The fast and effective isolation of nanocellulose from selected cellulosic feedstocks

The fast and effective isolation of nanocellulose from selected cellulosic feedstocks

Accepted Manuscript Title: The fast and effective isolation of nanocellulose from selected cellulosic feedstocks ˇ Author: Matjaˇz Kunaver Alojz Anˇzl...

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Accepted Manuscript Title: The fast and effective isolation of nanocellulose from selected cellulosic feedstocks ˇ Author: Matjaˇz Kunaver Alojz Anˇzlovar Ema Zagar PII: DOI: Reference:

S0144-8617(16)30444-1 http://dx.doi.org/doi:10.1016/j.carbpol.2016.04.076 CARP 11016

To appear in: Received date: Revised date: Accepted date:

16-11-2015 15-4-2016 16-4-2016

ˇ Please cite this article as: Kunaver, Matjaˇz., Anˇzlovar, Alojz., & Zagar, Ema., The fast and effective isolation of nanocellulose from selected cellulosic feedstocks.Carbohydrate Polymers http://dx.doi.org/10.1016/j.carbpol.2016.04.076 This is a PDF file of an unedited manuscript that has been accepted for publication. As a service to our customers we are providing this early version of the manuscript. The manuscript will undergo copyediting, typesetting, and review of the resulting proof before it is published in its final form. Please note that during the production process errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain.



THE FAST AND EFFECTIVE ISOLATION OF NANOCELLULOSE FROM



SELECTED CELLULOSIC FEEDSTOCKS



Matjaž Kunaver1,*, Alojz Anžlovar1, Ema Žagar1



1



Hajdrihova 19, 1000 Ljubljana, Slovenia, Tel: +38614760363, Fax: +38614760300



*

National Institute of Chemistry, Laboratory for Polymer Chemistry and Technology,

Corresponding author: Matjaž Kunaver E-mail: [email protected]



Abstract



A new process for the production of nanocellulose from selected cellulose-containing natural



materials has been developed. The liquefaction reaction, using glycols and mild acid catalysis

10 

(methane sulphonic acid), was applied to four model materials, namely cotton linters, spruce

11 

wood, eucalyptus wood and Chinese silver grass. The process contains only four steps, the

12 

milling, the glycolysis reaction, centrifugation and final rinsing with an organic solvent. The

13 

nanocrystalline cellulose recovery was between 56% and 75%. The crystallinity index was greater

14 

than that of the starting materials due to the liquefaction of lignin, hemicelluloses and amorphous

15 

cellulose. The final product was a stable, highly concentrated nanocrystalline cellulose suspension

16 

in the organic medium. The liquid residue, after the liquefaction of the cotton linters contained

17 

significant quantities of levulinic acid. Different sugars were identified in the liquid residues that

18 

were derived from cellulose and hemicelluloses during the liquefaction reaction.

19 

1. Introduction

20 

Cellulose containing biomasses have become possible alternatives to fossil resources for

21 

chemicals manufacture and for fuel production, cellulose being the most abundant polymer in

22 

nature. Cellulosic resources include agricultural residues (wheat straw, corncobs, sugarcane

23 

bagasse, corn stover), forest residues and energy crops (hardwood and softwood sawdust, silver

24 

grass), municipal and industry wastes (waste paper waste cotton textiles and waste timber-based

25 

materials). Low cost cellulosic materials represent a feasible option for the production of

26 

materials that carry a higher added value.

27 

Most of the low-value lignocellulosic biomasses consist of cellulose, hemicelluloses and lignin

28 

(Fengel and Wegener 1989). The inner structure contributes to the hydrolytic stability and

29 

structural robustness. Cellulose, as a bulk material, acts as a framework, based on highly oriented

30 

cellulose fibrils. Cellulose is complex in its chemical composition and its intra- and

31 

intermolecular hydrogen bonding. Within the cellulose fibrils there are highly ordered regions,

1   

32 

less well ordered regions and relatively highly disordered regions. The ordered (more crystalline)

33 

regions can be extracted, resulting in the creation of nanocrystalline cellulose (NCC).

34 

The crystallinity index of cellulose has been used to describe its relative amount of crystalline

35 

material and has been determined by several methods (Terinte et al., 2011). In general, the

36 

crystallinity index varies from 33 to 60 (Thygesen et al. 2005). Nanocrystalline cellulose, used as

37 

a reinforcing material in nanocomposites, has been the subject of research worldwide (Habibi et

38 

al. 2010). Besides its low cost, renewability, light weight and high aspect ratio, NCC has a high

39 

modulus of elasticity and considerable tensile strength. These are the reasons for its incorporation

40 

into many promising synthetic and natural polymeric matrices (Khalil et al. 2012), for its use in

41 

different packaging material applications (Ridgway and Gane 2012), as well as in automobile

42 

transportation and drug delivery applications (Lam et al. 2012).

43 

The isolation of nanocellulose has been studied by many authors since the first isolation of

44 

cellulose nanofibrils (Turbak et al. 1983). Favier et al. (1995) have reported on the properties of

45 

nanocomposites containing cellulose whiskers, from which time the number of published results

46 

related to nanocellulose isolation, its use in different composites and in different applications has

47 

grown annually(Klemm et al. 2005).

48 

Several processes have been developed for the NCC isolation. These include:

49 



Mechanical pulping, mostly of wood (Chakraborty et al. 2005),

50 



Chemical pulping, where lignin is removed by a Kraft process (Jiang and Hsieh 2013),

51 



Steam explosion, resulting in the breakdown of the biomass structure, the hydrolysis of hemicelluloses and lignin and defibrillation (Abraham et al. 2011),

52  53 



Acid hydrolysis with sulphuric acid, hydrochloric acid and, more seldom used, phosphoric acid and hydrobromic acid (Brinchi et al. 2013),

54  55 



56 

cellulose (Kos et al. 2014 and Li et al. 2011).

57 

The most common method of choice of processing towards NCC isolation is acid hydrolysis.

58 

Typically, the cellulose fibers are subjected to strong acid hydrolysis under the controlled

59 

conditions of temperature, acid concentration, agitation and time. Kos et al. (2014) applied

60 

microwaves to shorten the reaction time of the acid hydrolysis process to only ten minutes. Also,

61 

by varying the sulphuric acid concentration, they were able to control the NCC average

62 

dimensions. Experiments dealing with the isolation of NCC from different natural sources and

63 

details outlining experimental conditions have been published in recent years. Thus, Dai et al.

Microwave  assisted  hydrolysis  or  high  intensity  ultrasonication  of  microcrystalline 

2   

64 

(2013) isolated nanocellulose from hemp fibers using dodecyltrimethylammonium bromide and

65 

ultrasonic agitation. Johar et al. (2012) processed rice husks, using an alkaline pre-treatment,

66 

coupled with bleaching and acid hydrolysis steps. Fan and Li (2012) have studied the influence of

67 

the reaction temperature, the time and the sulphuric acid concentration on isolated yields of NCC

68 

from cotton pulp fibers. Mandal and Chakrabarty (2011) prepared NCC from waste sugarcane

69 

bagasse by delignification, the removal of hemicelluloses and sulphuric acid-based hydrolysis.

70 

Nascimento et al. (2014) used a similar process for the isolation of NCC from white coir. Also, Li

71 

et al., (2011) used a similar process for the isolation of NCC from bleached softwood Kraft pulp.

72 

The use of different acids (hydrochloric acid (Yu et al. 2013), phosphoric acid (Espinosa et al.

73 

2013), hydrobromic acid (Sadeghifar et.al 2011) and p-toluenesulphonic acid (Anžlovar et.al.

74 

2016) is quoted in the literature, but mostly aqueous sulphuric acid solutions, in concentrations

75 

above 60%, have been used. Although very little information concerning yields obtained is

76 

available, most of these authors have determined that the increase in crystallinity index of

77 

products have been significant, namely from 77 for cotton fibers to 91 for the isolated NCC

78 

(Teixeira et al. 2010); the average dimensions of the nano crystals being between 250 nm and 600

79 

nm in length and from 4 nm to 70 nm in diameter.

80 

Although attempts to convert cellulose into useful chemicals, in an aqueous medium, have been

81 

made over an extended period, the liquefaction of lignocellulosic biomass has been known for an

82 

even longer period. Liquefied lignocellulosic materials have been considered to be an important

83 

feedstock for the creation of polymeric blends and derivatives/composites, options having been

84 

described by several authors including Kunaver et al. (2010); Lin et al. (1994), and Hassan and

85 

Shukry (2008). The products have been used as polyols in polyurethane reactions (Chen and Lu

86 

2009), as adhesives (Kunaver et al. 2010a; Juhaida et al. 2010) and as a fuel for gas turbines

87 

(Seljak et al. 2012).

88 

This paper concerns the process of preparing NCC from different natural sources by a

89 

liquefaction reaction, using glycols as the main reactant and an acid catalyst in low concentration.

90 

Here, during the one step reaction, lignin, hemicelluloses and the more disordered components of

91 

the cellulosic fibers are liquefied, only the crystalline cellulose remaining as a solid residue.

92 

Compared to the well-known acid hydrolysis-based procedure, a loading of only 3% of acid was

93 

used. The yields, crystallinity index and morphology of thus produced NCC were comparable to

94 

those NCC products that were described in recently published papers.

95  96 

2. Materials and methods

97 

2.1. Materials 3   

98 

Cellulose linters and wood sawdust were provided by GGP (Gozdno Gospodarstvo Postojna,

99 

Slovenia). Methane sulfonic acid was supplied by Arkema, France. All of the other reagents were

100 

supplied by Sigma-Aldrich (>98 %, GC, Reagent Plus). The Chinese silver grass (Miscanthus

101 

sinensis) was obtained from the experimental plantation of Petrović U., Ljubljana, Slovenia. The

102 

Eucalyptus wood chips (Eucaliptus globulus) were provided by Agronelli Agroindustria, Uberaba

103 

Brasil. The samples were dried to 10 % (w/w) of water content in a laboratory oven and milled to

104 

2 mm particles using a RETSCH SM-2000 mill in conjunction with a 2 mm grinding mesh. Wood

105 

sawdust was dried in a laboratory oven to 10 % (w/w) in its water content and sieved through 5

106 

mm mesh sieve. The chemical composition of cellulose-containing materials was determined

107 

according to standard methods (TAPPI T222 om-11, TAPPI T211 om-12, TAPPI T204 cm-07,

108 

TAPPI T207 cm-08, TAPPI T203 om-09, TAPPI T223 cm-10). The composition of materials that

109 

were used in these experiments is presented in Table 1.

110 

Table 1. The composition of the materials and their crystallinity index.

Biomass 

111 

Hemicelluloses  Cellulose  (%)  (%) 

Lignin  (%) 

Extractive s (%) 

Ash  (%) 

Crystallinity  index (CrI) 

Cotton linters 

7.1±0.7 

81.3±4.2 

2.5±0.4 

6.3±0.9 

2.8±0.1 

64±7 

Spruce wood 

29.6±2 

42.3±3 

26.9±5 

0.9±0.9 

0.3±0.1 

47±5 

Chinese silver  grass 

33.9±4.4 

47.1±6.0  10.5±4.7 

5.6±1.3 

2.9±0.5 

46±7 

Eucalyptus  wood 

26.9±1.8 

44.3±3.1  26.1±2.0 

2.3±0.2 

0.4±0.2 

57±4 

Data reported are on a dry matter basis.

112  113 

2.2. Biomass liquefaction and NCC isolation

114 

In each case, the diol or glycerol or a mixture of the two types, (300 g) and methane sulphonic

115 

acid (9 g) were placed into a 1000 cm3 three-necked reactor, equipped with mechanical stirring.

116 

The mixture was heated to 150 oC and was stirred constantly. After the milled biomass had been

117 

added to the preheated reaction mixture, the liquefaction process was carried out for 180 minutes.

118 

The polyhydroxy alcohols used in the liquefaction reaction were diethylene glycol, ethylene

119 

glycol, glycerine and mixtures of these alcohols. Typically, a ratio of 4:1 between the glycol (or

120 

glycerol) and the biomass was used. 3% of methane sulfonic acid was added (calculated on the

121 

amount of the glycol). The reaction temperature was maintained at 150 oC. These reaction 4   

122 

conditions were chosen according to the previous experience in the liquefaction of wood and

123 

similar biomasses (Jasiukaitytė et al. 2012; Kunaver et al. 2012).

124 

The reaction mixture was cooled to room temperature, diluted 1:1 with 1,4-dioxane and

125 

centrifuged at 8000 rpm for 20 minutes. The sediment was dispersed in 1,4-dioxane and

126 

centrifuged using the same conditions. The process of re-dispersion and centrifugation was

127 

repeated three to five times until a clear supernatant liquid was obtained. Finally, the sediment

128 

was dispersed in 1,4-dioxane, with additional sonication for 10 minutes (Ultrasonic Processor

129 

UP400S, Hielscher). The product was a 15% to 20% (w/w) suspension of NCC in 1,4-dioxane.

130 

A diluted suspension of NCC was centrifuged at 8000 rpm for 30 minutes to separate the

131 

nanocrystals from the liquefied products in the supernatant liquid. The yield, (Y) of the NCC

132 

isolation was calculated according to the mass of the solid residue, obtained after rinsing and

133 

centrifuging the products that were obtained after the liquefaction reaction, taking into account

134 

the crystallinity index of the initial cellulose.

Y [%] =

135 

m ⋅ 100 % Sc %Cell Cr I M⋅ ⋅ . 100 100 100

Equation 1

136 

Here, m denotes the mass of dry product, M denotes the initial mass of the original sample, %Sc is

137 

the initial solids loading in the reaction mixture, %Cell is the cellulose content in the starting

138 

material and CrI is the crystallinity index (%) of the starting material.

139 

2.3.

140 

2.3.1. X-ray diffraction (XRD)

141 

The NCC samples were characterized by wide-angle X-ray diffraction using a XPert PRO MPD

142 

diffractometer from PANalytical with a Cu anode as the X-ray source, at wavelength Cu Kα1:

143 

1.5406 Å. Diffractograms were measured at 25 oC in the 2-theta range from 5o to 40o, with a step

144 

of 0.04o and step time of 300 s. The crystallinity index was calculated according to the Segal

145 

method (Segal et al. 1959) from the ratio of the height of the 002 peak (Ioo2) and the minimum

146 

between 002 and the 101 peaks, subtracted from the background signal that was measured

147 

without cellulose. It should be noted that the Segal method suffers some inaccuracy due to the

148 

inaccurate amorphous peak position, and, consequently the influence of the amorphous material

149 

present in the sample is underestimated. Four crystalline peaks are shown. However, only the

150 

highest (002) peak is used in calculation. None-the less, this much simplified method is suitable

151 

for use when comparing the relative differences between samples. In order to obtain more reliable

152 

results for the crystallinity index, two additional methods were applied namely, the Segal

Characterization

5   

153 

calculation using “the amorphous peak method, at 21o “ (Terinte et al. 201, Park et al. 2010) and

154 

the amorphous subtraction method, for which alkali lignin was used as the amorphous reference

155 

standard (Agarwal et al. 2011). The crystallite sizes were estimated by using well known Scherrer equation (Klug and

156  157 

Alexander 1974):

Dhkl =

158 

Kλ βhkl ⋅ cos Θ

Equation 2

159 

Here, Dhkl is the crystallite size, K is the Scherrer constant (being 1 for needle-like crystals),

160 

(Smilgies 2009), λ is the wavelength of the radiation used (0.15406 nm) and βhkl is the width at

161 

half-maximum of the diffraction peak angle of the (002) crystal plane. The βhkl peak fitting was

162 

performed prior to calculation of crystallite size.

163 

2.3.2. Dynamic light scattering (DLS)

164 

The average hydrodynamic diameter of the species in the aqueous NCC suspensions was

165 

determined by dynamic light scattering at 25 oC, using a Malvern Zetasizer Nano-ZS, (Malvern

166 

Instruments Ltd.) The instrument was calibrated using a Thermo Scientific Nanosphere Size

167 

standard. For the diameter values and for the size distribution measurements, the NCC

168 

suspensions were diluted by 100x with deionized water and sonicated for at least 5 minutes,

169 

(Ultrasonic Processor UP400S, Hielscher).

170 

2.3.3. Scanning Transmission Electron Microscopy (STEM) and Scanning Electron

171 

Microscopy (SEM)

172 

The microtopographies of NCC samples were observed by STEM. The STEM micrographs were

173 

taken on a Zeiss Supra 35 VP at an acceleration voltage of 20.0 kV and a working distance of

174 

4.5–5.0 mm, using a STEM electron detector. Samples for the STEM measurements were

175 

prepared by the drop-casting of a 100x diluted NCC suspension in acetone. Prior the drop-casting

176 

procedure, the NCC suspensions were sonicated for 10 minutes (Ultrasonic Processor UP400S,

177 

Hielscher). The same suspensions were applied to a glass substrate from which the acetone

178 

quickly evaporated. The dried glass support with its NCC particles on the surface was then coated

179 

with gold and used for SEM observations.

180 

2.3.4. Thermogravimetric analysis (TGA)

181 

TGA analyses of dry samples were performed on a Mettler-Toledo TGA/DSC 1 instrument. Each

182 

sample (5 mg) was heated at 10 oC/min from 30 oC to 800 oC, under N2 purging (50 mL/min).

6   

183 

2.3.5. Fourier transform infrared spectroscopy (FTIR)

184 

FTIR analyses of dry samples were performed on a Perkin Elmer Spectrum 1 instrument using

185 

KBr technique. The dried NCC powders were embedded in KBr pellets and the absorption spectra

186 

were recorded in the range of 4000 cm-1 to 400 cm-1. The FTIR spectra were used for the

187 

determination of the crystallinity, as described by Nelson and O’Connor (1964). Here, the ratio

188 

between the 1731 cm-1 absorption band and the 2900 cm-1absorption band gives the crystallinity

189 

index of the sample.

190 

2.3.6. Gas chromatographic measurements

191 

The amount of levulinic acid in the reaction mixture was determined using an Agilent 6890N gas

192 

chromatograph, coupled with the mass selective detector, Agilent 5973N. Thus, 0.1 g of the

193 

sample was put into a 20 mL vial. 3 mL of the BF3/methanol reagent (Merck) was added and the

194 

vial sealed. The vial was heated at 80 oC for 60 minutes. 3 mL of chloroform and 5 mL of water

195 

were added and the mixture well shaken. The resulting methyl ester of levulinic acid was

196 

extracted into the chloroform layer, which was then used for the analysis.

197 

The hydroxyl group-containing components of the reaction mixture were analysed as trimethyl

198 

silyl ether derivatives. The etherification was performed according to the method described by

199 

Esposito and Swann (1969).

200 

Gas chromatographic analyses were performed using a DB-35MS column of 30 m in length and

201 

0.25 mm in I.D. The temperature program was 4 minutes, with an initial temperature of 50 oC,

202 

then heating to 250 oC at 30oC/min with holding for 10 minutes at the final temperature. 2uL of

203 

the sample was injected with a Split 100:1 mode. Mass spectra were collected within the 33 – 550

204 

mass range. The Wiley mass spectra library (Wiley 1999) was used for the identification of the

205 

methyl ester of levulinic acid and of the trimethyl silyl ether derivatives of the hydroxyl group

206 

containing components.

207  208 

3. RESULTS AND DISCUSSION

209 

3.1. Nanocellulose yields

210 

First, the efficiency of the biomass liquefaction process, with respect to the yields of NCC

211 

obtained, was studied by changing the reaction temperature, the reaction time and the reagent

212 

composition. The choice of the polyhydroxy alcohol, the acid catalyst loading and the glycol to

213 

lignocellulosic material ratio that was used was that optimized by Jasiukaitytė et al. (2012). The

214 

results show that there was little deviation in the yields of the NCC recovery across the changes 7   

215 

made to the process parameters. The temperature of the reaction was 150 oC, while the ratio of the

216 

glycol to cellulose-containing-material was kept constant at 1:4. The choice of polyhydroxy

217 

alcohol selection did not influence significantly the yields of the reactions. The acid catalyst

218 

loading was kept constant and was not below 3%, calculated on the glycol content. The initial

219 

water that was present in the wood or other biomass materials evaporated within the first few

220 

minutes of the reaction, since the temperature was sufficiently high. All of the samples in this

221 

study were obtained through the same preparation route. The % recovery of the nanocrystalline

222 

cellulose, the crystallinity index of the nanocrystalline cellulose and the average crystal width are

223 

presented in the Table 2. The yields are moderate and differ due to different cellulose content in

224 

the original material. Additionally, the cell structure might also influence the efficiency of the

225 

reaction. That would explain the low yield that was obtained when the Chinese silver grass was

226 

liquefied.

227  228 

Table 2. The % recovery of NCC, the crystallinity index, the average crystal length and crystal width.

Biomass 

Average  length 

 (%) 

Crystallinity  index (CrI)a 

of NCC(nm)b 

Average NCC  crystal width (nm)c 

74.5±6.0 

80% 

242±8 

12.7±0.4 

Spruce wood 

61.5±3.2 

63% 

235±23 

8.9±0.1 

Chinese  silver grass 

55.6±4.0 

62.8% 

250±17 

8.9±0.2 

Eucalyptus  wood 

63.0±8.5 

66% 

306±13 

9.0±0.1 

Cotton 

NCC recovery 

linters 

229 

a

230 

b

231 

c

232 

The liquefaction temperature was lower than that previously reported in the published literature

233 

(Kunaver et al. 2010) in order that greater yields of NCC might be obtained. The reaction yields

234 

decreased on increasing the reaction temperature to greater than 150 oC.

235 

3.2. DLS measurements

The crystallinity index was calculated using the Segal 21-WAX method The length of the NCC crystals was evaluated from the SEM micrographs.

The width of the NCC crystals was estimated by using the Scherrer equation.

8   

236 

The results of the DLS measurements can be related to the Brownian motion of the nanoparticles

237 

in the medium. The value given by this technique is the radius of a sphere having the same

238 

diffusion coefficient as the rod-like NCC particles. The method is suitable for the rapid evaluation

239 

of the NCC average particle size. However, correlations with data obtained from the STEM

240 

micrographs were needed. The average lengths are within the range observed by Fan and Li

241 

(2012) and by Brinchi et al. (2013).

242 

The obtained average hydrodynamic diameter of the NCC particles was similar regardless to the

243 

origin of the particles. The samples were dispersed in water prior the measurements, almost

244 

immediate agglomeration being observed. This process was partly avoided by the

245 

ultrasonification of each sample just prior the measurement taking place. 5 % to 8 % (by

246 

intensity) of the aggregates was always detected, their average size being between 3000 nm and

247 

4000 nm.

248 

The average particle size for different time intervals during the reactions was also measured by

249 

DLS. The results are shown in Figure 1.

250  251 

Figure 1. Average hydrodynamic diameter of the NCC particles size vs. the reaction time (min)

252 

used: eucalyptus (a), Chinese silver grass (b), cotton linters (c) and spruce wood (d).

253 

In each instance, for each polysaccharide source, the relationship is almost linear, from 292 nm

254 

after 60 minutes of reaction time for wood to 125 nm at the end of the reaction. Here, only nano-

255 

sized particles were taken into consideration. It is evident from these results that during the

256 

liquefaction reaction, the average particle size was reduced. The average particle sizes differ at 60

257 

minutes of reaction time due to the differences in the particle sizes of the starting materials, 9   

258 

namely that the wood particles were in a shape of needles up to 5 mm length whilst the Chinese

259 

silver grass and eucalyptus particles were taken as a mixture of dust and smaller particles, up to 3

260 

mm in length. Here, the lignin and hemicellulose content might have influenced the speed of the

261 

size reduction during the reaction. Longer reaction times and higher temperatures could result in

262 

the complete dissolution of nanocellulose particles (Jasiukaitytė et al. 2012). Large aggregates

263 

and cellulose fibrils that did not dissolve in the earlier stages of the reaction were identified in the

264 

spruce wood distribution patterns. As the reaction progressed, the average hydrodynamic

265 

diameter distribution became narrower and more uniform. Typical DLS hydrodynamic size

266 

distributions are shown in Figure 2, the small peak at 4770 nm indicating the presence of large

267 

aggregates.

268 

 

269 

Figure 2. Hydrodynamic size distribution of NCC isolated from selected cellulose sources at

270 

different reaction times

271 

When the NCC was dispersed in water, aggregation was immediately observed. The addition of a

272 

suitable surfactant, such as Tween 85 helped to keep the suspension stable during the DLS

273 

measurements although it was not possible completely to avoid the presence of a small amount of

274 

aggregates.

275 

3.3. SEM and STEM microscopy evaluations

276 

Figure 3 shows the SEM micrograph of rod-like nanocrystalline cellulose particles, as derived

277 

from cotton linters, Chinese silver grass, spruce wood and eucalyptus wood. The highly diluted

278 

suspension was prepared in acetone, using ultrasonification. A drop of suspension was put on the

279 

glass support from which the acetone evaporated. The length of the NCC fibers was 220 nm to

280 

300 nm and their diameter 14 nm to 23 nm, the average aspect ratio being 15. Although small

10   

281 

aggregates and nanofiber-like structures were formed during the evaporation of the acetone, the

282 

individual NCC particles were able to be observed and measured.

283 

Evaluations of the NCC particles’ dimensions confirmed the values that were obtained from the

284 

SEM micrographs. The values are also comparable to the results emanating from the DLS study.

285 

The differences between the SEM derived results and the DLS derived measurements may arise

286 

from the fact that the DLS-technique measures the hydrodynamic diameter of a sphere having the

287 

same diffusion coefficient as the rod like NCC in suspension, while the SEM technique gives the

288 

actual particle dimensions. The morphology of NCC particles differs across the samples. The

289 

NCC crystals derived from the cotton linters are more separated while the NCC crystals from

290 

other three samples form a structure that is similar to those of nanofibers. The length and the

291 

width of all of the NCC samples is similar. The STEM micrograph representing the cotton linters

292 

NCC sample is shown in Figure 1 S1 of the Supplementary materials.

 

293  294 

Figure 3. SEM micrographs of NCC: cotton linters (a), chinese silver grass (b), spruce wood (c)

295 

and eucalyptus wood (d).

296 

3.4. X-ray diffraction measurements

297 

The crystallinity index and the values of the average diameter of the NCC particles are presented

298 

in Table 2, the corresponding diffractograms being shown in Figure 4. The diffractograms

299 

display their main peak at 22.8o, being characteristic of cellulose I. The reported crystallinity

300 

index of cotton linters is 64.4%, (Morais J.P.S. et al. 2013). The crystallinity index of the NCC

301 

that was isolated from cotton linters was much greater (80%). This is because all of the disordered

302 

sections would have been dissolved during the reaction while the more highly ordered crystalline 11   

303 

regions would be more resistant to attack by the reagents. The crystallinity Miller’s indices 1Ī0,

304 

110 and 200 are parallel to those of the cellulose chains and are well defined in the X-ray

305 

diffraction patterns. The crystallinity index was calculated using Segal 21-WAX method.

306 

Although this method gives greater values than those obtained using other methods such as the

307 

peak deconvolution method or the amorphous subtraction method, it is very convenient in its use,

308 

particularly when comparing the products. Similar results were obtained with Chinese silver

309 

grass, spruce wood and eucalyptus, with crystallinity index values in the range from 62.8% to

310 

66%, although the crystallinity reflexions other than 200 were less explicit. These results show

311 

lower values for the crystallinity index, most likely because the initial nanocrystalline cellulose

312 

loading was much lower in the starting material, due to the presence of a certain proportion of the

313 

amorphous nanocellulose as a nanofiber and because the side products remained adsorbed on the

314 

surface of the nanocrystals even after several rinsing operations had been carried out, thus

315 

influencing the diffractogram in the amorphous region. This point is also indicated by slight

316 

coloration of NCC suspension that was obtained from spruce wood and Chinese silver grass due

317 

to the greater amount of lignin determined in the starting material (Figure 5, S1 of the

318 

Supplementary materials). The data obtained from different methods for the crystallinity

319 

determination are presented in the Table 1 S1of the Supplementary materials.

320  321 

Figure 4. XRD diffractograms of NCC: cotton linters(a), Chinese silver grass (b), spruce wood (c)

322 

and eucalyptus wood (d).

12   

323 

The average diameter was calculated according to the Scherrer equation. The calculated values

324 

are less than those observed from the SEM micrographs. Measurements from micrographs are

325 

less accurate due to the lower resolution and the fact that very few single crystallites were found.

326 

The authors calculated the average diameter, (the Scherrer equation approach), after the

327 

glycolysis of the products of the different cellulose sources, under the similar reaction conditions.

328 

The values obtained were between 8.9 nm and 12.7 nm.

329 

3.5. Thermal stability of nanocrystalline cellulose

330 

All of samples gave an initial weight loss at low temperatures (below 110 oC), mainly due to

331 

water loss. (Figure 2 S1 of the Supplementary materials). The thermal degradation onset

332 

temperature, (To) and the maximum decomposition temperature, (Tmax) are presented in Table 3.

333 

Values for raw cotton linters are included in order to show the significant difference between Tmax

334 

of nanoparticles and that of the raw cotton fibers. It is clear that the nanoparticles have a greater

335 

surface area compared with those of the cellulose fibers, leading to a greater surface area being

336 

exposed to the heat. The Tmax value of the analysed samples is in direct correlation with the

337 

measured crystallinity index, being the lowest for cotton linters (284.6 oC), with a crystallinity

338 

index of 89% and the highest for spruce wood (326.1 oC), with a crystallinity index of 68%. The

339 

decrease of the Tmax has been explained in some literature sources ( Li et al. 2011 ) as being due

340 

to the presence of sulphate groups, which would significantly lower the degradation temperature

341 

of NCC. This is because the elimination of any sulphate groups results in the occurrence of a

342 

lesser activation energy. The additional elemental analyses and 1H NMR analyses proved the

343 

presence of only trace quantities of sulphur and sulphonate groups in all of the NCC samples.

344 

Thus, the main reason for the Tmax decrease is the larger surface area of NCC crystals. The same

345 

reasoning applies to the char residues. A greater quantity of char was generated when the NCC

346 

from cotton linter was analysed. The reason may be due to the greater proportion of carbon in

347 

highly crystalline sample.

348 

3.6. FTIR analysis of NCC dry powders

349 

The relevant FTIR spectra are presented as Figure 3 S1 of the supplementary material. These

350 

show clearly that neither hemicelluloses nor lignin are present in the products. The FTIR spectra

351 

of all of the samples are practically identical, indicating that there are minimal differences in their

352 

chemical composition. Thus, bands at 1597 cm-1 and 1506 cm-1 (aromatic C-H out-of-plane

353 

vibrations of lignin) are missing. Also the band at 1735 cm-1, which is ascribed to the C=0

354 

stretching of the acetyl group in hemicelluloses is missing. The absorption band at 2900 cm-1 is

355 

associated with C-H stretching, signals at 1431 cm-1 and 1372 cm-1 are attributed to CH3, CH2 and

356 

CH stretching and bending. The signals at 1164 cm-1, 1113 cm-1 1060 cm-1 , C-O-C stretching

357 

and 898 cm-1 are attributed to glycosidic -C-O-C- deformation which is characteristic of the β13   

358 

glycosidic link in cellulose. The ratio between two adsorption bands, namely 2900 cm-1 and 1371

359 

cm-1 was used to determine the crystallinity index determination. The results are presented in the

360 

Table 1 S1 of the supplementary material. The accuracy of the method was checked by

361 

calculating the crystallinity index of an amorphous lignin standard, producing a value of 21.8%,

362 

which is unacceptable. The same standard sample was analyzed using XRD and was shown to be

363 

100% amorphous.

364 

3.7. Gas chromatographic analysis of liquid residue

365 

In order to identify the major components of the liquid residues, obtained after the isolation of the

366 

NCC species, the methyl esters of the acidic components and trimethyl silyl ethers of the

367 

hydroxyl groups containing components were synthesised. The GC/MS chromatogram of each of

368 

the methyl esters is presented in Figure 5. The main component is the methyl ester of levulinic

369 

acid, identified by comparing the MS spectrum with the reference spectrum from Wiley MS

370 

spectra library. When using cotton linters as the starting material, the yield of levulinic acid was

371 

between 7% (w/w) and 9% (w/w).  

372 

 

373 

Figure 5. The GC/MS chromatogram of the liquid residue, obtained after the isolation of NCC

374 

from selected materials. The methyl ester of levulinic acid was identified at 6.95 minutes.

375 

When using spruce wood or Chinese silver grass, the yield was between 3%(w/w) and 4%(w/w).

376 

The lowest yield was achieved with eucalyptus wood (2.7%). The yield depends on the cellulose

377 

loading of the starting material, being the greatest in the cotton linters and the least in eucalyptus

378 

and spruce wood. The depolymerisation of cellulose was monitored in detail, according to the

14   

379 

study of Yamada and Ono (2001), who observed that the first step is the formation of diethylene

380 

glycol glucoside, which further decomposes to levulinic acid. When dealing with wood or similar

381 

lignocellulosic materials, some sugars derived from hemicelluloses were identified as was some

382 

glucose. The major products of the depolymerisation of the hemicelluloses were xylose and

383 

furfural, with mannose in smaller quantities. The GC/MS chromatogram of the trimethylsilyl

384 

ethers is presented as Figure 4 S1 of the supplementary materials. Here, the trimethyl silyl ethers

385 

of sugars were identified at retention times from 10.65 minutes to 11.35 minutes, by comparing

386 

the MS spectra with the reference spectra given in the Wiley MS spectra library. The total amount

387 

of sugars present in the residual liquid was obtained by quantitative GC/MS analysis. The results

388 

are presented in Table 3. A greater value for the cotton linters sample was expected but the

389 

GC/MS analysis showed that conversion into the levulinic acid predominated.

390 

Table 3. The GC/MS determination of sugars present in the residual liquid and thermal

391 

parameters for the NCC samples and raw cotton linter.

392 

Biomass 

Total sugars 

To   o

a

Tmax   o

a

Residue  

(mg/g) 

( C)  

( C)  

(%) 

Cotton linter 

16.08±1.4 

249.7 

284.6 

24.1 

Spruce wood 

14.59±1.2 

299.3 

326.1 

22.3 

Chinese silver grass 

10.65±1.0 

268.6 

301.7 

21.5 

Eucalyptus wood 

10.13±0.9 

290.1 

322.5 

20.9 

Raw cotton linter 

‐ 

314.4 

362.5 

17.9 

393 

a

394 

It is possible to isolate the levulinic acid selectively from liquid residues using alkyl phenolic

395 

solvents, as indicated by Alonso et al. (2011).

396 

The sugars that were identified in the liquid residue from the wood liquefaction process could be

397 

used as a feedstock for several fermentation processes in ethanol production (Singh et al. 2014,

398 

Koller et al. 2015). Also, the liquid residues could be used as a source of a range of valuable

399 

chemicals such as gamma-valerolactone and hydroxymethyl furfural (Wettstein et al. 2012).

To and Tmax were calculated from TGA profiles.

400  15   

401 

4. Conclusions

402 

The liquefaction with glycols, using methane sulphonic acid as a catalyst has been employed in

403 

attempts at simplifying the process of NCC production. The whole process contains only four

404 

steps, the milling, the glycolysis reaction, centrifugation and final rinsing with an organic solvent.

405 

The yields and the crystallinity indices obtained were in the range of published methods in which

406 

hydrolysis with sulphuric acid was used. During the one step glycolysis reaction, lignin,

407 

hemicelluloses and the more disordered components of the cellulosic fibers were liquefied, only

408 

the crystalline cellulose remaining as a solid residue. The nanocrystalline cellulose recovery was

409 

between 56% and 75%. Compared to the well-known acid hydrolysis-based procedure, a loading

410 

of only 3% of acid was used. Product isolation and cleaning was achieved by simple

411 

centrifugation and rinsing with 1,4-dioxane. The method can be applied to different cellulose-

412 

containing biomasses. The main benefit of the process arises from the ability to prepare stable

413 

NCC suspensions in an organic medium at 10 times greater loadings than can be achieved in

414 

aqueous suspensions. The thermal stability of all of the NCC samples is less than that of the

415 

starting material due to the greater surface area of nanocrystals and is in good correlation with the

416 

crystallinity index. The liquid residues contain significant quantities of levulinic acid and

417 

different sugars that were derived from cellulose and hemicelluloses.

418  419 

Acknowledgments

420 

The authors gratefully acknowledge the Slovenian research Agency for financial support

421 

(program P2-0145).

422  423 

References

424 

Abraham, E., Deepa, B., Pothan, L.A., Jacob, M., Thomas, S., Cvelbar, U., Anandjiwala, R.

425 

(2011). Extraction of nanocellulose fibrils from lignocellulosic fibers: A novel approach.

426 

Carbohydrate Polymers, 86, 1468-1475.

427 

Agarval, U.P., Reiner, R.R., Ralph, S.A. (2011). Cellulose crystallinity of woods, wood pulps,

428 

and agricultural fibers by FT-Raman spectroscopy. Proceedings of the 16th ISWFPC, Tianjin,

429 

China.

430 

Alonso, D.M., Wettstein, S.G., Bond, J.Q., Root, T.W., Dumesic J.A. ( 2011). Production of

431 

biofuels from cellulose and corn stover using alkylphenol solvents. ChemSusChem, 4, 1078-

432 

1089. 16   

433 

Anžlovar, A., Huskić, M., Žagar, E. (2016). Modification of nanocrystalline cellulose for

434 

application as a reinforcing nanofiller in PMMA composites. Cellulose, 23, 505-518.

435 

Brinchi, L., Cotana, F., Fortunati, E., Kenny, J.M. ( 2013). Production of Nanocrystalline

436 

cellulose from lignocellulosic biomass: Technology and applications. Carbohydrate Polymers, 94,

437 

154-169.

438 

Chakraborty, A., Sain, M., Kortschot, M. (2005). Cellulose microfibrils: A novel method of

439 

preparation using high shear refining and cryocrushing. Holzforschung, 59, 1, 102-107.

440 

Chen, F., Lu, Z. (2009). Liquefaction of wheat straw and preparation of rigid polyurethane foam

441 

from liquefaction product. Journal of Applied Polymer Science, 111, 508-516.

442 

Dai, D., Fan, M., Collins P. (2013). Fabrication of nanocellulose from hemp fibers and their

443 

application for the reinforcement of hemp fibers. Industrial Crops and Products, 44, 192-199.

444 

Espinosa, S.C., Kuhnt, T., Foster, E. J., Weder, C. (2013) Isolation of Thermally Stable Cellulose

445 

Nanocrystals by Phosphoric Acid Hydrolysis. Biomacromolecules, 14, 1223–1230.

446 

Esposito, G.G., Swann, H.M. (1969). Gas chromatographic determination of polyhydric alcohols

447 

in oils and alkyd resins by formation of trimethylsilyl derivatives. Analytical Chemistry, 41,

448 

1118-1120.

449 

Fan, J., Li, Y. (2012). Maximizing the yield of Nanocrystalline cellulose from cotton pulp fiber.

450 

Carbohydrate Polymers, 88, 1184-1188.

451 

Favier, V., Chanzy, H., Cavaillé, J.Y. (1995). Polymer nanocomposites reinforced by cellulose

452 

whiskers. Macromolecules, 28, 6365-6367.

453  454 

Fengel, D., Wegener, G. (1989). Wood – Chemistry, ultrastructure, reactions. (2nd ed.)  Berlin,  New York: Walter de Gruyter, ISBN 3‐11‐008481‐3 

455 

Hassan, E., Shukry, N. (2008). Polyhydric alcohol liquefaction of some lignocellulosic

456 

agricultural residues. Industrial Crops and Products, 27, 33-38.

457 

Habibi, Y., Lucia, L.A., Rojas, O.J. (2010). Cellulose nanocrystals: chemistry, self-assembly, and

458 

applications. Chemical Reviews, 110, 3479-3500

459 

Jasiukaitytė, E., Kunaver, M., Poljanšek, I. (2012). Influence of cellulose polymerization degree

460 

and crystallinity on kinetics of cellulose degradation. Bioresources, 7, 3, 3008-3027.

461 

Jiang, F., Hsieh, Y-L. (2013). Chemically and mechanically isolated nanocellulose and their self-

462 

assembled structures. Carbohydrate Polymers, 95, 32-40. 17   

463 

Johar, N., Ahmad, I., Dufresne, A. (2012). Extraction, preparation and characterization of

464 

cellulose fibers and nanocrystals from rice husk. Industrial Crops and Products, 37, 93-99.

465 

Juhaida, M.F., Paridah, M.F., Hilmi, M.T., Sarani M.M., Jalaluddin H., Mohamadzaki A.R.

466 

(2010). Liquefaction of kenaf (Hibiscuscannabinus L.) core for wood laminating adhesive.

467 

Bioresource Technology, 101, 1355-1360.

468 

Khalil, H.P.S.A., Bhat, A.H., Yusra, A.F.I. (2012). Green composites from sustainable cellulose

469 

nanofibrils: A review. Carbohydrate Polymers, 87, 963-979.

470 

Klemm, D., Heublein, B., Fink, H.P., Bohn, A. (2005). Cellulose: fascinating biopolymer and

471 

sustainable raw material. Angewandte Chemie, 44, 3358-3393.

472 

Klug, H.P., Alexander, L.E. (1974). X-ray diffraction procedures: For polycrystalline and

473 

amorphous materials, H.P.Klug and L.E. Alexander (eds.) John Wiley &Sons, New York.

474 

Koller, M., de Sousa Dias, M.M., Rodríguez-Contreras, A., Kunaver, M., Žagar, E., Kržan, A.,

475 

Braunegg, G. (2015). Liquefied Wood as Inexpensive Precursor-Feedstock for Bio-Mediated

476 

Incorporation of (R)-3-Hydroxyvalerate into Polyhydroxyalkanoates. Materials, 8, 6543-6557.

477 

Kos, T., Anžlovar, A., Kunaver, M., Huskić, M., Žagar, E. (2014). Fast preparation of

478 

Nanocrystalline cellulose by microwave-assisted hydrolysis. Cellulose 21, 2579-2585.

479 

Kunaver, M., Jasiukaitytė, E., Čuk, N., Guthrie, J.T. (2010). Liquefaction of wood, synthesis and

480 

characterization of liquefied wood polyester derivatives. Journal of Applied Polymer Science,

481 

115, 3, 1265-1271.

482 

Kunaver, M., Medved, S., Čuk, N., Jasiukaitytė, E., Poljanšek, I., Strnad, T. (2010a). Application

483 

of liquefied wood as a new particle poard adhesive system. Bioresource Technology, 101, 1361-

484 

1368.

485 

Kunaver, M., Jasiukaitytė, E., Čuk, N. (2012). Ultrasonically assisted liquefaction of

486 

lignocellulosic materials. Bioresource Technology, 103, 360-366.

487 

Lam, E., Male, K.B., Chong, J.H., Leung, A.C.W., Luong, J.H.T. (2012). Applications of

488 

functionalized and nanoparticle-modified Nanocrystalline cellulose. Trends in Biotechnology, 30,

489 

5, 283-290.

490 

Li, W., Wang, R., Liu, S. (2011). Nanocrystalline cellulose prepared from softwood kraft pulp via

491 

ultrasonic-assisted acid hydrolysis. Bioresources, 6(4), 4271-4281.

18   

492 

Lin L., Yoshioka M., Yao Y., Shiraishi N. (1994). Liquefaction of wood in the presence of phenol

493 

using phosphoric acid as a catalyst and the flow properties of the liquefied wood. Journal of

494 

Applied Polymer Science, 52, 1629-1636.

495 

Mandal, A., Chakrabarty, D. (2011). Isolation of nanocellulose from waste sugarcane bagasse

496 

(SCB) and its characterization. Carbohydrate Polymers, 86, 1291-1299.

497 

Morais, J.P.S., Rosa, M.F., Filho, M.M.S., Nascimento, L.D., Cassales, A.R. (2013). Extraction

498 

and characterization of nanocellulose structures from raw cotton linter. Carbohydrate Polymers,

499 

91, 229-235.

500 

Nascimento, D.M., Almeida, J.S., Dias, A.F., Figueirêdo, M.C:B., Morais, J.P.S., Feitosa, J.P.A.,

501 

Rosa, M.de F. (2014). A novel green approach for the preparation of cellulose nanowhiskers from

502 

white coir. Carbohydrate Polymers, 110, 456-463.

503 

Nelson, M.L., O’Connor, R.T. (1964). Relation of certain infrared bands to cellulose crystallinity

504 

and crystal lattice type. Part II. A new infrared ratio for estimation of crystallinity in celluloses I

505 

and II. Journal of Applied Polymer Science, 8, 1325-1341.

506 

Park, S., Baker, J.O., Himmel, M.E., Parilla, P.A., Johnson, D.K. (2010). Cellulose crystallinity

507 

index: measurement techniques and their impact on interpreting cellulose performance.

508 

Biotechnology for Biofuels, 3-10.

509 

Ridgway, C.J., Gane, P.A.C. (2012). Constructing NFC-pigment composite surface treatment for

510 

enhanced paper stiffness and surface properties. Cellulose, 19, 547-560.

511 

Sadeghifar, H., Filpponen, I., Clarke, S.P., Brougham, D.F., Argyropoulos, D.S. (2011).

512 

Production of cellulose nanocrystals using hydrobromic acid and click reactions on their surface.

513 

Journal of Materials Science, 46:7344-7355.

514 

Segal, L., Creely, J.J., Martin, A.E., Conrad, C.M. (1959). An empirical method for estimating the

515 

degree of crystallinity of native cellulose using the X-ray diffractometer. Textile research Journal,

516 

29, 786-794.

517 

Seljak, T., Oprešnik, S.R., Kunaver, M., Katrašnik, T. (2012). Wood, liquefied in polyhydroxy

518 

alcohols as a fuel for gas turbines. Applied Energy, 99, 40-49.

519 

Singh, R., Shukla, S., Tiwari, S., Srivastava, M. (2014). A review on delignification of

520 

lignocellulosic biomass for enhancement of ethanol production potential. Renewable and

521 

Sustainable Energy Reviews, 32, 713-728.

19   

522 

Smilgies, D.M. (2009). Scherrer grain-size analysis adapted to grazing-incidence scattering with

523 

area detectors Journal of Applied Crystallography, 42, 1030-1034.

524 

Tang, Y., Yang, S., Zhang, N., Zhang, J. (2014). Preparation and characterization of

525 

Nanocrystalline dellulose via low-intensity ultrasonic-assisted sulphuric acid hydrolysis.

526 

Cellulose, 21, 335-346.

527 

Teixeira, E.M., Correâ, A.C., Manzoli, A., Leite, F.L., Oliveira, C.R., Mattoso L.H.C. (2010).

528 

Cellulose nanofibers from white and naturally colored cotton fibers. Cellulose, 17, 595-606.

529 

Terinte, N., Ibbett, R., Schuster, K.C. (2011). Overview on native cellulose and microcrystalline

530 

cellulose I structure studied by X-Ray diffraction (WAXD): comparison between measurement

531 

techniques. Lenzinger Berichte, 89, 118-131.

532 

Thygesen, A., Oddershede, J., Lilholt, H., Thomsen, A.B., Stahl, K. (2011). On the determination

533 

of crystallinity and cellulose content in plant fibers. Cellulose, 12, 563-576.

534 

Turbak, A.F., Snyder, F.W., Sandberg, K.R. (1983). Microfibrillated cellulose, a new cellulose

535 

product: Properties, uses and commercial potential. Journal of Applied Polymer Science, Applied

536 

Polymer Symposium, 37, 815-827.

537 

Wettstein, S.G., Alonso, D.M., Gurbuz, E.I., Dumesic, J.A. (2012). A roadmap for conversion of

538 

lignocellulosic biomass to chemicals and fuels. Current Opinion in Chemical Engineering, 1, 218-

539 

224.

540 

Wiley Registry of Mass Spectral Data 7th Ed. , (1999). Agilent Technologies, Palo Alto, CA

541 

94306 U.S.A.

542 

Yamada, T. and Ono, H. (2001). Characterization of the products resulting from ethylene glycol

543 

liquefaction of cellulose. Journal of Wood Science, 47, 458-464.

544 

Yu, HY, Qin, ZY., Liang, BL., Liu, N., Zhou, Z., Chen, L. (2013). Facile extraction of thermally

545 

stable cellulose nanocrystals with a high yield of 93% through hydrochloric acid hydrolysis under

546 

hydrothermal conditions. Journal of Materials Chemistry, A 1:3938–3944.

547 

20   

547  548 

List of Tables:

549 

Table 1: The composition of the materials and their crystallinity index

Biomass 

550 

Hemicelluloses  Cellulose  (%)  (%) 

Lignin  (%) 

Extractives  (%) 

Ash  (%) 

Crystallinity  index (CrI) 

Cotton linters 

7.1 

81.3 

2.5 

6.3 

2.8 

64 

Spruce wood 

29.6 

42.3 

26.9 

0.9 

0.3 

47 

Chinese silver  grass 

33.9 

47.1 

10.5 

5.6 

2.9 

53 

Eucalyptus  wood 

26.9 

44.3 

26.1 

2.3 

0.4 

57 

Data reported are on a dry matter basis.

551 

21   

551  552 

Table 2: The % recovery of NCC, the crystallinity index, the average crystal length and crystal width.

Biomass 

Average  length 

 (%) 

Crystallinity  index (CrI)a 

of NCC(nm)b 

Average NCC  crystal width (nm)c 

Cotton linter 

74.5±6.0 

80% 

242±8 

12.7+/‐0.4 

Spruce wood 

61.5±3.2 

63% 

235±23 

8.9+/‐0.1 

Chinese  silver grass 

55.6±4.0 

62.8% 

250±17 

8.9+/‐0.2 

Eucalyptus  wood 

63.0±8.5 

66% 

306±13 

9.0+/‐0.1 

553 

a

554 

b

555 

c

556 

 

NCC recovery 

The crystallinity index was calculated using Segal 21-WAX method The length of the NCC crystals was evaluated from SEM micrographs.

The width of the NCC crystals was estimated by using the Scherrer equation.

557 

22   

557  558 

Table 3: The GC/MS determination of sugars present in the residual liquid and thermal

559 

parameters for the NCC samples and raw cotton linter

Total sugars 

To  

Tmax  

Residue  

(mg/g) 

(oC)a 

(oC)a 

(%) 

Cotton linter 

16.08±1.4 

249.7 

284.6 

24.1 

Spruce wood 

14.59±1.2 

299.3 

326.1 

22.3 

Chinese silver grass 

10.65±1.0 

268.6 

301.7 

21.5 

Eucalyptus wood 

10.13±0.9 

290.1 

322.5 

20.9 

Raw cotton linter 

‐ 

314.4 

362.5 

17.9 

Biomass 

560 

a

561 

 

To and Tmax were calculated from TGA curves.

562  563  564  565  566 

List of Tables in Supplementary materials:

567 

Table 1 S1: Crystallinity index of nanocrystalline cellulose that was isolated from selected

568 

cellulose-containig materials, determined by different methods:

569 

23   

569  570 

Figure captions:

571 

Figure 1. Average hydrodynamic diameter of the NCC particles size vs. the reaction time (min)

572 

used: eucalyptus (a), Chinese silver grass (b), cotton linters (c) and spruce wood (d).

573 

Figure 2: Hydrodynamic size distribution of NCC isolated from selected cellulose sources at

574 

different reaction times

575 

Figure 3: SEM micrographs of NCC: cotton linters (a), Chinese silver grass (b), spruce wood (c)

576 

and eucalyptus wood (d)

577 

Figure 4: XRD diffractograms of NCC: cotton linters(a), Chinese silver grass (b), spruce wood (c)

578 

and eucalyptus wood (d)

579 

Figure 5: The GC/MS chromatogram of the liquid residue, obtained after the isolation of NCC

580 

from selected materials. The methyl ester of levulinic acid was identified at 6.95 minutes.

581 

Figure captions in Supplementary materials:

582 

Figure 1 S1: STEM micrograph of nanocrystalline cellulose, isolated from cotton linters

583 

Figure 2 S1: Differential TGA analysis of selected cellulose-containing materials

584 

Figure 3 S1: FT-IR spectra of nanocrystalline cellulose that was isolated from selected cellulose-

585 

containig materials: (a): Chinese silver grass, (b): spruce wood, (c): eucalyptus, (d): cotton linter

586 

Figure 4 S1: The GC/MS chromatogram of liquid residues after the isolation of NCC from spruce

587 

wood. The trimethyl silyl ethers (TMS) of the sugars were identified from 9.4 minutes till 12.0

588 

minutes. (The TMS ethers of glucose, xylose and galactose were observed at 9.74, 10.91 and

589 

10.99 minutes, respectively).

590 

Figure 5 S1: Suspension of NCC in 1,4-Dioxane: (a) spruce wood, (b) eucalyptus (c) Chinese

591 

silver grass, (d) cotton linters

592  593  594 

24   

594 

Highlights 

595 



A new process for the production of nanocrystalline cellulose was developed 

596 



The liquefaction reaction using glycols and mild acid catalysis was used 

597 



Four model cellulose containing materials were used 

598 



The yields and crystallinity index were high 

599 



Levulinic acid and different sugars were identified in the liquid residue 

600 



Nanocellulose suspension in organic medium with grossly reduced agglomeration 

601 

 

602  603  604 

25   

SUPPORTING INFORMATION FOR THE FAST AND EFFECTIVE ISOLATION OF NANOCELLULOSE FROM SELECTED CELLULOSIC FEEDSTOCKS Matjaž Kunaver1,*, Alojz Anžlovar1, Ema Žagar1 1

National Institute of Chemistry, Laboratory for Polymer Chemistry and Technology, Hajdrihova 19,

1000 Ljubljana, Slovenia, Tel: +38614760363, Fax: +38614760300

Figure 1 S1. STEM micrograph of nanocrystalline cellulose isolated from cotton linters.

Table 1 S1. Crystallinity index of nanocrystalline cellulose isolated from selected cellulose containig materials determined by different methods.

Amorphous subtraction

Segal 21-WAX

Segal 18-WAX

Cotton linter

53.9%

80%

89%

58.0%

Spruce wood

42.8%

63%

68%

48.0%

Chinese silver grass

43.9%

62.8%

80%

48.9%

Eucalyptus wood

45.9%

66%

79%

50.9%

Biomass

FT-IR

Figure 2 S1. Figure 2 S1 Differential TGA analysis of selected cellulose containing materials. The DTGA of the raw cotton linter was added in order to show the significant difference between Tmax of nanoparticles and raw cotton fibers.

Figure 3 S1. FT-IR spectra of nanocrystalline cellulose isolated from selected cellulose containig materials: (a) Chinese silver grass, (b) spruce wood, (c) eucalyptus, (d) cotton linters.

Figure 4 S1. The GC/MS chromatogram of liquid residues after the isolation of NCC from spruce wood. The trimethyl silyl ethers (TMS) of the sugars were identified from 9.4 minutes till 12.0 minutes. (The TMS ethers of glucose, xylose and galactose were observed at 9.74, 10.91 and 10.99 minutes, respectively).

Figure 5 S1. Suspension of NCC in 1,4-Dioxane: (a) spruce wood, (b) eucalyptus (c) Chinese silver grass, (d) cotton linters.