Abstract
Although organosolv processes using high-boiling solvents have been investigated in recent decades for developing novel industrial processes, there are potential benefits of using high-boiling point solvents for traditional sulphate-based cooking processes, both from an industrial perspective and from a laboratory perspective. Using high-boiling solvents, experiments can be done under atmospheric conditions, thus making it easier to continually monitor laboratory experiments and extracting aliquots at desired intervals. Using such a system, alkaline consumption was monitored during impregnation of spruce chips in glycerol media using chemical charges of 1 M NaOH and 0.1 M NaHS, i. e., kraft pulping conditions, and compared to a similar investigation of alkaline consumption in water media using steel autoclaves. The resulting data was fitted to a first order kinetic model, with an apparent activation energy of 22 kJ mol−1 in glycerol media. Finally, a “normal quality pulp” of kappa number 28 and a viscosity of 1113 ml g−1 was successful produced using a cooking process with an impregnation step at 140 °C for 3 h and a cooking step at 160 °C for 4 h. A nuclear magnetic resonance study on the dissolved lignin produced for said experiment showed characteristics typical of other kraft lignins.
Introduction
Although the kraft process remains the most common process for producing chemical pulp to this day, alternatives have been investigated over recent decades, spurred by the desire to obtain purer fractions of biomass, by concerns over chemical effluents from the sulphite and kraft processes, from desires to reduce capital investment costs, or from some combination thereof (Jiménez et al. 2004, Demirbaş and Celik 2005, González et al. 2008, Sun et al. 2015).
Many of these alternative processes fall into the category of organosolv processes: pulping methods utilising organic solvents, sometimes with the addition of catalysts (such as acid, alkali or sulphur containing chemicals), to fractionate and dissolve biomass. The earliest of these methods utilised low boiling point solvents such as methanol and acetone, the original Kleinert process as well as the Alcell- and MD organocell processes developed from it being prominent examples (Kleinert 1976, Aziz and Sarkanen 1989). Since then, many different organic solvents have been investigated for use in organosolv processes. Examples of such investigations as applied to biomass includes the work of Gast and Puls (1984), who applied mixtures of water and ethylene glycol to produce pulps from birchwood, the work of Jiménez et al. (1997, 1998), who investigated the use of acid-water mixtures as well as phenol as a means of pulping wheat straw, as well as a latter work of Jiménez et al. (2004), investigating the use of alkali-glycol-water mixtures as a means of pulping olive tree trimmings. Further examples include the work of Uraki and Sano (1999), who employed various polyhydric alcohols with sulphuric acid as a catalyst for the pulping of fir, larch and cedar, the work of González et al. (2008), who investigated the effects of various glycols as well as ethanolamine catalysed by alkali for the pulping of rice straw and empty fruit bunches as well as the work of Kim et al. (2018), who employed glycol ether catalysed by hydrochloric acid for the pulping of eucalyptus.
In some cases, organosolv pulping makes use of high boiling point solvents such as polyethylene glycol or glycerol in order to perform the process in question under atmospheric conditions. Among these high boiling point solvents, glycerol, as a by-product of the manufacture of biodiesel in the form of methanol esters of fatty acids from triglycerides, has seen particular interest due to the recent spike in supply caused by the surge in the biodiesel market as oil prices have risen (Novo et al. 2011, Sun et al. 2015, Gabhane et al. 2020). This interest has later expanded, with many investigations into high boiling point solvents relating to pre-treatments of non-wood biomass in preparation for hydrolysis or enzymatic treatment being made, such as in the work of Sun et al. (2015), who investigated the ability of a glycerol organosolv pre-treatment to improve the hydrolysability of the components of wheat straw or in the work of Gabhane et al. (2020), who successfully applied a glycerol thermal pre-treatment to paddy straw, finding it effective in lignin and hemicellulose removal. More traditional work investigating the use of glycerol as an organosolv process for the production of pulp can be exemplified in the work of Novo et al. (2011), who applied mixtures of water and glycerol at temperatures up to 198.3 °C to produce pulp from bagasse. Other authors have complemented the use of glycerol or glycerol-water mixtures with the use of sodium hydroxide as catalyst. Examples include the work of Demirbaş (1998), who applied glycerol-water mixtures with additions of up to 10 w% of sodium hydroxide to samples of beech, spruce and ailanthus, obtaining pulps with yields of 53 % at kappa numbers of 16, or the work of Küçük (2005), who applied glycerol-water mixtures with sodium hydroxide added as catalyst to samples of spruce and ailanthus, comparing the resulting yields to those obtained through the use of the n-butanol organosolv process as well as in the work of Demirbaş and Celik (2005), who applied mixtures of pure glycerol using sodium hydroxide as catalyst to samples of poplar and spruce and achieved successful delignification at temperatures above 165 °C. To the authors knowledge, however, no work has yet attempted to replicate kraft cooking conditions with addition of sulphide as well as hydroxide in glycerol media.
In a system where glycerol is used as a high boiling point solvent rather than an active nucleophile as is the case in organosolv processing, the emphasis regarding various physical and chemical properties of glycerol changes. Used as a solvent, the ability of glycerol to properly solubilise and mobilise the active hydroxide and sodium sulphide ions is crucial, as is the ability to cause swelling of the wood structure similarly to water.
A rough predictions of glycerol’s solubilising properties can be made by comparing the Hansen solubility parameters of glycerol with those of water, with glycerol displaying a δD of 17.4 MPa1/2, a δP of 12.1 MPa1/2 and a δH of 29.3 MPa1/2 as compared to waters δD of 15.5 MPa1/2, δP of 16.0 MPa1/2 and δH 42.3 MPa1/2 (Hansen 2007) The values of glycerol are thus seen to be different to water in each of the categories, with an Ra distance of 14.1 MPa1/2, yet still of the same magnitude, and roughly equivalent to those of methanol, with a δD of 15.1 MPa1/2, a δP of 12.3 MPa1/2 and a δH of 22.3 MPa1/2. Glycerol has also experimentally proven to be an excellent solvent for sodium hydroxide (Demirbaş 1998).
Since the ability to swell wood is a common trait of all polar solvents (Demirbaş 1998, Küçük 2005, Novo et al. 2011) it is reasonable to assume that glycerol would follow a similar behaviour to water during impregnation, which was also seen experimentally in the work of Demirbaş and Celik (2005). Additionally, given the abnormally high diffusion and mobility of residual water in glycerol solutions (Glycerine Producers’ Association 1963) the action of cooking chemicals could be hypothesised to have similar behaviours in glycerol as they do in water.
A special mention concerns the ability of glycerol liquor to penetrate wood chips. Glycerol has a significantly higher viscosity than water, although the difference is reduced at higher temperatures (Glycerine Producers’ Association 1963). As a result, given that liquid movement is inversely proportional to viscosity, it is reasonable to predict a reduction in liquor penetration when using glycerol as solvent. Further complicating matters, dissolution of oxygen is lower in glycerol than in water, which could prevent air bubbles from escaping the chips (Malkov 2002). This effect, however, could be somewhat mitigated by the fact that glycerol also exhibits a lower surface tension than water (Glycerine Producers’ Association 1963), which can otherwise retard the ability of air to escape wood chips (Malkov and Tikka 2002).
The main benefit of using high boiling point solvents for cooking is the possibility of performing the process under atmospheric conditions. This could be of interest in industrial settings since it could allow for a reduction in capital investment costs (Jiménez et al. 2004). One, perhaps overlooked benefit, however, relates to the benefits of using such a system for laboratory investigations. Despite the venerable age of the kraft process, there are still unsolved research questions related to its understanding and optimisation. One such question is the consumption of alkali during impregnation.
During impregnation of wood chips, alkali is consumed through deacetylation of the wood as well as through activation of carboxylic acids, thus reducing the amount of intermolecular hydrogen bonds and allowing the wood structure to swell (Zanuttini and Marzocchi 1997, Zanuttini et al. 1999, Costanza et al. 2001, Zanuttini et al. 2005, Solár et al. 2008, 2011). As a result, diffusion of liquor and chemicals into the chip is made easier (Jiménez et al. 1990). Achieving this impregnated, swollen state is crucial for an even delignification during the later cooking stage. Insufficient impregnation results in higher kappa numbers, lower yields, and higher amounts of reject (Gustafson et al. 1989, Costanza et al. 2001, Malkov 2002, Määttänen and Tikka 2012).
The impregnation of wood chips in pulping is currently believed to occur according to a shrinking-core model. According to this model, initial reactions on the surface of the chip is rapid, allowing polar solvents to penetrate and swell the wood tissue. Thereafter, a “moving front” of chemical activity moves progressively closer to the core of the wood chip, ahead of which is unreacted, unswollen wood, and behind which is a neutralised area of swollen wood where chemical transfer is easier (Zanuttini et al. 2000, Zanuttini et al. 2005, Brännvall and Reimann 2018). At temperatures above 100 °C, this reaction front is primarily driven by reaction kinetics, rather than diffusion (Zanuttini et al. 2000, Costanza et al. 2001, Määttänen and Tikka 2012). The deacetylation and swelling of the wood changes its material properties, increasing its diffusion constant (Solár et al. 2008) and over time, the alkali concentration in the swollen wood is able to reach an equilibrium with the surrounding liquor (Hultholm et al. 1997). Once cooking starts, any additional transfer of hydroxide ions needed for delignification can be achieved by means of diffusion through the swollen wood (Määttänen and Tikka 2012).
A simplified schematic of the shrinking core model is presented in Figure 1: In the swollen shell, the alkali concentration (depicted as a blue gradient) is close to the alkali concentration of the liquor, while in the reactive moving front, alkali concentration gradually decreases as deacetylation becomes incomplete. In the unreacted core, deacetylation and swelling has yet to take place, and concentration of alkali is low.

A schematic of the shrinking-core model.
One challenge when performing research on impregnation, or indeed many topics within the field of pulping, is the need to replicate industrial conditions of high temperature and pressure within a laboratory environment. This generally requires the use of autoclaves or other reactors, which creates a barrier of entry while also preventing aliquots from a single reaction to be collected; instead, multiple autoclaves are generally prepared under similar conditions and removed at different times, significantly increasing the required amount of work. Use of high-boiling solvents could mitigate these issues, not just for organosolv processes, but also for adaptations of kraft pulping and while previous research has focused on using high boiling point solvents for novel organosolv or extraction processes, there is nothing preventing its use for regular kraft pulping.
In the present work, an adaptation of the kraft cooking process in glycerol media has been investigated as a means of monitoring alkaline consumption during impregnation, as a proof of concept for whether kraft pulping in glycerol at atmospheric pressure might be a useful technique for studying chemical pulping. This impregnation data has been compared with similar experiments in water using steel autoclaves. Once proper impregnation conditions were thus elucidated, it was also possible to implement and investigate a full cooking process based on atmospheric pulping and test whether such a process could have any commercial viability.
Materials and methods
Materials
Spruce wood chips for the glycerol experiments were kind gifts from SCA Munksund. Sodium hydroxide of Emsure grade was procured from (Sigma-Aldrich, Darmstadt, Germany). ≥ 60 % Sodium hydrysulphide hydrate was procured from (Sigma-Aldrich, St. Louis, MO, USA). Glycerol of GPR Rectapur grade was procured from (VWR International, Leuven, Belgium). All other chemicals were of analytical grade. Temperature was monitored using an Amarell Precision Thermometer (Amarell, Kreuzwertheim, Germany).
Glycerol cooking system
Kraft cooking was replicated in glycerol as follows: sodium hydroxide and sodium hydrogen sulphide was added neat into a round bottom flask according to desired effective alkali and sulphidity, after which an amount of GPR Rectapur grade glycerol, appropriate to the desired liquid to wood ratio, was added. Temperature was increased (incidentally removing any lingering impurities of water), stirring initiated, and a flow of nitrogen added to the reaction vessel. Once all chemicals were dissolved, starting aliquots of the cooking liquor were collected to measure initial NaOH and NaHS concentrations. Finally, wood chips were added to the reaction vessel and the resulting reaction monitored.
For reference, a control experiment was also conducted, following the same steps as per the above description but obviating the addition of chemicals and nitrogen gas.
Alkaline glycerol consumption experiment
Experiments were conducted as described above on 18 g of spruce wood chips in 130 ml of glycerol liquor using starting chemical concentrations of 1 M NaOH and 0.1 M NaHS (corresponding to an effective alkali of 28 % and a sulphidity of 18 % at a liquid to wood ratio of 7.2 to 1). Aliquots of 5 ml were collected at 0 min, 15 min, 30 min, 60 min, 90 min and 120 min and were used to determine hydroxide concentration over time. The experiment was replicated using increasing temperatures of 120 °C, 130 °C, 140 °C, and 150 °C.
Atmospheric cooking experiment
Full experiments of cooking in glycerol media were conducted as described above on 18 g of spruce wood chips in 130 ml of glycerol using starting chemical concentrations of 1 M NaOH and 0.3 M NaHS (corresponding to an effective alkali of 28 % and a sulphidity of 46 % at a liquid to wood ratio of 7.2 to 1). Impregnation was performed at 140 °C for 3 h after which the temperature was ramped to 160 °C and cooking was performed over 4 h. After the reaction, the reaction vessel was cooled, the black liquor extracted and the (delignified) wood chips washed overnight. After washing, the wood chips were defibrated using a NAF defibrator operating at 2 bar of water pressure. The resulting pulp was centrifuged, and its yield determined gravimetrically. Similarly, the reject (material retained in a metal mesh basket attachment of the NAF defibrator with 1.5 mm perforations) was collected and gravimetrically compared to the starting material.
Alkaline water consumption experiment
For reference, an experiment of alkaline consumption was also done in water media. In this experiment, batches of 200 g of spruce wood chips were added to a set of rotative steel autoclaves, which were allowed to react in a polyethylene glycol bath at temperatures of 90 °C, 120 °C, 130 °C, 140 °C and 150 °C using starting chemical concentrations of 0.6 M NaOH and 0.2 M NaHS and using a liquid to wood ratio of 5.5 to 1 (thereby corresponding to an effective alkali of 12 % and a sulphidity of 53 %). For each temperature, five autoclaves were added and taken out after 5 min, 10 min, 20 min, 30 min and 60 min, respectively. The autoclaves were rapidly cooled, and the liquor extracted for residual alkali and sulphur analysis.
Lignin precipitation, isolation and sample preparation
Lignin was precipitated from the glycerol black liquor as follows: 10 ml of glycerol black liquor was diluted with distilled water (in order to lower the viscosity of the solution) after which alkali was added in order to redissolve the lignin. The solution was then passed through a filter in order to remove any remaining pulp in the liquor.
Once the solution was thus filtered, it was acidified to a pH of 3, precipitating the lignin. The acidified solution was sequentially centrifugated in a Hettich Centrifuge Rotina 420 (Andreas Hettich GmbH & Co. KG, Tuttlingen, Germany) at 4800 rpm for 20 minutes at a pH 2.5 a total of seven times, after which a final centrifugation at pH 3.5 was applied and the precipitated lignin thus obtained was transferred to a Vacucell vacuum drying oven (BMT Medical Technology s. r. o., Zábrdovice, Czech Republic), where it was left to dry overnight at a temperature of 40 °C.
After being dried thus, 92.3 mg of sample was dissolved in 0.6 ml of DMSO-d6, after which it was subjected to inverse NMR experiments as described below. A separate sample of 27.8 mg was prepared according to the method of Argyropoulos (1995) after which it was subjected to 31P NMR analysis as detailed below.
Analysis methods
Residual alkali measurements were done on the black liquor aliquots according to SCAN-N 33:94 and residual hydrogen sulphide ion measurements were done according to SCAN-N 31:94, while Kappa number measurements were done on the produced pulp in accordance with ISO 302:2015 and viscosity measurements were done on the produced pulp in accordance with ISO 5351.
The precipitated lignin was subjected to a nuclear magnetic resonance (NMR) spectroscopy analysis including a heteronuclear single quantum coherence (HSQC) analysis, a complementary edited heteronuclear single quantum coherence (E-HSQC) analysis, a heteronuclear multiple bond correlation (HMQC) analysis and a quantitative phosphorous 31P NMR analysis.
The HSQC experiment was done using the hsqcetgpsi pulse sequence with increments of 1024 × 256, 72 scans per increment, an acquisition time of 86 ms, a relaxation delay of 2 s and a receiver gain of 203 with a spectral width of 15 ppm in the proton dimension and 165 ppm in the carbon dimension. The E-HSQC experiment was done using the hsqcedetgp pulse sequence with increments of 1024 × 256, 40 scans per increment, an acquisition time of 83 ms, a relaxation delay of 2 s and a receiver gain of 203 with a spectral width of 15 ppm in the proton dimension and 165 ppm in the carbon dimension. The HMBC analysis was done using the hmbcqpndqf pulse sequence with increments of 4096 × 128, 224 scans per increment, an acquisition time of 0.33 s, a relaxation delay of 2 s and a receiver gain of 203 with a spectral width of 15 ppm in the proton dimension and 222 ppm in the carbon dimension. The 31P NMR analysis was done using the zgig30 pulse sequence using 64k data points, 5120 scans, an acquisition time of 1.68 s, a relaxation delay time of 6 s and a receiver gain of 203 with a spectral width of 120 ppm.
All experiments were done on a Bruker Avance III HD 400 MHz instrument (Bruker Corporation, Billerica, MA, USA) equipped with a BBFO probe (Bruker Corporation, Billerica, MA, USA), including a Z-gradient coil. Processing was done using the software MestReNova v14.2.1-27684 (Mestrelab Research, Santiago de Compostela, Galicia, Spain), including apodisation (90°-shifted square sine bell for the HSQC spectra, 0°-shifted sine bell for the HMBC spectra, and 1 Hz exponential multiplication for the 31P NMR experiment), manual phase adjustment, and automatic baseline correction using a third order Bernstein Polynomial Fit for the 31P NMR experiment.
Results and discussion
Alkaline consumption in water
An initial study of alkaline consumption in water media was done by subjecting five autoclaves filled with 200 g of spruce wood chips as well as white liquor at chemical concentrations of 0.6 M NaOH and 0.2 M NaHS to temperatures of 90 °C, 120 °C, 130 °C, 140 °C and 150 °C for varying amounts of time, after which residual alkali was measured, and the alkali consumption calculated. The result of these experiments can be seen in Figure 2.

Alkaline consumption of spruce at different temperatures during kraft pulping impregnation conditions in water based white liquor.
In this experiment, it can be seen that most of the alkaline consumption is achieved in the first 15 minutes, similarly to what has been observed in previous works (Määttänen and Tikka 2012) after which alkaline consumption is seen to follow a similar trend to that observed by Karlström (2009), who reported consumptions of 100 kg ton−1 wood after 90 min of reaction at 120 °C, 90 kg ton−1 wood after 90 min of reaction at 110 °C and 70 kg ton−1 wood after 90 min of reaction at 100 °C, all cases using initial concentrations of 0.6 M NaOH and 0.2 M NaHS.
An Arrhenius-analysis of the data was done by fitting the data to a first order kinetic expression. In principle, assuming an elementary reaction, the neutralisation of acetyl groups by alkali would be described by a second order kinetic expression proportional to the concentration of acetyl groups as well as the concentration of alkali. However, for a system of wood undergoing such neutralisation, the concentration of alkali can be assumed to be in excess of the accessible acetyl groups, resulting in a pseudo-first order expression dependant on the concentration of acetyl groups. Similarly, the molar consumption of acetyl groups, which is equal to the molar consumption of hydroxyl groups and proportional to the alkaline consumption expressed as g kg−1 wood, will also follow pseudo-first order kinetics as a result. By treating the alkaline consumption as a pseudo-first order phenomenon following a
k-values and activation energies derived from a regression according to pseudo-first order kinetics for the respective experiments in water and glycerol.
Temperature | Spruce k values (min −1 ) | Glycerol Spruce k values (min −1 ) |
90 °C | 0.124 | – |
120 °C | 0.090 | 0.012 |
130 °C | 0.152 | 0.018 |
140 °C | 0.205 | 0.017 |
150 °C | 0.200 | 0.022 |
Arrhenius analysis | Spruce values (kJ mol −1 ) | Glycerol Spruce values (kJ mol −1 ) |
Activation energy | 12.2 | 22.4 |
Alkaline consumption in glycerol
One of the hypotheses of the present work was that glycerol, being a polar solvent able to swell wood in a similar fashion to water (Demirbaş 1998, Küçük 2005, Novo et al. 2011) while seemingly being able to also transport solutes in a similar fashion due the high mobility of residual water in the matrix, (Glycerine Producers’ Association 1963) could be used for investigations of alkaline consumption similar to the more classic experiment above. Doing so would have the benefit of allowing the experiment to proceed under atmospheric conditions as well as lowering the barrier of entry to similar research in the future. As such, a similar set of experiments were conducted on spruce wood chips in glycerol. The glycerol experiments were conducted in a smaller scale, using 18 g of wood chips and volumes of 130 ml of GPR Rectapur grade glycerol using initial chemical concentrations of 1 M NaOH and 0.1 M NaHS. In this case, aliquots of 5 ml were taken out of the same batch at intervals of 15 min, 30 min, 60 min, 90 min and 120 min respectively. Residual alkali and alkaline consumption were measured and calculated analogously to the water-based experiments above, and the results are shown in Figure 3.

Alkaline consumption of spruce at different temperatures during kraft pulping impregnation conditions in glycerol based white liquor.
For temperatures below 150 °C, consumptions of alkali are seen to be significantly lower than their counterparts in the water-based experiment although interestingly, the difference between the two systems is significantly mitigated at higher temperatures, particularly at 150 °C. One possible reason for this effect is the exponential lowering of glycerol viscosity at high temperatures, which is halved from 7.797 centipoise at 120 °C to 3.823 centipoise at 150 °C for solutions of glycerol (Glycerine Producers’ Association 1963).
The above profiles together with their respective temperatures were used to model the experiments in accordance with the same assumptions as for the water experiments conducted above with the resulting analysis giving rate values as seen in Table 1, an Arrhenius plot depicted in Supplementary Figure 2 in the supplementary information and an apparent activation energy of 22 kJ mol−1. While higher than the apparent activation energy of 12 kJ mol−1 observed in the water-based experiment, this activation energy is still below 30 kJ mol−1 and therefore suggestive of a primarily diffusion-driven phenomenon (Germgård 2017).
Atmospheric cooking in glycerol
With the impregnation behaviour in glycerol elucidated, and with the initial goal of demonstrating glycerol to be a viable setup for continued experiments under laboratory conditions concluded, the cooking system was modified to a full pulping process. Although impregnation proved most efficient at 150 °C, a lower temperature of 140 °C was selected due to the high risk of initiating cooking reactions at the higher temperature. To compensate, impregnation was extended to three hours. Cooking was conducted at 160 °C for four hours and starting chemical concentrations were selected to 1 M NaOH and 0.3 M NaHS, corresponding to an effective alkali of 28 % and a sulphidity of 46 % at a liquid to wood ratio of 7.2 to 1.
Using these conditions in the same set-up as for the consumption experiments above, spruce wood chips were delignified. They were then washed overnight and defibrated using a NAF defibrator operating at 2 bar of water pressure. By these means, a pulp of kappa number 28 and a pulp viscosity of 1113 ml g−1 was produced with a screened yield of 37 % and a reject content of 15 %. While the kappa number and total yield of the experiment shows promise for utilising glycerol for atmospheric kraft cooking, the reject content is unacceptably high.
To control for the nucleophilic properties of the pure glycerol, a control experiment was performed on spruce wood chips in glycerol without the addition of chemicals. Although some extraction was seen to take place, the thus treated wood chips retained 94 % of their dry weight and could not be defibrated into pulp when subjected to the NAF defibrator.
The high amount of reject produced in the atmospheric cooking despite the investigation into impregnation could be a result of insufficient penetration (given that glycerol has previously been found to be an excellent solvent for hydroxide in the work of Demirbaş (1998) and has been found able to swell wood as in the work of Demirbaş and Celik (2005), it seems unlikely to the authors that either diffusion or swelling would be at fault) of the glycerol into the wood matrix. Penetration of cooking liquor into wood chips through cavities concerns the flow of liquid into wood chips by means of a pressure gradient (Määttänen and Tikka 2012). Given that liquid flow is inversely proportional to the viscosity of the liquid in question, this process would naturally be lower for the glycerol system than in a system were water is used as solvent. The impregnation of wood in glycerol could also have been partially hindered by the lower dissolution of oxygen in glycerol compared to water, which makes glycerol less able to remove air bubbles, thereby reducing penetration (Malkov 2002).
If penetration is indeed to blame for the high amounts of reject (particularly if the cause is due to issues with the dissolution of oxygen), it is possible that the situation could be remedied by pre-steaming the wood chips (Gustafson et al. 1989), although this would require experimental verification. Alternatively, insufficient penetration could be avoided by using thinner wood chips, as seen in the work of Jiménez et al. (1990), who found wood thickness to be a significant variable for the penetration of cooking liquor into Douglas fir chips or in the work of Demirbaş and Celik (2005), who achieved significantly better delignification using wood chips at a thickness of 0.3 mm compared to 2 mm when cooking poplar and spruce wood chips in alkaline glycerol.
As a final set of experiments for elucidating the behaviour of glycerol cooking, lignin was precipitated from black glycerol liquor, lyophilised, and analysed using nuclear magnetic resonance (NMR) spectroscopy. Specifically, 92.3 mg of lyophilised lignin was redissolved in 0.6 ml of DMSO-d6 and analysed using a heteronuclear single quantum coherence (HSQC) experiment, a multiplicity edited heteronuclear single quantum coherence (E-HSQC) experiment and a heteronuclear multiple bond correlation (HMBC) experiment, while 27.8 mg of lyophilised lignin was phosphorylated and analysed using quantitative 31P NMR. The HSQC and 31P NMR protocols represent established methods of semi-quantifying characteristic bonds in lignin, and quantifying hydroxyl functionalities, respectively.
The HSQC spectrum, presented in Figure 4, was semi-quantified according to the method of Sette et al. (2011). The HSQC spectrum is seen to contain functionalities typical of kraft lignin, with a β-O-4 content of 2.03 mol%, a β-β content of 1.97 mol% and a β-5 content of 1.09 mol%, normalised on the C2 carbon in lignin. Although these values are in the range typically seen in other kraft-lignins (for instance, see Giummarella et al. (2020), reporting values of 6.7 mol% β-O-4 and 1.9 mol% β-5 for an industrial softwood kraft lignin), the β-O-4 content in particular is lower than would be expected of regular kraft lignin, indicating a higher amount of degradation than is normal at this kappa number. This is likely a consequence of the liquor penetration issues discussed above, resulting in excessive degradation of the dissolved lignin. If this penetration issue could be solved or mitigated, it is therefore possible that this degradation could also be mitigated in turn.

HSQC spectra of lignin extracted from the glycerol black liquor, with HMBC data of the same lignin superimposed in green. Also superimposed in green is a window around the glycerol signal at δH 3.5, δC 62-72, showing that there are no long-range correlations between glycerol and lignin.
In addition to the regular functionalities normally seen in kraft lignins, signals related to the glycerol solvent can be seen at shifts (δH 3.5, δC 62-72). This is particularly noticeable in a complementary E-HSQC spectrum that was acquired on the same material, which can be found in Supplementary Figure 3 in the supplementary material. To investigate whether any long-range correlations could be seen for the glycerol, a complementary HMBC analysis was made, which is shown alongside the HSQC spectra in Figure 4. While glycerol peaks can again be identified at shifts (δH 3.5, δC 62-72), no long-range correlations to lignin can be seen in the HMBC spectrum. While one should be careful when making conclusions based on the absence – rather than the presence – of NMR peaks, the large prevalence of glycerol by virtue of being used as solvent together with the slow t2 relaxation of glycerol makes this absence suspicious and corroborates the hypothesis that the system has simply reacted according to regular kraft mechanics.
In order to quantify the hydroxyl functionality of the procured lignin, a 31P NMR spectra was taken and quantified according to the method of Granata and Argyropoulos (1995). In this spectrum, which is presented in Supplementary Figure 4 in the supplementary material, the lignin is seen to contain 1.83 mmol g−1 of aliphatic hydroxyls, 4.16 mmol g−1 of aromatic hydroxyls and 0.51 mmol g−1 of carboxylic hydroxyls with a total functionality of 6.50 mmol g−1. These values are, again, in the range of values typically seen for kraft lignin, with Giummarella et al. (2020) reporting values of 2.30 mmol g−1 of aliphatic hydroxyls, 3.84 mmol g−1 of aromatic hydroxyls and 0.37 mmol g−1 of carboxylic hydroxyls for a sample of industrial softwood kraft lignin.
Conclusions and technical significance
Atmospheric cooking was achieved by using glycerol as a media for the kraft cooking process, thus allowing continued monitoring of residual hydroxide. Consumption was found to be slower in glycerol than in water media at temperatures below 150 °C, as well as proceeding according to a
Full atmospheric cooking was attempted using three hours of impregnation at 140 °C and four hours of cooking at 160 °C, successfully producing a normal quality pulp at kappa number 28 albeit at a low yield of 37 % and a high reject of 15 %. The dissolved lignin showed functionalities typical for kraft lignin, although displaying excessive fragmentation, with a low β-O-4 content of 2.03 mol% and an aliphatic hydroxyl content of 1.83 mmol g−1. No lignin-glycerol correlations could be seen, corroborating the interpretation that the reaction has behaved analogously to a regular kraft system.
The study thus demonstrates that it is indeed possible to replace water in kraft pulping with glycerol and produce pulp with normal kappa numbers and viscosities, as well as to generate lignin with characteristics typical for kraft lignins. While the present study was not able to achieve acceptable levels of reject content, this could be investigated further, and if solved would allow for full replication of the kraft process in glycerol media. The major technical advantage of using glycerol in kraft pulping would be the possibility of performing the process at atmospheric pressure, thus lowering investment costs, and reducing barriers of entry. In particular, the costs of constructing digesters for such a system would be much lower than the costs of constructing digesters for a traditional water based kraft pulping system. Glycerol is relatively cheap, and no large risks are associated with its handling, being non-toxic and non-flammable. Nevertheless, the development of a chemical recovery system for glycerol pulping is challenging and as of yet unsolved, and the outcome of such developments will be central for any eventual commercialisation of the method. In the short term the method might be of greater value in research and pedagogic use: since pulping can be performed atmospherically, it can be performed “openly” in a laboratory without the need for closed autoclaves. This also greatly facilitates aliquot sampling and introduces the possibility of continuous online measurements.
Funding source: Knut och Alice Wallenbergs Stiftelse
Award Identifier / Grant number: KAW 2015.0390
Funding statement: The authors acknowledge funding from the Knut and Alice Wallenberg Foundation (KAW) (Grant Number: KAW 2015.0390) through the Wallenberg Wood Science Centre.
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Conflict of interest: The authors declare that they have no conflicts of interest.
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Artikel in diesem Heft
- Frontmatter
- Biorefining
- Microwave heating rate and dielectric properties of some agricultural wastes
- Chemical pulping
- Adapting the kraft cooking process in glycerol media. Studies of impregnation kinetics
- Paper technology
- Numerical simulation of heat pump drying system for paper exhaust hood
- Using machine learning to predict paperboard properties – a case study
- Paper physics
- Wet creping of paperboard
- Experimental investigation into paper dust formation during knife edge cutting on a laboratory scale
- Bending stiffness and moment capacity of cardboard obtained from three-point and elastica bending tests
- Paper chemistry
- Application of TMP-DCMC-BBR/KH-791-SiO2/HPDSP multifunctional protective fluid in paper protection
- Study on aging resistance of AAAS grafted in situ on paper documents
- Coating
- Flexible graphene oxide/polyacrylonitrile composite films with efficient ultraviolet shielding and high transparency for the protection of paper-based artifacts
- Activated carbon paper as ethylene adsorber
- Printing
- Effect of progressive deinking and reprinting on inkjet-printed paper
- Digital printing systems and office papers interactions and the effects on print quality
- Packaging
- Comparison of methods to characterize the penetration of hot melt adhesive into paper
- A study on forming limit diagram and laminated stamping of paperboard
- Environmental Impact
- Ultrafiltration and reuse opportunities of sectorial effluents from a kraft pulp mill in Brazil
- CaCO3 solubility in the process water of recycled containerboard mills
- Miscellaneous
- Feasibility for the preparation of aerogels with celluloses extracted mildly from waste palm leaves
Artikel in diesem Heft
- Frontmatter
- Biorefining
- Microwave heating rate and dielectric properties of some agricultural wastes
- Chemical pulping
- Adapting the kraft cooking process in glycerol media. Studies of impregnation kinetics
- Paper technology
- Numerical simulation of heat pump drying system for paper exhaust hood
- Using machine learning to predict paperboard properties – a case study
- Paper physics
- Wet creping of paperboard
- Experimental investigation into paper dust formation during knife edge cutting on a laboratory scale
- Bending stiffness and moment capacity of cardboard obtained from three-point and elastica bending tests
- Paper chemistry
- Application of TMP-DCMC-BBR/KH-791-SiO2/HPDSP multifunctional protective fluid in paper protection
- Study on aging resistance of AAAS grafted in situ on paper documents
- Coating
- Flexible graphene oxide/polyacrylonitrile composite films with efficient ultraviolet shielding and high transparency for the protection of paper-based artifacts
- Activated carbon paper as ethylene adsorber
- Printing
- Effect of progressive deinking and reprinting on inkjet-printed paper
- Digital printing systems and office papers interactions and the effects on print quality
- Packaging
- Comparison of methods to characterize the penetration of hot melt adhesive into paper
- A study on forming limit diagram and laminated stamping of paperboard
- Environmental Impact
- Ultrafiltration and reuse opportunities of sectorial effluents from a kraft pulp mill in Brazil
- CaCO3 solubility in the process water of recycled containerboard mills
- Miscellaneous
- Feasibility for the preparation of aerogels with celluloses extracted mildly from waste palm leaves