (i.e. polymer) has been described in many papers (Wittman and Lotz 1990; Quillin et al. 1993; Felix and Gatenholm 1994; Son et al. 2000; Borysiak 2012, 2013b). This aspect plays also a decisive role in the nucleation process. Therefore, it can be assumed that parameters of crystal lattice of cellulose II correspond better with size of metal ion, thus increasing interactions and consequently enhancing sorption efficiency. However, in this research high ion adsorption was obtained only when nanometric cellulose II was used. Composites with micrometric cellulose II were not so effective, which suggest the presence of some synergy. High efficiency of calcium, magnesium, and iron ion adsorption can be obtained using chitosan composites containing both, filler with polymorphic form of cellulose II and its nanometer fraction. The presence of only cellulose nanometric filler (CNC I) did not guarantee high adsorption efficiency.

Wettability studies

Analysis of the results given in Table 3 shows that all of the tested samples were hydrophobic (contact angle > 90°). For almost all samples values of water CA were comparable and in range from 107.3° to 110.3°. Surprisingly, contact angle for CHT/CNC II sample was different, it was only 96°. Such situation was not observed for any other material. Figure 7 presents photos of samples during CA tests.
Table 3
Contact angle for chitosan and its composites
Sample
Contact angle (CA) (°)
CHT
110.3
CHT/C I
107.3
CHT/C II
107.9
CHT/CNC I
108.4
CHT/CNC II
96.0
Fig. 7
Photos taken during measurements of contact angle using water
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Chitosan itself is known to have low interaction with water. This is due to protonated amine groups (NH3+) disposed in chitosan backbone that appear while dissolution in acid solution (formation of cationic polymer). Migration of positive charges to sample surface results in weakening its adhesion with polar molecules of water (Mathur and Narang 1990).
In this study four different cellulose types were used as fillers for chitosan. However, when compared to pristine chitosan, only in case of one material its hydrophobicity was reduced. It is clear that CNC II filler was responsible for decrease of the contact angle value. The reasons for this phenomenon are complex and require consideration of two main factors: polymorphic form and size of filler.
Firstly, each cellulose polymorph has some unique properties that result from different supermolecular structure of the material. Cellulose II, called regenerated cellulose too, is less crystalline and has bigger size of elementary cell than cellulose I. Moreover, structure of cellulose II is looser and less packed than in native cellulose. It is a high affinity between molecules of water and polar groups of cellulose that causes films of regenerated cellulose to be among the most hydrophilic polymeric films (Lindman et al. 2017). Secondly, as follows the analysis of DLS results, particles of CNC II were definitely smaller (50.8–142 nm) than particles of C II (~ 40 µm) or even CNC I (78.8–4800 nm). The reduction in particle size was also associated with an increase in the amount of free -OH groups.
The results of wettability tests correlate well with adsorption studies. CHT/ CNC II composites were characterized with the highest sorption capability and the highest hydrophilicity. In this system, the metal ion found in the solution could much easier move to the interior of the bulk, where they could be coordinated by the functional groups of chitosan and thus adsorbed.

Tensile properties of composites

Tensile tests were performed to calculate Young’s modulus (YM), tensile strength (TS), and elongation at break (EB) parameters. The obtained data are presented in Table 4.
Table 4
Tensile properties of chitosan and its composites
 
YM (GPa)
TS (MPa)
EB (%)
CHT
0.24 ± 0.06
24.9 ± 1.3
42.2 ± 4.5
CHT/C I
1.66 ± 0.19
42.0 ± 2.0
8.7 ± 0.8
CHT/CNC I
2.52 ± 0.39
74.6 ± 2.5
50.4 ± 4.9
CHT/C II
1.29 ± 0.16
26.7 ± 1.4
5.8 ± 1.2
CHT/CNC II
0.92 ± 0.14
38.2 ± 3.2
7.5 ± 1.4
Introduction of each filler into polymer matrix resulted in increase of YM parameter. However, the highest value of the Young's modulus (2.52 GPa) was noted for CHT/CNC I composite and it was over ten times higher than for unfilled chitosan (0.24 GPa).
It can be also seen that polymorphic form of filler used had an influence on YM—higher values of this parameter were observed for composites with CNC I and C I fillers than in case of CNC II and C II. Surprisingly, it is not possible to unambiguously determine the influence of the size of the particles used. In case of native celluloses (C I and CNC I) higher values of YM were obtained if nanometric filler was used and for mercerized fillers (C II and CNC II) this trend was reversed.
Tensile strength for all composites was higher than for chitosan. Films with CNC I were characterized with definitely the highest TS, almost 75 MPa while chitosan reached only 24.9 MPa. This parameter was affected not only by polymorphic form of filler but also its size. It is evident that higher values were achieved when native cellulose was used. It also noticeable that composites with nanometric fillers exhibited higher tensile strength than films with micrometric celluloses. It is believed that the increase of particle size of reinforcement causes an enhanced debonding of the filler from polymer matrix. During dynamic loading of composites with large diameter particles the filler is separated from the matrix, which results in formation of free spaces. This phenomenon was not observed for composites with small filler particles.
As expected, introduction of cellulosic fillers into chitosan matrix resulted in sharp decrease of elongation at break. Interestingly, EB for composite with CNC I was found to be 50.4%, while for chitosan it was 42.2%. Achieving such high elasticity value for composite is extremely important because in most cases introduction of even a small amount of filler into polymer matrix causes EB parameter to drop. This is due to the high stiffness of cellulosic fillers that limit the elasticity of the material (Samir et al. 2004; Dai et al. 2015; Hosseini et al. 2015).
In view of above it is obvious that the tensile properties of composites depended strongly on the polymorphic variety and size of cellulosic filler used.
Composites with cellulose II are often characterized by lower values of tested parameters than materials with native cellulose, what is in agreement with other studies. Tests carried out on composites with wood proved that alkalization of wood was responsible for the reduction of mechanical properties (Marcovich et al. 2001). Other researchers also did not confirm the positive effect of mercerization on the macroscopic properties of composites (Ichazo et al. 2001; Pimenta et al. 2008; Borysiak 2013b; Borysiak and Grząbka-Zasadzińska 2016; Grząbka-Zasadzińska et al. 2018).
In general, it can be seen that composites with nanometric filler were characterized by higher mechanical parameters than micrometric composites (except for YM for mercerized fillers). That is due to higher effectiveness of stress transfer between matrix and nanometric filler (Fu et al. 2008). It is also in line with other researches showing that modulus of composites increases as the particle size decreases (Grząbka-Zasadzińska et al. 2019).
However, since particles of CNC II were found to be smaller than particles of CNC I one could expect that CHT/CNC II composites would exhibit better mechanical properties than CHT/CNC I. In fact, it is more complicated as two factors have to be taken into account: (1) negative effect of mercerization mentioned above, (2) agglomeration of nanometric fillers. As we showed in our previous work (Grząbka-Zasadzińska et al. 2019) characteristic feature of samples containing significant amounts of nanometric size particles, up to 220 nm, was their tendency to form micrometric agglomerates.

Conclusions

In this work, we analyzed the influence of supermolecular structure and dispersive properties of cellulose on the effectiveness of the metal ion adsorption in chitosan composites. It was shown that after mercerization CNC II had a particle size in the range of 50–120 nm, while starting CNC I had not only nanometric (80–120 nm) but also micrometric fraction (ca. 3–4 µm). Composites of chitosan and various types of cellulosic fillers were subjected to adsorption tests in aqueous solutions of following metal ion: Ca(II), Mg(II), and Fe(III).
Results of FAAS and FTIR tests showed some interesting, unreported relationship between the structure of the filler and effectiveness of the sorption process. It was found that the efficiency of metal ion sorption depends on two parameters—polymorphic form and size of the filler. The highest efficiency of adsorption (for all metal ion) was noted when filler with nanometric size of particles and supermolecular structure characteristic for cellulose II was used. Micrometric cellulose II did not guarantee such high efficiency.
In addition, it is worth noting, that composites with nanometric cellulose with polymorphic form of cellulose I, did not exhibit high adsorption efficiency. This results from ion of metal matching the dimensions of crystal lattice of cellulose. Nonetheless, the mechanism of this adsorption process is still not fully examined. Therefore, we plan to carry out further analysis using XPS method or desorption tests that could provide more insight into mechanism of sorption of metal ion on such biocomposites.
Contact angle studies have shown that composites with nanometric cellulose II had higher wettability of the surface. It ensures greater hydrophilicity and, consequently, affinity to aqueous metal ion solutions. From an application point of view, it is important that all chitosan composites were characterized by higher strength than the chitosan matrix.

Acknowledgments

This work was supported by the Polish Ministry of Education and Science.

Declarations

Conflicts of interest

The authors declare no conflict of interest.

Research involving human participants and/or animals

No Human Participants and/or Animals were involved in the study.
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Titel
The influence of crystalline structure of cellulose in chitosan-based biocomposites on removal of Ca(II), Mg(II), Fe(III) ion in aqueous solutions
Verfasst von
Aleksandra Grząbka-Zasadzińska
Izabela Ratajczak
Katarzyna Król
Magdalena Woźniak
Sławomir Borysiak
Publikationsdatum
14.05.2021
Verlag
Springer Netherlands
Erschienen in
Cellulose / Ausgabe 9/2021
Print ISSN: 0969-0239
Elektronische ISSN: 1572-882X
DOI
https://doi.org/10.1007/s10570-021-03899-3

Supplementary Information

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