This study was aimed at the development of a better understanding of the agglomeration behavior of sulfated cellulose nanocrystals (CNCs) in the presence of sulfates with monovalent (NH4+, K+, Na+) and divalent (Ca2+) cations, and to demonstrate their potential in simple and efficient product separation. Protonated CNCs were counterion-exchanged and their ionic strength was increased by adding sulfates of the respective cation to trigger agglomeration. The critical concentrations of agglomeration (CAC) and peptization (CPC) were determined. We found that the agglomeration behavior of CNCs could be attributed to matching affinities between the cations and the sulfate half-ester groups on the CNC surfaces. Based on these findings, a facile and efficient downstream process was designed to separate CNCs from neutralized reactant solutions using CAC and CPC. This method provides colloidally stable CNCs at high yield provided by centrifugation. When salt concentrations in the product are maintained below the CAC, as prepared CNCs from neutralized reactant solutions might be used in hydrogels and emulsions.
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Introduction
Cellulose nanocrystals (CNCs) are nanorods with widths ranging from 3 to 50 nm and aspect ratios from 5 to 50 (ISO 2017b). They have received an increasing amount of attention from academia and industry alike due to their straightforward production and their remarkable physical and chemical properties, which make them high-performance building blocks for a wide range of potential commercial applications (Cowie et al. 2014; Thomas et al. 2018; Dufresne 2019). CNCs are commonly produced by sulfuric acid-catalyzed hydrolysis of purified cellulosic feedstock extracted from botanical sources, tunicates, or bacteria (Habibi et al. 2010; Sacui et al. 2014), although numerous extraction methods exist (Trache et al. 2017). Hydrolytic cleavage of glycosidic linkages and further breakdown of cellulose to glucose and oligosaccharides, as well as conversion to 5-(hydroxymethyl)furfural preferably occurs in the amorphous domains of cellulose (Sun et al. 2016), leaving CNCs with higher acid resistance as the product. The morphology and yield of CNCs for a process are mainly determined by processing temperature, time, and the cellulose source (Beck-Candanedo et al. 2005; Dong et al. 2016). Concurrent with the hydrolysis, sulfate half-esters (R–O–SO3−) are grafted onto some of the hydroxy sites of the CNCs. The number density of surface sulfate groups can be controlled by acid concentration and the acid-to-cellulose ratio (Dong et al. 2016; Abitbol et al. 2018). The electric surface charge governs electrostatic interparticle repulsion forces and thus the colloidal stability of CNCs in polar media. CNCs produced by sulfuric acid-catalyzed hydrolysis usually contain between 240 and 330 mmol of sulfate per kg of CNCs (Dong et al. 1996; Araki et al. 1999).
Never-dried CNC colloids and counterion-exchanged CNCs (H+ → Na+) are commonly used for subsequent processing, as well as to produce new materials incorporating CNCs. Thus, a significant effort has been made to understand and to tune their colloidal stability. Several works have addressed the effect of electrolytes and ionic species on the agglomeration and gelation behavior of colloidal CNCs (Dong et al. 1996; Dong and Gray 1997; Boluk et al. 2011; Shafiei-Sabet et al. 2014; Cherhal et al. 2015; Peddireddy et al. 2016; Phan-Xuan et al. 2016; Bertsch et al. 2017; Mikhailov et al. 2017; Wu et al. 2017, 2019; Liu et al. 2018; Moud et al. 2018, 2019; Qi et al. 2019). All of the aforementioned studies focused on agglomeration of sulfated CNCs induced by chlorides, with inorganic counterions of varying valence. Studies have shown that the critical agglomeration concentration (CAC) of a volume of an electrolyte is in the range of tens of mM and decreases to a few mM with increasing valence of the counterion, roughly following the Schulze-Hardy rule (Phan-Xuan et al. 2016).
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Agglomeration of CNCs also plays a role in downstream processing when CNCs are separated from the reactant solution that also contains sulfuric acid, the previously mentioned byproducts formed by hydrolysis, and incompletely hydrolyzed cellulosic residues. However, the unit operations involved have received only little attention. Hydrolysis of cellulose in a solution volume is usually quenched by adding a ten-fold amount of water (Trache et al. 2017). CNCs are then present in an agglomerated state due to the prevalently high ionic strength and cannot form a stable colloid. This agglomeration facilitates the removal of any excess ions and soluble reaction products by repeated washing by centrifugation and decanting of the supernatant, and subsequent redispersion in fresh water. In the presence of only sulfate anions, the critical peptization concentration (CPC) is approached at about 100 mM sulfuric acid when peptization of the CNCs occurs, recognizable by an accruing cloudiness of the supernatant. Subsequent washing steps at ionic strengths below the CPC would imply a loss of colloidally stable product fractions in the discarded supernatant. Thus, any further purification of the intermediate product involves low-efficiency techniques such as dialysis or reverse osmosis, or it requires special apparatus, for example for diafiltration or electrodialysis (Rudie 2017).
In scale-up scenarios, CNC production may involve neutralization of the remaining acid with caustic soda after centrifugation (Reiner and Rudie 2013; Assis et al. 2017). Alternatively, the reactant solution can be neutralized with mono- or divalent hydroxides or metal oxides at an arbitrary step in downstream processing (Müller and Briesen 2017, Metzger et al. 2018). By analogy with product separation from diluted reactant solutions, ionic residues must be thoroughly removed from neutralized reactant solutions to obtain a colloidally stable product.
To date, studies of salt-induced agglomeration of CNCs have only addressed the use of chlorides to control the product properties, while the roles of salt and ionic residues during product separation have received no attention to our knowledge. In this study, we hypothesize that CNCs will show similar agglomeration behavior in the presence of sulfates as they do with chlorides. We therefore presume that it is not only ionic strength but also the type of cation that contributes to the colloidal stability of CNCs. Because the separation efficiency by centrifugation is directly related to colloidal stability, we assumed that the introduction of cations during neutralization of the intermediate product affects the CPC. Therefore, neutralization can be used to reduce the effort to purify the product.
The colloidal stability of sulfated CNCs in the presence of the secondary sulfates (NH4)2SO4, K2SO4, Na2SO4, and CaSO4 was investigated in this work by a fast and easy-to-use spectrophotometric method. The results were applied to design an efficient purification process based on the CAC and the CPC during centrifugation, yielding colloidally stable CNCs. The results are of particular interest for the sustainable production of CNCs with low resource requirements in downstream processing steps.
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Materials and methods
Chemicals
Whatman ashless filter aids (cotton α-cellulose) were purchased from Sigma-Aldrich (Taufkirchen, Germany). Calcium hydroxide (Ca(OH)2, 96%), sulfuric acid (H2SO4, 96%), potassium hydroxide (KOH, 85%), ammonium hydroxide (NH4OH, 25%), and sodium hydroxide (NaOH, 99%) were used for preparing and processing CNCs and were purchased from Carl Roth (Karlsruhe, Germany). Poly-L-lysine (0.1% (aq), Ted Pella, Redding, CA, USA), ethanol (70%, Carl Roth, Karlsruhe, Germany), and uranyl acetate (SERVA, Heidelberg, Germany) were used for transmission electron microscopy. Sodium chloride (NaCl, 99.5%) and sodium hydroxide (NaOH (aq), 2 mM), required for conductometric titration, were purchased from Carl Roth. All chemicals were used in their as-received state. Ultrapure (type 1) water (H2O) with a resistivity of 18.2 MΩ cm (Milli-Q Direct 8 system, Merck Chemicals, Schwalbach, Germany) was used to prepare solutions for all experiments.
Preparation and processing of CNCs
Aqueous colloidal suspensions of sulfated CNCs were prepared by heterogeneous hydrolysis of oven-dried (105 °C, 30 min) cellulose with sulfuric acid, based on the method of Cranston and Gray (2006). The bound water content of the cellulosic feedstock after drying was determined to be 4.5 wt% by Karl Fischer titration, and was considered when calculating the weighed portions of the educts. Sulfuric acid, 96 wt% was diluted to 64.2 wt% with water and pre-heated to 45 °C. Cellulose was added in at a mass-mixing ratio of 10 \(m_{{H_{2} SO_{4} }} m_{cellulose}^{ - 1}\) with the weighed portions of sulfuric acid, \(m_{{H_{2} SO_{4} }}\), and cellulose, \(m_{cellulose}\), and stirred constantly for 45 min.
The agglomeration behavior of CNCs in the presence of secondary sulfates was studied in CNCs which were separated by centrifugation and dialysis (route A), as commonly reported in literature. The neutralization-based separation of CNCs by centrifugation (route B) was conducted to demonstrate the applicability of the results from route A. Both routes were implemented in this work as illustrated in the flowcharts in Fig. 1. A detailed description of the unit operations involved in both routes, as well as further treatment of the CNCs prior to subsequent analyses, is given in the following sections.
Fig. 1
Downstream processes for the purification of CNCs by centrifugation/dialysis (a) and neutralization/centrifugation (b). Further sample treatments for studying the agglomeration behavior and for determining the dispersion properties of the CNCs are presented below the dashed line
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Route A: Product separation from diluted reactant solutions
After hydrolysis, the reactant solution was quenched by tenfold dilution with regard to the effective initial acid concentration (64 → 6.4 wt%) with 4 °C water. Excess acid and soluble byproducts were decanted after leaving the precipitate to settle overnight. The resultant cloudy suspension was washed by twofold centrifugation for 15 min at 4500 × g (Centrifuge 5804 R, Eppendorf, Hamburg, Germany), decanting, and further dilution with water. The precipitate was then dialyzed in regenerated cellulose tubes with a molecular weight cutoff of 12—14 kDa (ZelluTrans/ROTH T3, Carl Roth, Karlsruhe, Germany) against running water with a volumetric flow of 0.5 L h−1 in a 7 L vessel to remove the remaining acid and soluble byproducts. Dialysis was stopped when the waste water had a conductivity ≤ 30 µS cm−1 after equilibration for 6 h. Agglomerated CNCs were disagglomerated by sonication with a homogenizer (Sonopuls HD 3400 with the sonotrode VS 70 T, Bandelin, Berlin, Germany) at an energy input of 5 kJ g−1 cellulose and an amplitude setting of 30% in an ice bath. In accordance with Beck et al. (2011), no breakage of covalent cellulose-sulfate half-ester bonds—and thus no release of sulfate ions—was assumed due to sonication. Incompletely hydrolyzed solid cellulosic residues were then removed by centrifugation for 15 min at 4500 × g. Any further treatment with ion-exchange resins was omitted due to the extensive dialysis (Abitbol et al. 2013). The final dispersion of never-dried protonated CNCs, denoted as H-CNC, was stored at 4 °C until further use.
To study salt-induced agglomeration, H-CNCs were first neutralized as separate samples by the addition of the respective base until a stable pH of 7 was reached. The samples were named in accordance with the respectively exchanged counterion NH4+, K+, Na+, or Ca2+ (Table 1). Then, the CAC, at which agglomeration is initially observed, and the CPC, at which all CNCs are agglomerated, were empirically determined using a binary search approach. For this approach, the ionic strengths, \(I\), of aliquots of each sample were adjusted by adding aqueous solutions of the secondary sulfate. In accordance with the literature (Cherhal et al. 2015), agglomeration at higher salt concentrations occurred instantly for all salts and was visible to the unaided eye. Destabilized CNCs would settle out over time (Cherhal et al. 2015), but the fraction of colloidally stable CNCs, \(\varphi_{s}\), was separated by centrifugation for 15 min at 4500 × g and optical absorbance was used to quantify \(\varphi_{s}\). The ionic strength of each sample was then adjusted in 15 steps from the CAC to the CPC. The salt solutions had been previously prepared by mixing the respective bases with sulfuric acid. The CNC concentration was kept constant at 1 wt% throughout the experiments.
Table 1
Nomenclature of CNCs by the respective counterions and properties of the associated secondary sulfates
Sample
Counterion
Associated sulfate salt
Salt solubilitya /g L−1
H-CNC
H+
NH4-CNC
NH4+
(NH4)2SO4
754
K-CNC
K+
K2SO4
111
Na-CNC
Na+
Na2SO4
170
Ca-CNC
1/2 Ca2+
CaSO4
2
aAt 20 °C; data retrieved from the GESTIS substance database: gestis-en.itrust.de
Route B: Product separation from neutralized reactant solutions
Partial quantities from the same batch that was used to produce the H-CNCs were separated after hydrolysis and the reaction was stopped by incremental neutralization with NH4OH, KOH, NaOH, or Ca(OH)2 to an excess of 15% of the initial sulfuric acid. For this operation, the reactant solutions were transferred to an ice bath to compensate for the neutralization enthalpy and were incrementally neutralized with their respective ice-cold base solutions. The concentration of bases with mono- and divalent cations was 1.25 M and 0.65 M, respectively. The intermediate products with monovalent cations were then washed by centrifugation for 15 min at 4500 × g, decanted to remove the supernatant, and successively redispersed in fresh water to remove excess ions and soluble byproducts from the hydrolyzed product. Each sample was then neutralized to a pH of 7 with its respective base. In the CaSO4 sample, the salt concentration exceeded its maximum solubility. Enough water and base were added to fall below the CAC after the first washing step. The pellet, including precipitated CaSO4 and entrained CNCs, was discarded. All samples were subsequently diluted to a salt concentration of 1.1 CPC and centrifuged again. The supernatant was decanted and the precipitate was diluted to 0.9 CAC using water. Similar to route A, all samples were eventually sonicated, centrifuged again, and stored at 4 °C until further use. Quantities of each sample were dialyzed to compare their dispersion properties to CNCs from route A.
Instrument measurements
All measurements were performed at least in triplicate and are presented with the 95% confidence interval of the mean. The uncertainty of quantities depending on multiple variables is driven by the propagation of error.
Conductometric titration
The content of the protonated sulfate half-esters (R-OSO3H) of the CNCs was determined by conductometric titration (Konduktometer 703 with the electrode sensor SE 204, Knick, Berlin, Germany) at 23 °C, based on the method proposed by Beck et al. (2015). 5 mL of a 1 wt% CNC dispersion was diluted into 80 mL of water. 1 mL of 0.1 M NaCl (aq) was added to elevate the conductivity to a measurable level. 2 mM NaOH (aq) was used as titrant in 0.2 mL increments under constant stirring. Stable conductivity readings were recorded 30—60 s after each addition.
The volume-corrected conductivity values were plotted against the added volume of NaOH. The equivalence volume of NaOH needed, and thus the number of accessible sulfate groups, was calculated from the intersection of the least squares regression lines of the two linear branches (\(R^{2}\) ≈ 1) of the titration curve.
The conductivity of the waste water was also measured during dialysis (see Supporting Information).
Dry weight and yield calculations
The concentrations of dry constituents at different stages of production were calculated from the mass quotient of an aliquot before water evaporation, \(m_{wet}\), and after water evaporation, \(m_{dry}\), by lyophilization (2–4 LSCplus, Christ, Osterode am Harz, Germany). Acidic aliquots were neutralized to a pH of 7 by titration against NaOH before water evaporation, and the weight of the formed salt, \(m_{salt}\), was considered in order to calculate the concentration of the cellulosic fraction. The cellulosic fraction of a sample of weight, \(m_{sample}\), was then extrapolated from the aliquot’s concentration. The yield refers to \(m_{cellulose}\), considering the overall mass balance and losses of individual unit operations. The yield, \(Y\), of cellulosic solid residues after centrifugation is:
The cellulose-to-CNC conversion rate was calculated from the ratio of the dry mass after dialysis and the dry mass after dialysis, sonication, and centrifugation.
Concentration adjustments were performed by diluting the stock dispersions with the respective amount of water.
Dynamic and electrophoretic light scattering
The hydrodynamic apparent particle size of dispersed CNCs was measured by dynamic light scattering (DLS) using a Zetasizer Nano ZSP (Malvern Instruments, Worcestershire, UK) equipped with a red laser (633 nm) under a backscatter detection angle of 173°. The harmonic intensity-weighted average particle diameter (z-avg) and the polydispersity index (PdI) from the cumulants analysis were obtained according to ISO 22412 (2017a) for 0.025 wt% CNC dispersions after equilibration for 30 min at 25 °C in disposable polystyrene cuvettes.
The ζ potential is derived from the electrophoretic mobility of the CNCs, which was determined from electrophoretic light scattering (ELS) with the same instrument as above. 0.25 wt% CNC dispersions were analyzed after equilibration for 30 min at 25 °C in folded capillary cells (DTS1070). Smoluchowski behavior with \(f\left( {\kappa a} \right)\) = 1.5 was assumed for Henry’s function, where \(\kappa\) was the Debye length and \(a\) the particle radius.
Transmission electron microscopy
Pioloform-coated copper grids (G2440C) from Plano (Wetzlar, Germany) were incubated with 0.1% poly-L-lysine at 23 °C for 30 min, rinsed with water, and dried under dust-free atmosphere. Never-dried CNCs were diluted with H2O to a concentration of 0.025 wt% and homogenized in a low-intensity ultrasonic bath for 10 min before droplets of the suspension were applied to the grids with a pipette. After 20 min, the grids were rinsed with water and left for drying. Negative staining of the CNCs was performed with a saturated ethanolic uranyl acetate solution. Excess liquid was removed and the samples were dried again. Transmission electron microscopy (TEM) images were acquired with a Philips CM10 instrument, coupled with a CCD camera (IDS, Obersulm, Germany), at an acceleration voltage of 80 kV. Particle length \(L\) was evaluated from 66 randomly chosen, individual particles using ImageJ (Rasband 2018).
UV–Vis spectrophotometry
Cellulose has no conjugated or unsaturated bonds. Hence, the optical absorption of transmitted light in the forward direction (180°) is 0 and the absorbance is governed by scattering only. For non-absorbing particles, the specific absorbance \(A\) at infinite dilution of colloidally stable CNCs, \(c_{CNC}\) → 0, is
with the scattering coefficient \(k\), the wavelength \(\lambda\), and the wavelength exponent \(n\) (Heller et al. 1962). \(k\) is a function of \(a\) and the relative refractive indices of the particles \(\mu_{2}\) and the dispersant \(\mu_{1}\). \(n\) is a function of \(a\) and can be derived from the slope of \(\ln \left( {A c_{CNC}^{ - 1} } \right)\) versus \(\ln \lambda\).
For non-spherical particles, the scattering cross sections and therefore the equivalent radii \(a_{eq}\) can be represented by the radii of spheres with equivalent volume-to-surface-area ratios (Grenfell and Warren 1999). The size parameter
$$ x = \frac{{2\pi a_{eq} }}{\lambda } $$
(3)
of the CNCs being not significantly smaller than 1 over the scanned wavelength range indicates Mie scattering, while Rayleigh scattering can be ignored. This was confirmed on absorbance spectra with \(a_{eq}\) derived from TEM data and wavelength-dependent refractive index data of cellulose from Sultanova et al. (2009), modeled with MiePlot (Laven 2018).
Thus, a linear relationship between the specific absorbance of a sample and the respective CNC concentration is observed. UV–Vis spectrophotometry is therefore suitable for the determination of the concentration of non-spherical colloidal CNCs with similar equivalent radii by using a comparison library of spectra of known CNC concentrations. A change of \(a_{eq}\)—for example induced by agglomeration, a change in polydispersity, or the use of particles of different dimensions—would manifest in a change of \(n\). This establishes a validity criterion for the applicability of the library to the measurement data, but also limits its applicability for the determination of CNC concentration to particles of similar sizes only. The evaluation of the validity of measurement is shown in the Supplementary Information.
A library of the UV–Vis absorbance spectra was set up, consisting of 18 individual samples of H-CNCs with defined concentrations between 0 and 1 wt%. Aliquots of 1 mL were transferred to quartz glass cuvettes with an optical path length of 10 mm and spectra were recorded with a Specord 50 Plus spectrophotometer (Analytik Jena, Jena, Germany) in the wavelength range from 200 to 500 nm. The CNC concentration of an arbitrary, water-dispersed sample could then be calculated from Eq. (2), for a sample concentration that is in the same concentration range as the library.
Results and discussion
H-CNCs from diluted reactant solution
H-CNCs were produced by sulfuric acid-catalyzed hydrolysis of cellulose according to route A. A CPC of 115 mM SO42− of CNCs in the presence of residual sulfuric acid was empirically determined in a binary search. The yield of cellulosic solid residues after centrifugation was 46.2 ± 0.6%.
Further purification of the product was achieved by using dialysis. The conductivity of the waste water decayed exponentially to 30 µS cm−1 after 166 h and the exchange of 83 L of water (see Supporting Information). CNCs were separated from incompletely hydrolyzed solid cellulosic residues by centrifugation subsequent to dialysis and sonication. The overall yield for cellulose-to-CNC conversion was 33.9 ± 0.5%.
Figure 2a is a representative TEM image of H-CNCs. The number-weighted particle length distribution of H-CNCs ranged from 70 to 230 nm with a mean particle length \(L_{mean}\) of 120 nm (Fig. 2b). Particle width \(W\) was estimated to be ≤ 10 nm for the particles, yielding an aspect ratio of ≤ 25 for all H-CNCs. The mean hydrodynamic apparent particle diameter of H-CNCs was 198 ± 4 nm. Overestimation of the particle size by DLS in relation to the more accurate TEM evaluation can be explained by the presence of a minor fraction of strongly scattering larger particles (Jakubek et al. 2018). The PdI of 0.21 ± 0.02 suggests moderate polydispersity, in accordance with the TEM images.
Fig. 2
TEM image of negatively stained H-CNCs (a) and number-weighted length distribution from 66 particles (b)
×
The ζ potential of the H-CNCs was −47.5 ± 5.4 mV and had a distribution width Δζ of 7.8 ± 1.2 mV. A sulfate half-ester content of 238 ± 5 mmol kg−1 was determined by conductometric titration. Table 2 summarizes the results from cellulose hydrolysis and the most relevant properties of H-CNCs. The data is in accordance with literature values (Bondeson et al. 2006; Reid et al. 2017).
Table 2
Summary of hydrolysis and dispersion properties of H-CNCs
Yield (solids) (%)
Yield (CNCs) (%)
L (TEM) (Nm)
z-avg (nm)
ζ (mV)
c (R-OSO3−) (mmol kg−1)
46.2 ± 0.6
33.9 ± 0.5
70–230
198 ± 4
− 47.5 ± 5.4
238 ± 5
Salt-induced agglomeration of CNCs
Cation-specific agglomeration of CNCs by the addition of sulfate salts
Colloidally stable CNCs in the presence of salts form self-similar clusters as a function of the salt concentration (Cherhal et al. 2015; Phan-Xuan et al. 2016; Moud et al. 2018). Therefore, controlling the ionic species and the salt concentration provides control over colloidal stability and thus the agglomeration of CNCs.
Colloidal stability of counterion-exchanged CNCs was not impeded by minor salt additions, so the number fraction of colloidally stable CNCs remained constant until the salt concentration exceeded the CAC. As can be observed from Fig. 3a, the concentration of colloidally stable CNCs indeed did decline at salt concentrations above the CAC. The evolution of agglomeration with increasing salt concentration for every sulfate salt followed canonical colloidal behavior (Gregory 1976). Above the CPC, all CNCs were agglomerated and could be sedimented by centrifugation, leaving no colloidally stable CNCs in the supernatant. Both CAC and CPC follow the sequence K+ < Na+ < NH4+ < Ca2+.
Fig. 3
Concentration of colloidally stable CNCs, \(\varphi_{s}\), as a function of salt concentration \(c_{salt}\) (a) and ionic strength \(I\) (b) for mono- and divalent secondary sulfates in separate aliquots having the same initial CNC concentration
×
All monovalent salts have similar interval widths of ΔCxC = CPC—CAC, and a comparatively narrower one for the salt with a divalent cation (Table 3). Each salt has a different CAC and CPC with regard to its ionic strength and therefore agglomeration cannot be explained by the screening of electrostatic surface charge alone (Fig. 3b). Monovalent cations do not follow Hofmeister’s lyotropic series NH4+ < K+ < Na+ (Hofmeister 1888). Furthermore, there is a marked difference in the agglomeration behavior of CNCs in the presence of a sulfate with a divalent cation with regards to its ionic strength. A tentative explanation of the deviation from DLVO theory of CNCs in the presence of salts has been proposed by Phan-Xuan et al. (2016). The differing magnitude of the impact of salts on the agglomeration of CNCs could be explained by the law of matching affinities (Vlachy et al. 2009). Soft cations in terms of charge density—such as NH4+ and Ca2+—trigger earlier agglomeration of CNCs electrostatically stabilized by soft sulfate half-ester groups. The strong effect of Ca2+ on agglomeration could furthermore be induced by more intense clustering of CNCs in the presence of divalent salts, or could be initiated due to cross-linking of CNCs by multivalent cations (Wu et al. 2017; Moud et al. 2019).
Table 3
Critical concentrations and ionic strengths for agglomeration and peptization of CNCs in the presence of mono- and divalent secondary sulfates
Counterion
CAC
CPC
ΔCxC
c (mM)
I (mM)
msalt mCNC−1 (mg g−1)
c (mM)
I (mM)
msalt mCNC−1 (mg g−1)
c (mM)
I (mM)
msalt mCNC−1 (mg g−1)
NH4+
27
82
360
52
157
690
25
75
330
K+
37
112
650
63
189
1100
26
77
450
Na+
35
106
50
56
169
800
21
63
750
Ca2+
6
24
8
18
73
250
12
50
242
Colloidal stability at different salt concentrations
Figure 4a shows the evolution of the ζ potential of CNCs in the presence of sulfate salts with different cations between CAC and CPC. Adding a salt to sulfated CNCs promotes the screening of electrostatic charges and gel formation by particle agglomeration (Peddireddy et al. 2016; Moud et al. 2018). Thus, colloidal stability at the CAC was inferior to H-CNCs, manifesting in lower absolute ζ potentials in the presence of the sulfates. Soft cations showed an effect on colloidal stability at lower ionic strengths. The addition of sulfate salts in concentrations slightly above the CAC led to the precipitation of unstable clusters, which were sedimented by centrifugation and removed from the aliquots, as well as an increase in the absolute ζ potential of the colloidally stable particle fraction. The evolution of the ζ potential between CAC and CPC showed similar trends for all sulfates with increasing salt concentration; first, colloidal stability increased with increasing ionic strength, but then decreased to |−20|–|−30| mV towards the CPC (Fig. 4b, c). The highest absolute ζ potential for every salt was observed at \(\varphi_{s}\) ≈ 0.5.
Fig. 4
Zeta potential of colloidally stable CNCs in the presence of mono- and divalent secondary sulfates as a function of ionic strength (a), as a function of the fraction of colloidally stable CNCs \(\varphi_{s}\) (b), and as normalized between CAC and CPC (c)
×
It must be noted that the stable CNC fraction was very small toward the CPC (compare to Fig. 3a, b). Considering the loss of CNCs, adding salts between the CAC and the CPC could enable fractionation of CNCs by their colloidal stability (see Supporting Information).
Figure 5 shows the hydrodynamic particle diameter of CNCs between CAC and CPC in the presence of sulfates having different cations. Increasing ionic strength has led to an overall higher z-avg compared to that of H-CNCs. This might be caused by the formation of denser clusters and elongated agglomerates due to an increasing number of contact points per particle (Moud et al. 2018). However, in our study, no correlation of hydrodynamic particle diameter and salt concentration or ζ potential was found. This result suggested that a weak cluster network with similar colloidal structures independent of the salt concentration, which has been observed by Moud et al. (2018) in CNCs in the presence of sodium chloride.
Fig. 5
Hydrodynamic apparent particle size (z-avg) of colloidally stable CNCs in the presence of mono- and divalent secondary sulfates, normalized between CAC and CPC
×
Efficiency of separation of CNCs from neutralized reactant solutions
The use of secondary sulfates for efficient CNC product separation by using the CAC and the CPC is demonstrated. For this purpose, the hydrolysis process was stopped by neutralizing the reactant solution with NH4OH, KOH, NaOH, and Ca(OH)2. Washing steps were designed according to the CAC and the CPC, determined on H-CNCs (route B).
Salt solubility (Table 1), ionic strength at the CPC, and ΔCxC determine the amount of water required during product separation (see Supporting Information). Accordingly, the final CNC concentration was highest for sulfates with monovalent cations (Table 4). Since the agglomeration behavior of CNCs does not depend on particle concentration (Phan-Xuan et al. 2016), the parameter that must be considered is the ionic strength at the CAC of the final CNC dispersion. Thus, by concentrating the intermediate sample, the method demonstrated here allows for higher final CNC concentrations and the salt-to-CNC ratio can be further reduced, yielding higher product purity.
Table 4
Concentration of colloidally stable CNCs in the product after neutralization and centrifugation, as well as the salt concentration, normalized to the relative salt-to-CNC mass ratio and the ionic strength
Counterion
cCNC /wt%
msalt mCNC−1 /g g−1
I /mM
NH4+
1.675 ± 0.026
0.193 ± 0.003
18
K+
2.525 ± 0.045
0.233 ± 0.004
25
Na+
2.254 ± 0.074
0.201 ± 0.007
13
Ca2+
0.661 ± 0.026
0.111 ± 0.004
4
Figure 6 shows the yield and colloidal properties of H-CNCs compared to CNCs produced by route B using different base solutions for neutralization. To assess the colloidal properties under equivalent conditions, CNCs produced by route B were thoroughly dialyzed.
Fig. 6
Yield and dispersion properties of H-CNCs in comparison to CNCs from neutralized and centrifuged reactant solutions
×
The yield of cellulose-to-CNC conversion was similar for each separation procedure involving sulfates with monovalent cations. The slightly lower yields of CNCs that were obtained from route B than for the production of H-CNCs were attributed to product loss during manual sample handling. The significantly lower yield for neutralization with Ca(OH)2 was attributed to the loss of intermediate product with the precipitated salt. About 13% fewer sulfate half-ester groups per unit weight of CNCs were available for neutralized CNCs compared to H-CNCs. Thus, it was not possible to remove all counterions by dialysis; further deionization could be achieved by using a strong acid exchange resin (Abitbol et al. 2013). The lower concentration of accessible sulfate half-ester groups, in conjunction with the slightly greater hydrodynamic diameter, indicated the presence of CNC agglomerates which were not entirely broken up by sonication. Lower colloidal stability of CNCs as compared to H-CNCs was also reflected in the lower absolute ζ potential of CNCs from neutralized reactant solutions.
Conclusions and outlook
The agglomeration behavior of cellulose nanocrystals extracted from ashless cotton cellulose was studied in the presence of four secondary sulfates with mono- and divalent cations from Groups 1 and 2 of the periodic table. An increase of ionic strength led to progressively greater agglomeration between the CAC and the CPC. Colloidal stability of CNCs was observed at salt concentrations below the CAC. No stable colloids formed at salt concentrations above the CPC. Both CAC and CPC varied among the different types of mono- and divalent cations. Therefore, agglomeration behavior is not attributable to electrostatic charge screening only and can be attributed to cluster formation and matching affinities. This result corroborates the hypothesis of similar agglomeration behavior of CNCs in the presence of sulfates as with that in the presence of chlorides. CAC and CPC were identified for each sulfate, and were applied in designing a neutralization-based downstream process.
Peptization of CNCs at decreasing ionic strengths limits the applicability of centrifugation for product separation after hydrolysis and dilution. Therefore, the CPC was shifted by introducing cations during neutralization of the reactant solution with NH4OH, KOH, NaOH, and Ca(OH)2. Using both the CAC and the CPC for salt removal by successive centrifugation and dilution steps facilitated efficient separation of CNCs. The validity of the CAC and the CPC at higher CNC concentrations proves their independence of the CNC concentration. Thus, the process can be further improved to demand lower water consumption as well as lower consumption of other educts by first quenching the reaction with water, and then neutralizing the remaining acid after the first centrifugation.
When the added base formed a highly soluble sulfate salt, product yields were equal to those achieved for CNCs separated by dialysis. Any salt remaining in the product from neutralized solutions affected the dispersion properties of the CNCs; however, stable colloids were obtained. Reduction of the salt-to-cellulose ratio during centrifugation would enable lower salt concentrations in the product, by scaling the cellulosic portion. But dialyzing neutralized intermediate products did not result in fully protonated CNCs, and further purification might be accomplished through the use of ion-exchange resins. When ionic traces in the product are negligible for its use case, our process reduces the need for additional effort in product purification, since most sulfates are benign.
Knowledge about the CAC and the CPC could be used for fractionating CNCs by their colloidal stability. In the original never-dried state, the salt concentration can be adjusted to control the hydrogel structure. Last, intrinsically present counterions and salts promote redispersibility of dried CNCs and the stability of pickering emulsions (Beck et al. 2012; Missoum et al. 2012; Liu et al. 2018).
Acknowledgments
The authors thank Michaela Thalhammer for her experimental contributions with Karl Fischer titrations. Moreover, we want to thank Johann Landauer for valuable discussions.
Compliance with ethical standards
Conflict of interest
The authors declare that they have no conflict of interest.
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