Characterization of Eucalyptus heartwood and sapwood pulp after kraft cooking
- 87 Downloads
- 1 Citations
Abstract
The hardwood species Eucalyptus citriodora (Myrtaceae) is used as a raw material in paper industry that has a substantial proportion of heartwood. In addition to libriform fibres and fibre tracheids, heartwood has vessels blocked with tyloses and sapwood has live ray and axial parenchyma cells filled with starch. To understand the negative correlation that exists between extractives content in heartwood and pulp yield, both heartwood and sapwood of different sizes were subjected to kraft cooking separately at 170 °C. The pulps after kraft cooking were chemically characterized and analyzed for various properties using FTIR data, Water retention value and Ash content value. For 150 µm size wood sample, it is found that heartwood pulp has almost fivefold more residual lignin and 2.5 folds less ash content compared to sapwood pulp. For 2000 µm size sample, the water retention value increases by threefold for pulp compared to wood, but within the pulp, sapwood pulp has slightly higher water retention value compared to heartwood pulp. The FTIR also confirms that heartwood pulp contains slightly more lignin than sapwood pulp. As the sample size decreases from 2000 to 150 µm, it results in decrease of residual lignin content. Hence this study will be helpful for optimization of the process parameters during kraft cooking and also to optimize the rotation cycle of trees i.e. least amount of heartwood in wood log as required by the paper industry.
Keywords
Heartwood and sapwood Kraft cooking FTIR analysis Water retention value Klason lignin Ash contentIntroduction
a Cross-section of Eucalyptus wood used for the study. Note the heartwood and sapwood distinction. b Cross-section of single wood pulp fibre. Note the kinks, gaps and irregular diameter which are characteristic of pulp fibres
Hardwoods have libriform fibres, fibre tracheids and conducting vessels. It also has parenchyma cells which are short compact cells with stubby ends. Hardwoods generally consist of 45 % cellulose, 30 % hemicellulose, 20 % lignin and 5 % extractives on a dry weight basis (Smook 1992). During pulping process, lignin is removed from compound middle lamella (CML) and partially from cell walls either by mechanical or chemical methods. Chemical pulping involves treatment of wood chips at an elevated temperature(~170 °C) in a solution of NaOH + Na2S (also called white liquor) until a certain degree of delignification. During this process, a small quantity of cellulose and hemicelluloses also gets degraded. Bleaching is performed on pulp fibres to remove the residual lignin present in the cell wall. Consequent to cooking, bleaching and drying, cell wall deformations such as wrinkles, micro compressions and twists are commonly observed in pulp fibres (Fig. 1b). Due to this the paper offers more flexibility than wood log. The degree of polymerization values (weight average) of cellulose also decreases from 3500 to 600–1500 when wood is transformed into Pulp (Smook 1992). Among several theories proposed to explain the chemistry of pulping reactions, cellulose crystal theory (Young 1994) suggested that the paracrystalline regions in native cellulose fibrils are transformed into amorphous regions during pulping, where the extent of transformation depends on cooking conditions. Fahlén and Salmén (2005) reported the formation of pores in the matrix material and enlargement of the cellulose fibril aggregates as a result of chemical pulping. Besides many changes in wood structure during chemical pulping, the three linkages between the propane side chains and the benzene rings are broken to free the cellulosic fibres (Smook 1992).
SEM images (tangential plane) of sapwood (left) and heartwood (right) of Eucalyptus after partial delignification. Note the clear visibility of conducting vessels and parenchyma cells in sapwood
Materials and methods
Different sizes of Eucalyptus wood chips (before cooking) separated by sieve analysis
Kraft cooking (delignification)
Delignification is carried out in a high pressure reactor (Anton Parr Model 4848). The reaction mixture of white liquor and wood samples were loaded in 1000 ml SS reactor with temperature control and stirrer rotation at 160 rpm. The conditions for pulping of 5 g of oven dry weight wood: liquor-to-wood ratio (mL/g) 4:1; sulfidity 30 % (both Na2S and NaOH expressed as Na2O); active alkali 20 % (as Na2O). Based on the optimal ratio, 18.5 ml of the white liquor i.e. solution of water + NaOH + Na2S was used for delignification. The pulping was carried out under isothermal conditions in two stages at 130 °C for 30 min and at 170 °C for 90 min, with heating time of 10 min for both the temperatures. The delignified samples were separated from the residual liquor using a funnel and a Whatman filter paper. The pulp was dried in a hot air oven at a temperature of 104.5 °C until a constant weight was observed and stored for further analysis. It should be noted that both heart and sapwoods were delignified under same cooking conditions.
Analysis of pulp
Raw heartwood and sapwood were analyzed before delignification and later milled and sieved fractions were analyzed after the kraft pulping process. Ash content for both the raw wood and kraft pulp fractions was determined by incinerating the samples at 525 °C until constant weight was attained in a muffle furnace (TAPPI T211). For incineration experiment, known oven dried weights of the samples were kept in a pre-weighed silica crucible for a period of 2–3 h
Total lignin content of wood samples
| Sample | Acid soluble (%) | Insoluble (Klason) (%) | Total (%) |
|---|---|---|---|
| Sapwood | 21.5 | 5.3 | 26.8 |
| Heartwood | 20.5 | 4.9 | 25.4 |
All the raw and delignified samples were analyzed using Fourier Transform Infrared (FTIR) spectroscopy in order to detect the various functional groups especially aromatic skeleton vibrations present in them. In order to get the spectral data, samples were dried, ground to fine size and mixed with potassium bromide (KBr) in approx. ratio of 1:100 and compressed to form the pellets. To understand the structural and morphological differences, both sapwood and heart wood were subjected to partial cooking to observe the longitudinal sections using scanning electron microscopy (after gold sputtering).
Results and discussion
Adding NaOH into the wood cells enables the cleavage of the β-O-4 structural linkages of lignin and the cleavage of ether and ester bonds between lignin and hemicellulose. As 10 % of alkali is consumed in initial period of cooking for the neutralization of acids deriving from the polysaccharides (acidic and uronic acids) and 25–30 % of the alkali is consumed for neutralising lignin degradation products. By maintaining the reasonable sulfidity levels (30 %) and varying the size of wood for both heartwood and sapwood, the aim of this study is to understand the process of delignification as it occurs in heartwood and sapwood separately. More specifically, the aim is to observe a possible amplification or a clearer pronouncement of the differences in delignification of heartwood and sapwood of a particular species given that the delignification was carried out at exactly the same reaction conditions for both. In line with the hypothesis, such differences were more clearly observed for a smaller size of raw wood, owing to improved chemical impregnation and availability of a larger surface area for the delignification reaction to occur. This difference was observed in all the results of experimental procedures employed in the study i.e. residual lignin content, water retention value, ash content and FTIR spectrophotometry.
Total residual lignin content of pulp measured through klason lignin technique
| Sample size (μm) | Sapwood pulp (%) | Heartwood pulp (%) |
|---|---|---|
| 2000 | 1.5 | 3.8 |
| 1000 | 1.3 | 2.9 |
| 600 | 1.1 | 2.9 |
| 425 | 0.9 | 2.8 |
| 300 | 0.6 | 2.5 |
| 150 | 0.5 | 2.4 |
Ash content of pulp measured by keeping samples in muffle furnace at 525 °C
| Ash content of pulp (%) | ||
|---|---|---|
| Sample Size (μm) | Sapwood pulp | Heartwood pulp |
| 2000 | 0.403 | 0.165 |
| 1000 | 0.419 | 0.162 |
| 600 | 0.425 | 0.165 |
| 425 | 0.430 | 0.168 |
| 300 | 0.438 | 0.171 |
| 150 | 0.443 | 0.173 |
Water retention value (WRV) of wood and pulp measured by using centrifugal method (2300 rpm for 15 min)
| Sample size (μm) | Sapwood | Heartwood | Sapwood pulp | Heartwood pulp |
|---|---|---|---|---|
| 2000 | 0.826 | 0.811 | 2.881 | 2.241 |
| 1000 | 0.829 | 0.807 | 2.906 | 2.262 |
| 600 | 0.822 | 0.813 | 2.954 | 2.279 |
| 425 | 0.827 | 0.820 | 2.998 | 2.290 |
| 300 | 0.829 | 0.832 | 3.033 | 2.304 |
| 150 | 0.840 | 0.849 | 3.061 | 2.333 |
FTIR Spectrum of the lignin in raw wood samples of size 425 μm. Peaks in the region 900–1800 cm−1 are characteristic of lignin and 1507 cm−1 indicates the occurrence of aromatic structures in the lignin and peak at 1735 cm−1 characteristic of carbonyl stretching of unconjugated ketone and carboxyl groups
The band around 1460 cm−1 representative of C–H deformations (asymmetric) is absent again in sample size of 425 µm (for both heartwood and sapwood). The band around 1339 and 1234 cm−1 representative of syringyl ring breathing with CO stretching is also absent in sample size of 425 µm (for both heartwood and sapwood pulp). This confirms the fact that the size reduction improves the delignifaction capacity of the wood, because lignin is removed not only from CML but also from the cell wall. The band around 1160, 1114 and 1055 cm−1 representative aromatic C–H in-plane deformation is present in all speactra’s shown in Figs. 4, 5 and 6. The band around 890 cm−1 representative of aromatic C–H out-of-plane deformation is present in all FTIR spectra’s, but intensity is low for sapwood pulp indicating the easier removal of lignin in smaller size (425 µm) sapwood samples. The presence of the peak at 1735 cm−1 in the FTIR spectra of raw wood (Fig. 6) could be due to the carbonyl (C=O) stretching vibration of the carboxyl groups of hemicellulose and lignin. Such peak is not observed in FTIR spectra of pulp samples shown in Figs. 4 and 5 except as a low intense peak for 2000 µm heartwood pulp. This confirms the fact that wood has more residual lignin than pulp, but cooking after size reduction can decrease the residual lignin content as shown in Table 2.
Conclusion
Most of the earlier research works were focused on the negative effect of heartwood on delignification of the total wood but not on heartwood in particular. From the experimental analysis, it can be concluded that though the amount of lignin is almost the same in heartwood and sapwood for the given species, it is difficult to remove lignin from heartwood than from sapwood. This could be due the blockage of vessels and accumulation of secondary compounds in heartwood. Hence pulp mills reject the wood logs having heartwood even in smaller quantities. This study concludes the relative difficulty of delignification of heartwood not only by using established experimental procedures of wood analysis but also using other non-standard experiments such as the water retention value test and ash content assessment. These results are in line with the results of the residual lignin estimation. To accept the wood logs with less quantity of heartwood, one strategic approach could be directed at nullifying or mitigating the negative effects caused by heartwood content after the reaction. This in effect is what is currently practiced in the industry and could be improved upon further.
Notes
Acknowledgments
We are thankful to Dr.Karthik Chetan, Mr. Appalanaidu, Mr. Raju, Mr. Appalareddy, Mr. Bipin Chakravarthy and Mr. Uday Kumar for their valuable suggestions.
References
- Adusumalli RB, Raghavan R, Ghisleni R, Zimmermann T, Michler J (2010) Deformation and failure mechanism of secondary cell wall in Spruce late wood. Appl Phys A Mater Sci Process 100(2):447–452CrossRefGoogle Scholar
- Bamber RK (1987) Sapwood and heartwood, vol 2. Forestry Commission of New South Wales, Wood Technology and Forest Research Division, Beecrolt, pp 1–7. ISBN: 0724020675Google Scholar
- Del Río JC, Gutiérrez A, González-Vila F, Martín F, Romero J (1998) Characterization of organic deposits produced in the Kraft pulping of Eucalyptus globulus wood. J Chromatogr A 823:457–465CrossRefGoogle Scholar
- Egas APV, Simão JPF, Costa IMM, Francisco SCP, Castro JAAM (2002) Experimental methodology for heterogeneous studies in pulping of wood. Ind Engin Chem Res 41:2529–2534CrossRefGoogle Scholar
- Fahlén J, Salmén L (2005) Pore and matrix distribution in the fibre wall revealed by atomic force microscopy and image analysis. Biomacromolecules 6:433–438CrossRefPubMedGoogle Scholar
- Fengel D, Wegener G (1989) Wood: chemistry, ultrastucture, reactions. Walter de Gruyter & Co, BerlinGoogle Scholar
- Gominho J, Pereira H (2000) Variability of heartwood content in plantation-grown Eucalyptus Globulus Labill. Wood Fiber Sci 32(2):189–195Google Scholar
- Gominho J, Figueira J, Rodrigues JC, Pereira H (2001) Within-tree variation of heartwood extractives and wood density in the Eucalyptus hybrid Urograndis (Eucalyptus Grandis x E. Urophylla). Wood Fiber Sci 33(1):3–8Google Scholar
- Higgins HG (1984) Pulp and paper. In: Hills WE, Brown AG (eds) Eucalyptus for wood production. CSIRO/Academic Press, Australia, pp 289–312Google Scholar
- Hillis WE (1987) Heartwood and tree exudates. Springer-Verlag, BerlinCrossRefGoogle Scholar
- Irvine GM, Clark NB, Recuperos C (1996) Extended delignification of mature and plantation Eucalypt wood. Part I: the principles of extended delignification. Appita J 49(4):251–257Google Scholar
- Kai Y (1991) In: Hon DNS, Shiraishi N (eds) Chemistry of extractives in wood and cellulosic chemistry. Marcel Dekker Inc., New York, pp 215–251Google Scholar
- Lourenço A, Baptista I, Gominho J, Pereira H (2008) The influence of heartwood on the pulping properties of Acacia melanoxylon wood. J Wood Sci 54:464–469CrossRefGoogle Scholar
- Lourenço A, Gominho J, Pereira H (2010) Pulping and delignification of sapwood and heartwood from Eucalyptus globulus. J Pulp Paper Sci 36(3–4):85–90Google Scholar
- Mariani S, Torres M, Fernandez A, Morales E (2005) Effects of Eucalyptus nitens heartwood in Kraft pulping. Tappi J 4(2):8–10Google Scholar
- Meerts P (2002) Mineral nutrient concentrations in sapwood and heartwood: a literature review. Ann For Sci 59:713–722CrossRefGoogle Scholar
- Meng L, Kang S, Zhang X, Wu Y, Sun R (2012) Comparative characterization of lignins extracted from cotton stalk based on complete dissolution in différent systems. Ind Eng Chem Res 51:9858–9866CrossRefGoogle Scholar
- Miranda I, Gominho J, Lourenço A, Pereira H (2007) Heartwood, extractives and pulp yield of three Eucalyptus globulus clones grown in two sites. Appita J 60(6):485–488Google Scholar
- Santiago AS, Neto CP, Vilela C (2008) Impact of effective alkali and sulfide profiling on Eucalyptus globulus kraft pulping. Selectivity of the impregnation phase and its effect on final pulping results. J Chem Technol Biotech 83:242–251CrossRefGoogle Scholar
- Smook GA (1992) Handbook for pulp & paper technologists. Angus Wilde publications Inc., VancouverGoogle Scholar
- Wimmer R, Downes G, Evans R, French J (2008) Effects of site on fibre, kraft pulp and handsheet properties of Eucalyptus globulus. Ann For Sci 65(6):602CrossRefGoogle Scholar
- Young RA (1994) Comparison of the properties of chemical cellulose pulps. Cellulose 1:107–130CrossRefGoogle Scholar





