Journal of Textile Research ›› 2026, Vol. 47 ›› Issue (04): 80-87.doi: 10.13475/j.fzxb.20250802501

• Fiber Materials • Previous Articles     Next Articles

Preparation of camphor wood pre-hydrolysis kraft dissolving pulp

LI Yuanjuan1, ZHOU Hengshu1,2,3,4(), XU Yi1,2,3,4, XIONG Haiying5   

  1. 1 School of Textile and Fashion, Hunan Institute of Engineering, Xiangtan, Hunan 411104, China
    2 Hunan Provincial Engineering Research Center for Short-Process Intelligent Textiles, Xiangtan, Hunan 411104, China
    3 Hunan Provincial University Key Laboratory of Intelligent Textile Processing Technology, Xiangtan, Hunan 411104, China
    4 Hunan Provincial Engineering Technology Research Center for Advanced Fiber Materials and Textile Processing, Xiangtan, Hunan 411104, China
    5 Hunan Fiber Quality Monitoring Center, Changsha, Hunan 410117, China
  • Received:2025-08-11 Revised:2026-01-29 Online:2026-04-15 Published:2026-04-15
  • Contact: ZHOU Hengshu E-mail:280434272@qq.com

Abstract:

Objective As a popular type of urban landscaping tree, camphor trees (cinnamomum camphora) generate substantial amounts of discarded trunks and branches annually. However, China has long relied on imports to meet its demand for high-grade dissolving pulp used in textile fiber production. To achieve value-added utilization of camphor wood resources and develop novel raw material sources for producing dissolving pulp, this study investigates the preparation process of camphor wood dissolving pulp using discarded trunks and branches as feedstock.

Method The camphor wood dissolving pulp was prepared by the pre-hydrolysis kraft process. First, camphor wood chips were subjected to hot water pre-hydrolysis to remove most hemicellulose, with single factor experiments to investigate how different process conditions would affect the pre-hydrolysis. Subsequently, the pre-hydrolyzed wood chips underwent kraft cooking using NaOH and Na2S to eliminate lignin, and orthogonal experiments was employed to determine optimal cooking parameters. Finally, the obtained pulp was bleached through a four-stage elemental chlorine-free (ECF) bleaching sequence, whick are ClO2 bleaching (D1), alkali refining treatment (E), ClO2 bleaching (D2), and H2O2 bleaching (P), to improve pulp quality. The prepared dissolving pulp was then tested for degree of polymerization, α-cellulose content, and brightness, while its surface morphology was examined by scanning electron microscopy.

Results The hot water pre-hydrolysis process was found effective in removing a substantial portion of hemicellulose from camphor wood. The single-factor variable study revealed that the contents of pentosan and holocellulose exhibited non-monotonic trends with increasing pre-hydrolysis temperature or prolonged holding time, while variations in the solid-to-liquid ratio showed no significant effect on their contents. For the kraft cooking process, given the stringent requirements for dissolving pulp regarding degree of polymerization, α-cellulose content, and brightness, a comprehensive evaluation through orthogonal experimental analysis indicated the following order of parameter influence: alkali charge > sulfidity > holding time > cooking temperature. The optimal conditions were determined as 22% alkali charge, 25% sulfidity, and a holding time of 120 min at 160 ℃. Under these conditions, the resulting camphor wood pulp exhibited a polymerization degree of 1 035.85, an α-cellulose content of 90.63%, and a brightness of 21.35%. During ECF bleaching, the stepwise removal of lignin through the four-stage D1ED2P sequence increased the pulp brightness to 78.91%, while simultaneously elevating the α-cellulose content and reducing the polymerization degree. SEM observations indicated that the original camphor wood surface contained abundant tubular pores, facilitating the penetration of pre-hydrolysis and cooking liquors. After the pre-hydrolysis kraft treatment, complete fiber separation was achieved due to the extensive removal of lignin and hemicellulose. The liberated fibers displayed a flattened morphology with surface wrinkles and grooves.

Conclusion Pre-hydrolysis effectively removes hemicellulose, with the contents of pentosan and holocellulose showing non-monotonic variations depending on pre-hydrolysis temperature and duration. Orthogonal experiments revealed that the influencing order of kraft cooking parameters was alkali charge > sulfidity > holding time > cooking temperature. The optimal conditions were determined as: 22% alkali charge, 25% sulfidity, 120 min holding time, and 160 ℃ cooking temperature. After four-stage ECF bleaching (D1ED2P sequence), the resulting dissolving pulp exhibited satisfactory properties, with 914.75 of polymerization degree, 94.17% α-cellulose content, 78.91% brightness, 0.42% ash content, and 10.62 mg/kg iron content, meeting essentially the requirements for regenerated cellulose fiber pulp. This indicates that camphor wood can serve as a high-quality raw material for producing dissolving pulp for spinning. However, further process optimization is necessary to enhance pulp brightness and reduce ash content. This study demonstrates a viable approach for the value-added utilization of camphor wood waste resources, with the prepared dissolving pulp satisfying the requirements for textile fiber applications and showing promising potential for industrial-scale implementation.

Key words: camphor wood, pre-hydrolysis, kraft, dissolving pulp, chemical pulp, pulp, cellulose fiber

CLC Number: 

  • TS102.2

Fig.1

Preparation process of camphorwood dissolving pulp"

Tab.1

Factor-level table for orthogonal experiment"

水平 A
用碱量/%
B
硫化度/%
C
蒸煮温度/℃
D
保温时间/min
1 18 15 160 60
2 20 20 165 90
3 22 25 170 120

Tab.2

Parameters of bleaching process"

漂段 漂白剂
名称
漂白剂
质量分
数/%
浆粕质
量分
数/%
温度/
反应时
间/min
pH值
D1 ClO2 3.6 10 70 90 3~4
E NaOH 2.0 10 75 60
D2 ClO2 0.9 10 70 90 3~4
P NaOH
H2O2
2.5
2.5
10 70 90

Tab.3

Main chemical composition content of camphor wood, eucalyptus and poplar"

材种 不同化学成分含量/%
综纤维素 聚戊糖 总木质素 热水抽出物 1%NaOH抽出物 苯-醇抽出物 灰分
樟木 84.87 22.27 20.88 4.23 14.90 4.05 0.93
桉木[17] 77.90 21.37 25.43 1.50 11.40 1.10
杨木[17] 81.36 22.65 24.40 1.20 16.10 1.80

Tab.4

Effect of temperature on pre-hydrolysis process"

温度/℃ 得率/% 综纤维素含量/% 聚戊糖含量/%
150 84.85 68.00 7.13
160 76.90 60.54 7.65
165 76.17 57.95 10.55
170 73.35 59.80 7.99

Tab.5

Effect of holding time on pre-hydrolysis process"

保温时间/min 得率/% 综纤维素含量/% 聚戊糖含量/%
60 78.59 60.19 11.67
90 76.17 57.95 10.55
120 75.69 58.78 9.83
180 74.68 58.34 7.65

Tab.6

Effect of solid-to-liquid ratio on pre-hydrolysis process"

固液比 得率/% 综纤维素含量/% 聚戊糖含量/%
1∶4 76.20 59.53 9.97
1∶5 76.17 57.95 10.55
1∶6 76.10 59.77 8.67
1∶7 75.35 60.66 9.98

Tab.7

Results and analysis of orthogonal experiment for sulfate cooking process"

试验号 A
用碱量
B
硫化度
C
蒸煮温度
D
保温时间
聚合度 α-纤维素含
量/%
白度/%
1 1 1 1 1 926.19 90.59 16.06
2 1 2 2 2 811.80 90.95 21.50
3 1 3 3 3 1 519.11 89.66 21.65
4 2 1 2 3 1 157.68 87.71 21.90
5 2 2 3 1 948.60 92.55 16.79
6 2 3 1 2 963.82 90.97 18.73
7 3 1 3 2 896.74 91.18 24.19
8 3 2 1 3 1 005.21 93.22 23.34
9 3 3 2 1 842.67 94.17 24.23
聚合度 K1 3 257.10 2 980.61 2 895.22 2 717.46 因素主→次DBCA
最优方案D3B3C3A1
K2 3 070.10 2 765.61 2 812.15 2 672.36
K3 2 744.62 3 325.60 3 364.45 3 682.00
极差R 170.83 186.66 184.10 336.55
α-纤维
素含量
K1 271.20 269.48 274.78 277.31 因素主→次ABDC
最优方案A3B2D1C1
K2 271.23 276.72 272.83 273.10
K3 278.57 274.80 273.39 270.59
极差R 2.46 2.41 0.65 1.40
白度 K1 59.21 62.15 58.13 57.08 因素主→次ADCB
最优方案A3D3C2B3
K2 57.42 61.63 67.63 64.42
K3 71.76 64.61 62.63 66.89
极差R 4.78 0.99 3.17 3.27

Tab.8

Properties of camphorwood dissolving pulp before and after bleaching"

漂白
前后
聚合
α-纤维
素含量/
%
白度/
%
灰分含
量/%
铁离子
含量/
(mg·kg-1)
漂白前 1 035.85 90.63 21.35
漂白后 914.75 94.17 78.91 0.42 10.62

Fig.2

Apparent morphology of camphor wood chips and pulp. (a) Camphor wood chip; (b) Pre-hydrolyzed camphor wood chips; (c) Camphor unbleached pulp; (d) Camphor bleached pulp"

Fig.3

FT-IR spectra of camphorwood and its dissolving pulp"

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