油棕丝中密度纤维板的研制与开发

介绍开发油棕丝的必要性和可行性,工业性试验表明油棕丝MDF,其质量不亚于木质MDF,目前国内可提供成套的油棕丝MDF制造设备,不仅可以使国产人造板生产线进入国际市场,且为我国海南、广东、福建等地区开发利用油棕丝MDF创造了条件,拓宽了人造板生产的原料来源。     

The influence of the ethanol pumping of wheat straw and of the beating of pulp on the resulting paper sheets

This paper reports on the influence of independent variables in the pulping of wheat straw (viz. cooking temperature and time, and ethanol concentration), and of the number of PFI beating revolutions to which the pulp is subjected, on the yield and Shopper-Riegler index of the pulp, and on the breaking length, stretch, burst index and tear index of the resulting paper sheets. By using a central composite factor design and the BMDP software suite, equations that relate each dependent variable to the different independent variables were obtained that reproduce the experimental results for the dependent variables with errors less than 25% at temperatures, times, ethanol concentrations and numbers of PFI beating revolutions in the ranges 140–180°C, 60–120 min, 40–80% and 0–1750, respectively. Ensuring the optimal Shopper-Riegler index for the pulp (73.18°SR), and also the optimal breaking length (6276 m), stretch (2.57%) and burst index (3.72 kN/g) for the papers sheets, entails using a high temperature (180°C), a large number of PFI beating revolutions (1750) and medium-to-high ethanol concentration and time values; these conditions, however, decrease the tear index for the paper sheets below the optimum level (4.60 mNm²/g). A high temperature and a large number of PFI beating revolutions, in conjunction with a low ethanol concentration (60%) and a short time (60 min), can be used to save solvent and increase the production; the values thus obtained for the dependent variables differ by less than 30% from their optimum levels in the worst case.     

麦草碱性亚硫酸盐制浆生物炼制的研究(I) ——深度脱木质素及木质素磺化特性

提出了非木材木质纤维生物质碱性亚硫酸盐制浆(ASP)生物炼制的理念,研究了总用碱量、亚硫酸化度、温度和时间对麦草碱性亚硫酸盐法蒸煮深度脱木质素特性和木质素磺化的影响。结果表明:麦草ASP法具有高的深度脱木质素选择性;深度脱木质素延伸与木质素磺化度提高具有一致性;总用碱量、亚硫酸化度、最高温度和保温时间对深度脱木质素选择性和木质素磺化度都有重要的影响;在总碱用量18.0%,亚硫酸化度85.0%,液比值3.5,最高温度168℃,保温150 min的条件下,可制得卡伯值8.8,得率56.8%,黏度为33.3 mPa.s的优良纸浆,此时黑液中磺化木质素磺酸基含量达2.16 mmol/g(以固形物计)。从深度脱木质素选择性、木质素磺化和纸浆基本特性考虑,麦草ASP法具有制浆生物炼制的前景。     

Influence of the chemical composition of kenaf bast and core on the alkaline pulping response

The bast and core of kenaf,Hibiscus cannabinus L., have markedly different chemical components and alkaline cooking responses. The bast had about double the hot-water extractives content and only about half the lignin content of the core. The core contained a large amount of hemicellulose, mostly composed of xylan. The lignin structures of bast and core were also quite different: The former had a significant abundance of syringyl structures. Evidence showed that the bast was much more easily delignified than the core. When the bast and core were cooked together in alkaline condition, the pulp yields at the same kappa number were higher than those of the individual pulpings of bast and core. The bast-core pulping gave a positive effect on the yield of bast pulp in the sodaanthraquinone and kraft pulpings. On the other hand, kenaf was abundant in the hot water extractives. These extractives consumed alkali during cooking to a relatively large extent but acted as a protector of hemicellulose and slightly increased the pulp yields.Part of this paper was presented at the 48th and 49th Annual Meetings of the Japan Wood Research Society, Shizuoka, April 3–5, 1998 and Tokyo, April 3–5, 1999     

Prehydrolysis of beechwood

Summary The kinetics of the isothermal prehydrolysis of beechwood at 160°C and 170°C were investigated. It was shown that the hydrolysis of the hemicellulose portion was realised in two phases. The depth and rate of the first rapid prehydrolysis phase and the second slow phase depend on the temperature used. The lignin content in the prehydrolysed chips increased with the duration of the prehydrolysis due to the easily removable hemicellulose portion. The maximum amount of lignin extracted was gained after 45–60 minutes of isothermal prehydrolysis at 160°C with the yield decrease to 82–80 per cent and at 170°C with the yield decrease to 70–68 per cent. At the temperature of 160°C the amount of the lignin portion extracted was about 5 per cent and at 170°C at about 10 per cent of the whole lignin content in wood. The extraction of the whole hemicellulose portion present in wood was attained at 160°C after 5 hours prehydrolysis time, at 170°C after 80 minutes.By the prehydrolysis of hardwood to 30 per cent loss of the wood substance highly purified dissolving pulp was prepared by AQ catalysed sodium pulping. The pulp attained was characterised by a high alpha-cellulose content over 97 per cent and a low solubility in solutions of alkali. The sulphur-free delignification together with the low consumption of active chlorine (1.5–1.7 per cent) cause less environmental pollution.     

OH法制浆工艺研究

研究了在氨水中添加少量钾碱作为蒸煮剂的稻草制浆新工艺，系统讨论了蒸煮液的用量和配比，液固化，蒸煮最高温度和保温时间对蒸煮效果的影响，继而确定了适宜工艺条件，结果表明，该蒸煮体系对稻草木质素的脱除率达到85．12％，纸浆得率38．12％，通过红外光谱（IR）测定了稻草蒸煮过程中木质素的结构变化，蒸煮黑液中因富含氮、磷、钾和有机质，可作为有机肥料资源用于农业生产，该工艺有望实现禾草类原料制浆工艺的清洁生产。     

麦草低温氧碱蒸煮黑液降黏技术

麦草经碱法蒸煮后,所得浆料不经洗涤,直接通入氧气进行处理。以黑液黏度,浆料卡伯值为考核指标,设置4因素3水平正交试验,对试验结果作极差分析发现,在用碱量0～2%、氧压0.2～0.6 MPa、温度70～100℃和时间30～90 min内得到较适宜的工艺条件为:用碱量1%,氧压0.6 MPa,温度85℃,时间60 min。氧碱蒸煮结果为:黑液黏度3.4 mPa.s,浆料卡伯值17.9。与第一段碱法蒸煮相比,黑液黏度降低33.3%,浆料卡伯值降低11.8%。     

Phylogenetic and pathogenicity evaluation of the marasmioid fungus Marasmius palmivorus causing fruit bunch rot disease of oil palm

Marasmius palmivorus is a marasmioid fungal species that exhibits parasitic behaviour, although most marasmioids are rarely parasitic. The fungus has been reported to cause fruit bunch rot disease of oil palm and coconut, but only a few studies on its pathogenic behaviour are available, particularly on oil palm. Hence, there is a need to assess the ability of the fungus to act as a pathogen and to study its molecular evolution and taxonomy. Nine isolates of M. palmivorus were successfully isolated from basidiocarps and diseased fruitlets of oil palm collected from oil palm plantations and were morphologically characterized on potato dextrose agar (PDA) followed by molecular identification based on nucleotide sequence alignments of internal transcribed spacer (ITS) regions of ribosomal RNA (rRNA) gene clusters with sequences from GenBank. Koch's Postulates confirmed that M. palmivorus could infect oil palm fruitlets with symptoms similar to those observed for bunch rot disease. Molecular phylogenetic studies using nucleotide sequences of ITS and the nuclear ribosomal large subunit (nLSU) showed that isolates sharing the same phenotypic characteristics of Marasmius palmivorus and Marasmiellus palmivorus are monophyletic and share a common ancestor. The fungus has also been shown to be more closely related to the genus Marasmius than Marasmiellus; therefore, we support retention of the taxon name of the pathogen causing bunch rot disease of oil palm as Marasmius palmivorus.     

Use of butanol-water mixtures for making wheat straw pulp

Summary A central composite design was used to investigate the influence of the cooking conditions (time, temperature and butanol concentration) for wheat straw with butanol-water mixtures on the properties of the pulp obtained (yield and holocellulose, α-cellulose, lignin and ethanol-benzene extractives contents) and the pH of the resulting waste water. A second-order polynomial model consisting of three independent process variables was found to accurately describe the organosolv pulping of wheat straw. The equations derived predict the yield, the holocellulose, α-cellulose, lignin and ethanol-benzene extractives contents of the pulp, and the pH of the waste water with multiple-R, R², adjusted-R² and Snedecor' F values of 0.99, 0.99, 0.99 and 310.33; 0.98, 0.97, 0.95 and 56.63; 0.91, 0.84, 0.74 and 9.14; 0.99, 0.98, 0.96 and 70.52; 0.97, 0.94, 0.92 and 40.42; and 0.98, 0.95, 0.93 and 49.33, respectively. The process variables must be set at low values in order to ensure a high yield and pH. On the other hand, if a high holocellulose content and low lignin and ethanol-benzene extractives contents are to be obtained, then the process variables must be set at high values. Finally, obtaining pulp with a high α-cellulose content entails using a long cooking time and a high temperature, as well as a low butanol concentration. Received 1 July 1996     

Characteristics of lignin obtained from steam-exploded softwood with soda/anthraquinone pulping

Lignins were obtained from a mixture of softwood sawdust using a hydrolytic pretreatment and a subsequent soda-anthraquinone delignification/pulping stage. Their potential uses and the effect of the pretreatment conditions on the yield (% of recovered lignin from black liquors) and chemical composition of isolated lignins were evaluated. The severity factor used combined the temperature and time of the hydrolytic process in a single ordinate (R_o). The severity range was modified from log R_o = 2.6 to log R_o = 4.6 and the pulping conditions were constant throughout the experiments. The effect of the cooking time on the chemical composition of precipitated lignins was also studied between 135–170 min for original (non-pretreated) material. Yield, elemental analysis, molecular weight distribution, Fourier transform infrared spectra (FTIR), structure, and the methoxyl and aliphatic/aromatic alcohol content of the various lignins, were compared.     

Influence on pulping yield and pulp properties of wood density of Acacia melanoxylon

Wood density and pulp yield are key parameters in the evaluation of tree productivity and quality for pulping and their relationships are of high practical importance. The influence of wood density on pulp yield and other pulp quality parameters was investigated using Acacia melanoxylon and its natural variability as a case study. Twenty trees were harvested (five trees in each of four sites in Portugal), and wood discs taken at different height levels, from the base to the top of the tree, providing 100 wood samples, covering the natural variability of wood density ranging from 449?kg?m^?3 to 649?kg?m^?3. Under the same experimental conditions of kraft pulping, screened pulp yield ranged 47.0?C58.2?%, Kappa number 10.9?C18.4, ISO brightness 14.9?C45.6, fibre length 0.660?C0.940?mm and fibre width 16.2?C22.9???m. The pulp yield and Kappa number were not correlated with wood density. Higher pulp yields were associated with lower Kappa numbers and alkali consumption, suggesting the important role of chemical composition of wood on kraft cooking. The results confirm the high pulping potential of Acacia melanoxylon trees grown in Portugal and suggest the possibility of tree selection using both wood density and pulp yield.     

Wood-to-bark adhesion of subalpine fir (<Emphasis Type="Italic"> Abies lasiocarpa</Emphasis>) in extreme temperatures

Wood-to-bark adhesion strengths were tested at 25 to –78°C under moisture contents of 0–200%. The freezing temperature of the cambium appeared to be between –20 and –40°C. The low freezing temperature was assumed to be due to the high pectin and protein contents in the cambium cells. At temperatures above the freezing point of the cambium (–20 to 25°C), the adhesion strength was curvilinearly and negatively related to moisture content. At temperatures below the freezing point of the cambium (–40 to –78°C), adhesion strength was not correlated with moisture content. For practical application, maintaining logs at high moisture content and temperatures above –20°C would assure a good debarking and yield high quality wood chips for pulping, with less wood loss to hog fuel.     

Combination treatment of kenaf bast fiber for high viscosity pulp

The viscosity of kenaf bast fiber has been found to be highly sensitive and variable with different pulping methods; therefore, it is important to choose proper chemicals and conditions for pulping and bleaching of kenaf bast fiber. From several pulping experiments, a nonconventional pulping method with a combination of ammonium oxalate pretreatment followed by soda pulping at normal pressure and then acidic chlorite delignification was developed to obtain high-viscosity pulp (162 centipoise). The optimum level of alkali dosage of soda pulping for high-viscosity pulp was found to be 15% (on pulp as NaOH). Pulps showed linear relations between viscosity and xylose or glucose contents, but the combination pulping method gave extremely high pulp viscosity, beyond the relations. The highest viscosity pulp from kenaf bast fiber demonstrated a tear index about twofold and a folding endurance 6.2-fold higher than those of Manila hemp pulp with comparable tensile and burst indexes. The high-viscosity pulp could be used in the production of high-quality currency paper or longevity paper for special uses.Part of this paper was presented at the 43rd Lignin Symposium, Fuchu, Tokyo, October 26–27, 1998     

A mathematical model of kraft pulping related to the alkali concentration in the cooking liquor

Summary A new mathematical model for checking and controlling the kraft pulping process has been derived. The model is based on the modified relationship between the lignin content and the alkali concentration of a cooking liquor expressed as the ratio of lignin/active alkali vs. concentration of the active alkali in a cooking liquor. The derived model characterizes the variation of the lignin content of the partially delignified wood or pulp with the concentration of the residual alkali in a cooking liquor during an entire pulping cycle, i.e. during the initial, transition, bulk and residual phases of the kraft delignification. The relationship between the lignin content of the partially delignified wood ships or pulp and the concentration of the residual alkali in a cooking liquor is expressed by the logarithmic straight line equation or its power form. The slope and intercept constants of the derived equation for the individual phase of delignification have different values. Received 5 June 1996     

The formation of LC and other aromatic end-group structures in <Emphasis Type="Italic">O</Emphasis>-alkyl-substituted cellulose during kraft pulping conditions

Ultraviolet resonance Raman spectroscopy (UVRRS) was used to study the formation of aromatic and/or lignin-carbohydrate (LC) structures at the reducing end groups of O-alkyl-substituted cellulose under conditions simulating the initial phase of kraft pulping. The derivatives studied were methyl cellulose (MC) with degree of substitution (DS) of 1.64–1.95, carboxymethyl cellulose (CMC) with DS ∼0.6, and a lignin model compound, creosol. The total alkali concentrations in the treatments were 0.1 M and 0.5 M and the sulfidities were 1%, 10%, and 30%. HS⁻ ions and creosol are both strong nucleophiles and they compete for the hot-alkali-generated unsaturated electrophilic reaction sites in the reducing end groups of the polysaccharides. The results indicated that conditions similar to those in the initial phase of conventional kraft cooking (high OH⁻ and low HS⁻ ion concentrations) increased the aromatic nature of the end groups and conditions similar to those in the initial phase of super batch cooking (low OH⁻ and high HS⁻ ion concentrations) partly inhibited the formation of aromatic and LC end groups.     

Eucalyptus wood decay: effects on productivity and quality of cellulose

We evaluated the effect of wood decay, caused by fungi Hypoxylon spp., on pulp productivity and quality. Wood samples with different proportions of contamination (0, 25, 50, 75, and 100%) were used to produce Kraft pulp under the same pulping conditions. In the second step, cookings were performed to achieve the same Kappa number (Kn = 17 ± 1), varying only the alkali charge. Wood and pulp were also analysed by scanning electron microscope (SEM). The risk of occurrence of wood decay reached its maximum between September and October, under inappropriate storage conditions and juvenile wood without bark. It was observed that the increase in the decayed content (DC) of wood chips affected the Kappa number (Kn), according to the model Kn = 1/(0.0595?0.00324*DC^0.34102). An increase of 38.7% of alkali charge was necessary to reach the same Kappa number with decayed wood. The yield for the contaminated wood was lower (48%) when compared to non‐contaminated wood (53%). Once contaminated, the wood chips demand more severe cooking conditions because of the difficulty of impregnation. This condition affected the pulp quality, reducing its viscosity by 30% and hemicelluloses content by 5%. In addition, losses of resistance were also observed in the final pulp, where the zero span and tensile indexes were reduced by 5 and 16%, respectively. The SEM observations showed that the ascostroma fungi tissue was not totally degraded during the Kraft process, resulting in the deposition of pitch on fibres. Considering the results achieved, it was possible to conclude that the eucalyptus wood decay, caused by the fungi Hypoxylon spp., significantly affects the pulp process and quality.     

欧美杨107杨正常木与应拉木制浆造纸性能比较

选取直立和倾斜欧美杨107杨为研究材料,根据正交试验确定正常木和应拉木最佳制浆条件,比较正常木和应拉木的制浆造纸性能,通过提高打浆转数对应拉木纸张性能的提高进行探讨。结果表明:正常木的最佳制浆条件为用碱量15%、最高温度164℃、最高温度保温时间75min;而应拉木最佳制浆条件为用碱量13%、最高温度160℃、最高温度保温时间40min。用碱量对正常木和应拉木制浆得率和卡伯值影响的通径系数在不同水平上显著。通过对正常木和应拉木制浆造纸性能比较发现,应拉木比正常木制浆得率高、卡伯值低、纸张力学性能均低,且抗张指数和耐破指数差距较大(约2倍),而撕裂指数差距较小。正常木和应拉木之间卡伯值、制浆得率、抗张指数、耐破指数均在0.001水平上差异显著,撕裂指数在0.05水平上差异显著。结合纸张断口形貌分析认为,胶质层的存在使得应拉木纤维成纸时不容易扁平坍陷,极大地阻碍了成纸时纤维之间的结合,因此降低了纸张力学性能;但是,由于其胶质层纤维素含量很高,因此其制浆性能优于正常木。随着打浆转数的提高,应拉木纸张力学性能增强,且接近正常木纸张水平,但过高会降低纸张力学性能。     

Study of extraction of phytosterol from masson pine raw tall oil

The conditions for the extraction of phytosterol from masson pine raw tall oil were studied by experimenting with the procedural steps that included saponification, extraction, crystallization, and recrystallization. The influences of alkali dosage, saponifying temperature, saponifying time, and variety and dosage of extracting agent on the yield of unsaponifiables were investigated. The effects of various solvents used for removing residual soap from unsaponifiables and the effects of crystallization temperature, time, and solvent on the yield and composition of crystal in the processes of crystallization and recrystallization were examined to determine suitable technical conditions. The phytosterol obtained using optimal conditions contained 92% -sitosterol and 8% campesterol. Its melting point and yield were 135.7°–136.8°C and 0.54% (based on the weight of crude tall oil), respectively.     

High-yield pulping of aspen wood: Relation between pulp properties and fibre characteristics by multiple linear regression

Summary High-yield pulps have been obtained by means of steam explosion pulping. This process was carried out as follows: 1) chips soak impregnation (60 °C, 24 h, L/C = 6) in solutions containing 8% Na₂SO₃ and a variable concentration of either Na₂CO₃ or NaHCO₃, ranging from 0 to 2%; 2) cooking at high temperature (190–200 °C) for short time (2-1 min); 3) rapid pressure release. This work shows that mechanical properties were substantially improved when adding a second chemical to the Na₂SO₃ impregnation solution. Moreover, refining energy requirement was significantly reduced. However, the higher chemical charge used made the optical properties drop. In this paper, mathematical models have been proposed in order to accurately predict specific refining energy and paper properties from sulfonate content and pulp yield. In addition, the relative importance of these two parameters has been studied.Thanks are due to the Natural Science and Engineering Council of Canada (NSERC) and Fonds pour la Formation de chercheurs et l'aide à la recherche of Quebec (FCAR) for their financial support.     

Comparison of Quality of Pulping and Paper-Making between Normal Wood and Tension Wood of Poplar Clone 107(Populus×euramericana‘Neva’) Tree

Both of straight and inclining poplar clone 107 tree were selected for studying materials in this paper.The optimal pulping conditions was established by orthogonal experimental design both for normal wood and tension wood,and the quality of pulping and paper-making between normal wood and tension wood was compared with each other. Finally,potential application for improving paper quality of tension wood through increasing beating revolutions was discussed.The result showed that the optimal cooking condition for normal wood was alkali concentration 15%,the highest temperature 164℃,time at highest temperature 75 min,and for tension wood it was alkali concentration 13%,the highest temperature 160℃,time at highest temperature 40 min.Path coefficient of effect of alkali concentration both on pulp yield and kappa value was significant at different levels.By comparison between average result of normal wood and tension wood in quality of pulping and paper-making,it was found that tension wood had higher pulping yield and lower kappa value than normal wood. Furthermore,for all mechanical properties of paper, normal wood hold higher value than tension wood, and even near two times than tension wood,such as burst index and tensile index.However,difference of tear index was quite narrow.Result of one way ANOVA showed that difference of burst index and tear index between normal wood and tension wood was significant at the 0.001 level,of tear index was significant at the 0.05 level.Based on observation of cross surface of paper,it was assumed that contribution of gelatinous layer to rigidity of single fiber had hampered collapse and compression of fiber during paper formation,which is essential for exerting combination between fibers in paper.So, mechanical properties of tension wood paper were decreased accordingly.However,owing to high cellulose content of gelatinous layer,tension wood was easier to pulping than normal wood.Mechanical properties of tension wood paper could be improved by increasing beating revolutions,