尾巨桉制浆工艺及机理研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
论文以尾巨桉为原料,测定其材性,并采用不同制浆方法、生物预处理及不同漂白程序,添加表面活性剂和干强剂,对其制浆适应性进行了系统研究,为尾巨桉的工业应用提供数据和理论指导。
     对尾巨桉材性和APMP制浆工艺及其机理进行研究,结果发现:尾巨桉相比于其它桉木的综纤维素含量高(75.8%),木材色泽较浅,基本密度比较小(0.487g/cm~3),纤维长宽比最大61,柔性系数比较大;得到尾巨桉APMP较适宜的化学预处理条件,尾巨桉APMP的白度达到了66%ISO,运用NOSA统计软件对试验结果进行了方差分析,得出了尾巨桉APMP裂断长、白度与化学预浸条件的回归方程。
     对不同立地条件下尾巨桉KP-AQ的制浆工艺进行研究。研究发现东门和雷州尾巨桉材性差别不大。得出东门和雷州尾巨桉尾巨桉KP-AQ制浆的蒸煮工艺条件比较相近。
     对雷州尾巨桉KP-AQ浆进行漂白研究,得出常规D_1-E-D_2-P漂后浆白度为81.1%,黏度为972mL/g。通过丙酮抽滤后,白度上升到83.2%;用Mg(OH)_2代替NaOH的漂后浆白度为81.0%,黏度为931mL/g;原浆经氧漂后白度为58.4%,黏度为914mL/g,卡伯值为7.76;O-D_1-E-D_2漂后纸浆白度为86.0%,黏度为872mL/g;O-D-E-P漂后纸浆白度为85.4%,黏度为883mL/g。
     用T.lanuginosus产木聚糖酶预处理雷洲尾巨桉KP-AQ浆,得出最佳工艺条件为:木聚糖酶用量10U/g,反应时间90min,处理温度60℃,pH值6.0,浆浓度10%。纸浆白度为55.2%,卡伯值为8.38。纸浆黏度有所提高,木聚糖酶助漂后纸浆物理强度有所增加。研究生物漂白机理得出:木聚糖酶处理后,浆中聚戊糖的含量下降了3.51%,酸不溶木素含量下降了0.12%。经X射线衍射仪分析,木聚糖酶处理前后纤维素的结晶度变化不大。扫描电镜分析得出,未经木聚糖酶预处理纸浆纤维表面比较光滑,结构紧密。经过预处理浆纤维表面出现了孔隙。对照浆和酶解浆的红外光谱和酶解液紫外光谱分析得出,木聚糖酶生物处理后纤维上产生游离羟基,增加了纤维间的氢键结合。木聚糖酶降解了纸浆中的部分木聚糖,溶出纸浆中的少量木素。与其它木聚糖酶相比,由T.lanuginosus产木聚糖酶预处理浆料黏度提高,酶用量少。
     雷洲尾巨桉KP-AQ浆TCF漂白的O-X-Mn-P中,纸浆白度达到80%,而黏度在800mL/g以上;轻(超轻)ECF工艺漂白尾巨桉KP-AQ浆,O-X-A-D_1-Ep-D_2漂白效果较好。总用氯量为0.95%时,纸浆白度达到85%以上。比达到相同白度的常规ECF(O-D_1-E-D_2)节省60%ClO_2,比O-D_1-Ep-D_2漂白工艺节约40%ClO_2,降低了漂白废水污染负荷。
     研究了表面活性剂在尾巨桉AS-AQ制浆及其各段漂白中的作用及机理。得到了添加LAS尾巨桉AS-AQ蒸煮的最佳条件,LAS能够使纸浆得率增加,白度提高,黏度增加,保水值增加,苯醇抽出物降低;加入LAS并没有使蒸煮液中蒽醌颗粒的粒径减小,蒸煮液中小于0.45μm粒径的蒽醌浓度在常温下比无LAS要低35%;LAS使木片内部的蒽醌含量大幅度的增加,使100℃和120℃的磺酸基数量提高了。
     在氧漂过程中最优的助剂为复合型表面活性剂(0.25%LAS和0.25%AEO-9)使白度增加3.6度,卡伯值降低1.3,黏度稍有降低;木聚糖酶在Tween80加入量20mg/mL时,酶活达到最大并提高27%;H_2O_2漂白的最佳助剂为NP系列,加入0.25%NP-10和0.75%NP40时,HLB值为16.1时效果最佳;在O-X-Q-P各段均加入助剂,可以使白度增加5.1度,手抄片纸浆物理强度增加。
     研究了添加壳聚糖类和淀粉类干强剂的效果。通过壳聚糖接枝共聚物的合成,将其应用在尾巨桉KP-AQ浆中。结果表明,CTSAD(壳聚糖-丙烯酰胺-二甲基二烯丙基氯化铵)比CTS(壳聚糖)各项物理强度指标提高明显,且用量较少。电子显微镜下看出,加入助剂后纤维交织状况更加密集,尤其加CTSA后,纤维交织的密集程度较之空白纸样有很大提高。
     探讨了阳离子淀粉-丙烯酰胺二元接枝共聚物、CTSAD三元接枝共聚物及混合使用工艺条件及其增干强效果。接枝率为35.59%阳离子淀粉-聚丙烯酰胺应用效果很好。用量在0.8%,打浆度在46°SR附近,成纸的撕裂指数由4.7mN·m~2/g提高到9.5mN·m~2/g,耐折度由229次提高到278次,抗张指数由74.70N·m/g提高到147.94N·m/g。对于混合增强剂,在反应温度40℃,pH8.5,阳离子淀粉-丙稀酰胺二元接枝共聚物与C他SAD三元接枝共聚物之比为5:5时,纸张的撕裂度、耐折度、抗张指数分别得到显著提高,并为碱性造纸和低定量造纸提供可能。
Using E.urophylla×grandis as the material,this research systematically studied the pulpability with different pulping methods,bio-pretreatment and bleaching sequence,by adding surfactant and reinforcing agent,which can be very useful for the industry application of E.urophylla×grandis.
     The study of the physical properties of E.urophylla×grandis and APMP pulping process showed that E.urophylla×grandis contained more homocellulose(75.75%),had lighter color and lower base density(0.487g/cm~3) with the length-width ratio of 61.0 and a fairly large flexibility index.The appropriate APMP chemical pretreatment conditions for E.urophylla×grandis were as follows:for the 1~(st) stage presoak,5.5%of NaOH,1%of H_2O_2,1%of Na_2SiO_3,0.5%of MgSO_4,0.3%of EDTA,were added,and the process lasted 45min at 75℃with the wood to liquor ratio at 1:4;for the 2~(nd) stage presoak,2.5%of NaOH,5%of H_2O_2,3%of Na_2SiO_3,0.5%of MgSO_4,0.3%of EDTA were added,and the process lasted 45min at 75℃with the wood to liquor ratio at 1:5.The brightness of E.urophylla×grandis APMP pulp reached 66%ISO,NOSA statistic software was applied to analyze the variance of data,the regression equation of breaking length,brightness,and presoak condition were obtained.
     The study of the pulpability of E.urophylla×grandis KP-AQ was studied at different planted distance.It was found that the physical properties of Dongmen E.urophylla×grandis and Leizhou E.urophylla×grandis were almost same.So the KP-AQ cooking condition of E.urophylla×grandis Dongmen and Leizhou E.urophylla×grandis in southern China was quite similar.
     The study of the bleachability of Leizhou E.urophylla×grandis KP-AQ showed that after D_1-E-D_2-P bleaching,pulp brightness was 81.1%and the viscosity was 972mL/g.Brightness increased to 83.2% after it was extracted treatment by acetone.Pulp brightness reached 81.0%and its viscosity was 931mL/g when NaOH was replaced by Mg(OH)_2.GE brightness reached 58.4%,viscosity was 914mL/g and Kappa number was 7.76 after the D_1-E-D_2-P bleaching.Brightness and viscosity became 86.0%and 872mL/g respectively after the O-D_1-E-D_2 bleaching.After O-D-E-P bleaching,they were 85.4%and 883mL/g respectively.
     The optimum conditions to pretreat Leizhou E.urophylla×grandis by using T lanuginosus were:10 U xylanase/g pulp,reaction time 90 min,temperature 60℃,pH 6.0 and consistency 10%.Pulp brightness was 55.2%,its kappa number decreased to 8.38 and the viscosity rose slightly.The strength properties increased slightly after bleaching.After studying bleaching mechanism,it was found that xylan in pulp decreased by 3.51%,and its acid indissoluble lignin decreased by 0.12%.XRD did not show considerable change in crystallinity.The SEM study showed the pulp had a more compact structure and smoother surface without xylanase pretreatment.IR and UV spectra proved that free hydroxyl may increase hydrogen bonding.Xylanse degraded some xylan and dissolved small bit of lignin.Compared with other xylan,the viscosity of the pulp increased after the treatment of T lanuginosus,and the amount of the xylan decreased.
     KMnO_4 charge was 0.6%in TCF(O-X-Mn-P) bleaching of Leizhou E.urophylla×grandis KP-AQ. The pulp brightness reached 80%and viscosity was more than 800mL/g.Light(superlight) ECF bleaching of KP-AQ had better effect by O-X-A-D_1-Ep-D_2.The pulp brightness reached over 85%at a total chlorine charge of 0.95%,which saved 60%and 40%ClO_2 respectively compared with the O-D_1-E-D_2 and O-D_1-Ep-D_2.
     The study of the effect and mechanism of surfactants in AS-AQ pulping and bleaching showed that the optimum conditions by adding LAS were as follows:12-13%of NaOH(as NaOH),16-18%of Na_2SO_3(as NaOH),0.06-0.1%of AQ,0.2-0.3%of LAS,120-140 min at maximum temperature.Pulp yield,brightness,viscosity and WRV were increased by adding LAS,while benzene-alcohol extractives were decreased.The addition of LAS did not decrease the particle size of anthroquinone in cooking liquor.The concentration of anthroquinone whose diameter is smaller than 0.45μm is 35%lower at room temperature than the cooking liquor without LAS.The amount of anthroquinone increased tremendously by adding LAS,which led to the increasing of sulfite at 100℃and 120℃.
     The best additive in oxygen bleaching was compound surfactants(0.25%LAS and 0.25%AEO-9), which can increase brightness by 3.6%and decrease kappa number and viscosity by 1.3 and 36mL/g respectively.Xylanase activity reached its maximum value and increased by 27%at the presence of 20mg/mL Tween80.NP series was the best additives for peroxide bleaching;the maximum effect was reached with an addition of 0.25%NP-10 and 0.75%NP40 with a 16.1 of HLB value.Pulp brightness increased by 5.1%and the hand sheets had better physical strength properties by adding the additive in the different stages of O-X-Q-P.
     The effects of different strength agents were studied.Grafting copolymer with chitosan was applied in KP-AQ pulping.The results showed that the pulp properties improved more appreciably with the application of CTSAD than CTS,and the amount of CTSAD used was smaller than that of CTS. Microscopic graph showed more compact fiber interweaving after the application of these additives, especially the application of CTSA.The density of the fiber interweaving increased dramatically compared with the control samples.
     The study of the strength enhancing effect of Starch-PAM bi-copolymer,CTSAD tri-copolymer and their mixture showed that the better strength enhancing effect achieved when grafting ratio of starch-PAM was 35.59%.At a dosage of 0.8%and 46oSR of beating degree,the tearing index increased from 4.7mN·m~2/g to 9.5mN·m~2/g,folding endurance enhanced from 229 to 278 times,tensile index rose from 74.70N·m/g to 147.94N·m/g.As for their mixture,tearing index increased by 14.9%,the folding times enhanced by 96.0%;the tensile index improved by 82.7%when the reaction temperature was 40℃,pH8.5,and starch-PAM grafting bi-copolymer to CTSAD grafting tri-copolymer ratio was 5:5,which will be very helpful to the basic and low weight papermaking.
引文
[1]2006年中国造纸行业发展分析及市场预测研究报告[M].
    [2]2007年中国造纸行业分析及投资咨询报告(上中下卷)[M].
    [3]Eric Chao Xu.阔叶木化学机械法制浆[M].中国造纸学会学术报告会论文集,2003,11.
    [4]W.E.希利斯.桉木的性质和抽出物的影响[J].广东造纸,1980.1:38-47;
    [5]安国兴.纸浆漂白新技术[J].国际造纸,2002,21(1):6-11.
    [6]安郁琴,谭水英.桉木KP浆废液治理[J].西北轻工业学院学报,1997(15):65-68.
    [7]安郁琴,于伟东.TCF高白度按木化学浆漂白[J].中国造纸学报增刊,1996(11):24-28.
    [8]蔡明德.应用研究中的制浆技术[J].浙江造纸,2006(3):41-45.
    [9]曹邦威.现代制浆造纸工业的发展趋势[J].2006,22(2):5-8.
    [10]曹邦威.纸浆漂白的最新研究动态[J].制浆造纸,2002(6):5-7.
    [11]曹朴芳.关于中国造纸工业结构调整问题的探讨[J].中华纸业,2000,21(7):6-10.
    [12]曹朴芳.实施林纸一体化工程建设规划,加快造纸工业发展[J].中华纸业,2004,25(7):12-13.
    [13]曹朴芳.中国造纸工业“十一五”发展及展望[M].2007国际造纸技术报告会论文集,2006:1-3.
    [14]曹丽娟,黄剑峰,张光华.壳聚糖和丙烯酰胺接枝共聚及其作为造纸助剂的研究[J].造纸化学品,2000(1):27.
    [15]柴欣生,付时雨,候庆喜,詹怀宁.葸醌在硫酸盐制浆中的溶解特性及对蒸煮的影响[J].中国造纸学报,2004(02).
    [16]陈长武,康振华.几种制浆方法评价的介绍[J].天津造纸,1995(2):21-25.
    [17]陈方,陈嘉翔.桉木化机浆性能的改善[J].中国造纸学报,1995(10):8-13.
    [18]陈洪伟.沙棘、柠条、红柳制浆性能的研究[M].北京林业大学硕士学位论文,2004.
    [19]陈嘉川,杨桂花,李昭成.G6-2细菌木聚糖酶漂白NaOH-AQ麦草浆的研究[J].中国造纸学报,2000(15):43-48.
    [20]陈嘉川,杨桂花,李昭成.KMnO_4用于麦草TCF漂白的研究[J].中国造纸学报,1999(14):51-55.
    [21]陈嘉翔,詹怀宇,余家鸾等.现代制浆漂白技术与原理[M].广州:华南理工大学出版社,2000.
    [22]陈嘉翔主编.制浆原理与工程[M].北京:中国轻工业出版社,2001.
    [23]陈奇志.造纸原料林基地建设[J].国际造纸,2000,19(3):6-13.
    [24]迟聪聪,张曾,黄干强.用镁碱代替钠碱的高得率浆过氧化氢漂白[J].中国造纸,2006,25(10):47-50.
    [25]戴忠国,张美云,杨燕.淀粉衍生物在造纸工业中的应用回顾[J].西南造纸,2003,(3):15.
    [26]董庆年.红外光谱法[M].北京石油出版社,1977.
    [27]范景阳编译.不断壮大的桉木浆生产商——Aracruz公司[J].国际造纸,2004,23(2):55-56.
    [28]方敏燕.岳纸内强科技创新,外重合作交流[J].中华纸业,2004,25(4):68.
    [29]房桂干,谢国恩,李萍等.短周期工业材制高得率浆有关材性及制漂白化机浆适应性综合评估方法的研究[J].林产化学与工业,1995,15(增刊):1-7.
    [30]甘家齐.开发利用按树制浆造纸加快彬氏一体化进展的探讨[J].西南造纸,2006,35(1):4-8.
    [31]高洪霞,黄显南.造纸用增干强剂及其新发展[J].纸和造纸,2006,25(6):38-42.
    [32]耿予欢.H_2O_2漂白中Na_2SiO_3取代剂的研究[J].北方造纸,1996(2):20-27.
    [33]古碧.造纸工业用变性淀粉[J].造纸化学品,1996(2):16-22.
    [34]顾民达.美利纸业集团有限责任公司林纸一体化“新世纪战略工程”[J].造纸信息,2000(9):27.
    [35]顾民达.我国纸浆原料林基地建设现状与发展对策(续)[J].中华纸业,2004,25(3):20-23.
    [36]顾民达.我国纸浆原料林基地建设现状与发展对策[J].中华纸业,2004,25(2):20-23.
    [37]广西贺纸有限责任公司.高白度桉木浆开发与生产[J].国际造纸,2000,19(5):51-52.
    [38]郭勇为.PRC-APMP生产线的工艺及装备特点[J].中国造纸,2005,24(3):27-29.
    [39]国家发展和改革委员会.全国林纸一体化工程建设“十五”及2010年专项规划[J].中华纸业,2004,25(3):6-13.
    [40]国家发展和改革委员会.造纸工业“十五”规划[M].2001.
    [41]和世宝,冯改灵.Na_2SiO_3在制浆造纸工业中的应用[J].黑龙江造纸,2003(3):31-32;
    [42]贺燕丽.贯彻落实林纸一体化规划,努力推动林纸一体化发展[J].中华纸业,2004,25(7):6-10.
    [43]侯彦召,卢宝荣.造纸“九五”攻关项目—“桉木制化机浆工艺及设备的研究”和“桉木化机浆配抄优质印刷纸技术的研究”通过验收及鉴定[J].中国造纸,2001(1):27.
    [44]胡惠仁,赵建,方碧波等.桉小RDH硫酸盐浆利常规硫酸盐浆的ECF和TCF漂白[J].中国造纸学报,2000,15(增刊):39-46.
    [45]胡惠仁等.阴离子聚丙烯酰胺提高纸张干强度的研究[J].中国造纸,1999(1).
    [46]胡宗渊.实施林纸一体化,加快建设造纸速生丰产林基地,走循环经济道路,为实现现代造纸工业而努力[J].造纸信息,2005(10):5.
    [47]黄干强,刘加垒,张曾等.改善KP浆二氧化氯漂白性能的研究,第二部分:采用缓和酸处理改善桉木KP浆漂白性能[J].中国造纸,2000(5):6-9.
    [48]黄干强等.CTMP中试样设备磨浆的实践[J].广东造纸,1997(1):37-40.
    [49]姬振豫.正交设计的方法与理论[M].世界科技出版社,2001,12.
    [50]吉兴香,陈嘉川,杨桂花.蒸煮助剂在化学制浆中的应用与发展趋势[J].纸利造纸,2005,11(6):25-27.
    [51]加快林纸一体化以缓解浆纸依赖进口局面.中国纸业网、2003.12.
    [52]碱性过氧化物机械浆(APMP)与漂白化学热磨机械浆(BCTMP)生产方法介绍[M].1991年学术年会论文及报告汇编.
    [53]江启沛,张晓勇,莫海涛,李佐虎.麦草碱性亚硫酸钾制浆工艺研究[J].中华纸业,2006,27(8):48.
    [54]焦学瞬.造纸制浆和废纸脱墨用表面活性剂[J].日用化学品科学,2002,25(6):27-30.
    [55]金永灿,陆晓坤,夏海霞.表面活性剂Tween 80对麦草浆次氯酸盐漂白的影响[J].纤维素科学与技术,2006,14(4):37-40.
    [56]邝仕均.新建的乌拉圭Botnia-Orion浆厂[J].国际造纸,2008,27(1):55-57.
    [57]劳嘉葆,张勇.麦草(NH_4)_2 SO_3—MgO制浆及加用表面活性剂的研究[J].中国造纸,第三期1991.6.
    [58]劳嘉葆.桉木硫酸盐浆用过酸漂白[J].造纸化学品,2004,(1):41-42.
    [59]劳嘉葆.桉木用木素降解霉菌的生物制浆.造纸化学品[J],2003(3):39-42.
    [60]劳嘉葆.阔叶木的P-RC法制浆[J].黑龙江造纸,2003(2):31-32.
    [61]李春艳,穆银华.亚硫酸钠在制浆生产实践中的应用[J].造纸化学品,2001(6):28.
    [62]李光日,付时雨,余惠生.硫酸盐苇浆残余木素生物降解前后结构特征的对比研究[J].纤维素科学与技术.2000,8(4):32-28.
    [63]李建民,马涛,张敬芳,刘纪营.表面活性剂在棉短绒制浆中的应用[J].造纸化学品,1993,5(2):26-27.
    [64]李静,陈昌华,苏茂尧.桉木APMP制浆过程浆中残余木素分子量的变化[J].纤维素科学与技术,1998,6(2):57-60.
    [65]李里特,朱运平,江正强等.极耐高温木聚糖酶的Eudragit S-100固定化及其对不同纸浆的助漂作用[J].中国造纸,2005,24(7):1-5.
    [66]李文俊,杨玲.表面活性剂在桑枝蒸煮中的应用[J].西南造纸,2002(5):18-20.
    [67]李秀婷,李里特,江正强等.耐热木聚糖酶助漂针叶木硫酸盐浆的研究[J].北京工商大学学报(自然科学版),2005,3(6):1-5.
    [68]李贤惠,钱学仁.纸浆中的羧基及其对造纸过程和纸张性能的影响[J].中国造纸,200827(7):51-57.
    [69]李元禄.无污染全无氯漂白(TCF)[J].中国造纸,1997(5):42.
    [70]李忠正,姚光裕,张大同.意大利杨木制浆性能的研究—碱性亚硫酸钠-蒽醌法[J].南京林学院学报,1984(1):9.
    [71]李宗全,傅英娟,邵志勇等.麦草Soda-AQ浆高锰酸钾脱木素及其纸浆可漂性的研究[J].中国造纸学报,2002,17(1):32-35.
    [72]梁川.2004年加拿大浆纸产量略有下降[J].造纸信息,2005(4):28.
    [73]梁实梅,张静娴,张松寿等.制浆技术问答(第二版)[M].中国轻工出版社,2004,5.
    [74]林风鸣.中国2010年的木材和主要林产品的供需预测和贸易发展趋势[J].林业科技通讯.1999,6:7.
    [75]林鹿.制浆漂白生物技术[M].北京:中国轻工业出版社,2001:211-212.
    [76]林文耀.我国制浆工艺技术的发展趋势[J]_国际造纸,2004(3):47.
    [77]林卓等.桉木浆中残余多酚化合物与木素及糖之间的联结[J].广东造纸,1984(2):22-29.
    [78]刘程,张万福,陈长明.表面活性剂应用手册[M].北京:化学工业出版社.1995.
    [79]刘焕彬.发展生态造纸工业的几点思考[J].中华纸业,2006(3):14-16.
    [80]刘丽媛,慈元钊.分散蒽醌在碱法蒸煮中的应用[J].中华纸业,2001,22(10):47-48.
    [81]刘秋娟,卢西恩.露西亚,柴欣生等.制浆工艺对高得率浆KP浆羧基含量的影响[J].中国造纸,2004,23(8):1-5.
    [82]刘成金,黎厚斌,柯贤文,等.壳聚糖类造纸助剂的作用原理及应用进展[J],2006,18(2):34-37.
    [83]刘士亮.化学浆若干漂白新技术及其在国内的应用前景[J].湖北造纸,2007(2):6-8.
    [84]刘书钗.制浆造纸分析与检测[M].北京:化学工业出版社,2004.
    [85]刘苇编译.壳聚糖对红麻纸张表面性能的影响[J].造纸化学品,2008,20(4):53-56.
    [86]刘学思,陈哲庆,赵涛等编译.澳大利亚的Penola浆厂[J].国际造纸,2008,27(1):63-67.
    [87]隆言泉,石淑兰等.荻在硫酸盐法和亚硫酸盐法蒸煮中的反应历程的比较[J].津轻工工业学院造纸科技研究室.
    [88]卢谦和主编.造纸原理与工程[M].北京:中国轻工业出版社,2004.
    [89]罗琪,陈嘉翔,余家鸾.桉木碱性过氧化氢机械浆的研究[J].广东造纸,1996(3):10-12.
    [90]罗珙.桉木碱性过氧化氢机械法制浆及其机理的研究.华南理[大学硕士论文[D].1993.
    [91]马忻译.阔叶木化学机械法制浆.中国造纸学会学术报告回论文集[M],2003(11):6-15.
    [92]马勇生,邱化玉.壳聚糖类造纸化学品的应用现状及研究进展[J].中国造纸,2004 23(8):51-55.
    [93]马勇生,邱化玉,乇建波等.壳聚糖-AM-DMC三元接枝共聚物对纸浆的增强效果[J]冲国造纸,2008 27(2):29-33.
    [94]毛吏,开发品种,增加效益.提高竞争能力新世纪印刷纸生产的发展趋向[J].造纸信息,2000(5):12.
    [95]苗庆显,秦梦华编译.纤维素保护剂Mg(OH)_2在化学制浆漂白中的应用[J].国际造纸.2004,23(4):53-56.
    [96]欧义芳,李忠正.桉木抽出物的主要化学组成及结构类型的初步研究[J].南京林业大学学报,1996,20(3):1.
    [97]欧义芳.桉树抽出物在硫酸盐法制浆过程中的作用机理[J].纤维素科学与技术,1998,6(3):38-43.
    [98]彭建军泽.阔叶小BCTMP——提高松厚度、平滑度和不透明度[J].国际造纸,2003,22(6):1-3.
    [99]彭毓秀,李忠正.桉木化学浆造纸性能的研究[J].中国造纸,1995(5):35-40.
    [100]祁述雄.中国桉树[M].中国林业出版社,2002,8.
    [101]任维羡,李鸿斌.桉木SCMP浆CH_3COOOH和H_2O_2漂白[J].中国造纸,1997(7):18-22.
    [102]沙克菊编译.化学浆漂白未来的前景[J].国际造纸,2007,26(4):1-4.
    [103]沈家玮,李涛,杜文方,胡书健.兰桉制浆性能的研究[J].云南工业大学学报,1995,3.
    [104]沈一丁,李刚辉.两性AN/AM/DMC/AA共聚物乳液制各及其对纸张的增强作用[J].中国造纸,2003,22(9):23.
    [105]宋士奎.落实林纸一体化规划,促进林业建设发展[J].中华纸业,2004,25(7):10-11.
    [106]孙来鸿,侯彦召.蓝桉APMP制浆及应用技术的现状与展望[J].中国造纸,2002(6):59-62.
    [107]孙来鸿译.山东泉林纸业集团新建APMP化机浆生产线和涂布纸机[J].造纸信息,2001(6):16.
    [108]孙秋菊.生物制浆:工程放大和经济评估[J].国际造纸,2003,22(4):29-31.
    [109]孙显慧.木聚糖酶用于纸浆漂白的研究[J1.湖北造纸,2004(4):11-14.
    [110]市场信息.2007年我国造纸工业概况[J].造纸化学品,2008,20(4):75.
    [111]石淑兰,何福望等.制浆造纸分析与检测[M].北京:中国轻工业出版社,2003.
    [112]唐珲军,安显慧,于钢.绿氧在碱法阔叶木蒸煮中应用的初步探讨[J].造纸化学品,2005(6):26-28.
    [113]唐秋,蒲俊文,姚胜,李琪.四种速生杨术制浆及漂白性能的研究[J].造纸科学与技术,2006,25(2):1-4.
    [114]陶劲松,陈港,刘松坡,武书彬,唐爱民.改性壳聚糖对纸张性能影响的初步研究[J].造纸科学与技术,2001,20(4):16-17.
    [115]童阿国.淀粉聚丙烯酰胺接枝共聚物在造纸中的应用[J].纸利造纸,2000,11(6):48.
    [116]万金娥,熊亦净.速生树碱性哑钠法制浆的研究[J].江两教育学院学报(白然科学),2001,12,22(6):41-43.
    [117]万金娥,熊亦净.速生树碱性亚钠法制浆的研究[J].江西教育学院学报,自然科学版,2001,22(6):41.
    [118]王恩碧.变性淀粉和聚丙烯酚胺在造纸工业上的应用[J].江苏造纸,1998(4):26-30.
    [119]王海毅,龙柱,谢来苏.不同纸浆羧基含量的测定[J].中国造纸2001(5):26-28.
    [120]王宏斌,蒲俊文,谢益民等.三倍体毛白杨AS-AQ法制浆技术研究[J].北京林业大学学报,2004,26(1):83-86.
    [121]王丽娟,牛梅红,杨汝男.速生阔叶木APMP制浆及制浆新工艺P-RC[J].两南造纸,2003,32(4):37-39.
    [122]王琳,刘书钗.淀粉与窄分子量聚丙烯酰胺接枝制备增干强剂的研究[J].湖北造纸,2005(4):24-26.
    [123]王尚义编著.最新印刷纸实用知识手册[M].印刷工业出版社,1993.
    [124]王少光,陈嘉川等.NaOH-AQ麦草浆二氧化氯漂白工艺的研究[J].中国造纸,2004(5):5-10.
    [125]王伟,陈嘉翔,高培基.桉木、蔗渣KP浆生物漂白的研究[J].中国造纸学报,1995(10):22-25.
    [126]王锡元.在我国造纸工业现代化进程中改造发展中国造纸机械制造业[J].中华纸业,1999,5.
    [127]王习文,李兵云,詹怀宇.非木材纸浆ECF漂白的研究[J].造纸科学与技术,2003(1):18-20.
    [128]王习文,詹怀宇,何为,李兵云,徐莉莉.表面活性剂强化的氧脱木素的研究[J].中国造纸学报,2003,18(2):43-46.
    [129]王香爱.阳离子淀粉的生产与应用[J].应用化工,2006,35(6):461-463.
    [130]王晓敏,杨汝男,李立等.麦草AS-AQ法浆亚硫酸化度的影响[J].大连轻工业学院学报,1996,18(2):102-106.
    [131]王杏春.开发桉树制浆造纸[M].中国造纸学会第十届学术年会论文集,2001:127-133.
    [132]为桉树申辩——谈谈桉树的生态功能[J].云南信息港[M].
    [133]韦素萍,黄义寿.桉木NaOH-AQ法与低硫化度硫酸盐法蒸煮的探讨[J].造纸科学与技术,2003,22(5):54-56.
    [134]吴宁,姚春丽,夏耀玲等.尾巨桉KP-AQ制浆及漂白特性的研究[J].中国造纸,2007,26(3):4-6.
    [135]吴淑芳,尤纪雪,李忠正.木聚糖酶对马尾松KP浆漂白机理的探索[J].维素科学与技术,2000,8(3):43-51.
    [136]吴淑芳.碱法麦草浆木聚糖酶处理后木质素和碳水化合物的变化[J].纤维素科学与技术,2002,10(2):43-46.
    [137]吴星娥,周景辉.纸张干强剂的研究[J].西南造纸,2003(2):36.
    [138]武书彬.工业木素的特性及其化学改性[J].纸和造纸,1996,5(2):49-51.
    [139]谢澄,陈中豪.磨浆对兰桉APMP浆特性的影响[J].广东造纸,2000(3):14-16.
    [140]谢澄,陈中豪,陈昌华等.两种桉木APMP制浆及其磨浆过程的研究[J].中国造纸学报,2000(1 5):27-32.
    [141]谢澄等.浅谈桉木APMP制浆工艺[J].广东造纸,1999,5(6):51-53.
    [142]谢益民,伍红,赖燕明等.APMP法制浆过程中桉木的化学成分的变化[J].广州造纸,1997.No.5-6:11-15.
    [143]谢益民,伍红,赖燕明.桉木的化学组成及材性对KP法制浆特性的影响[J].中国造纸, 1998(5):7-11.
    [144]徐清华,候世珍,安郁琴.尾叶桉改良硫酸盐浆臭氧漂白预处理及保护剂的研究[J].黑龙江造纸,2002(2):5-6.
    [145]徐兆瑜.阳离子淀粉与醚化剂开发前景广阔[J].造纸化学品,2002(1):14-18.
    [146]许文璋.发展我国尾叶桉制浆造纸的儿点看法[J].国际造纸,1995,14(4):14-20.
    [147]许勇翔,莫志芳.壳聚糖及其衍生物在造纸lIL业上的应用[J].湖北造纸,2001(2):13.
    [148]薛崇昀,李玉华.桉木纤维特性及化学成分的研究[C].中国桉树种植与制浆造纸研讨会论文集.2005:166-172.
    [149]杨蕾,姚春丽.不同立地条什对欧美杨107材性及ASAM制浆性能的研究[J].造纸科学与技术,2 007,26(3):8-12.
    [150]杨蕾.年产10万吨杨木APMP制浆车间设计.北京林业大学学士学位论文[D],2004.
    [151]杨懋暹.发展林纸一体化 突破木浆“瓶颈”之我见[J].中华纸业,2004,25(10):8-12.
    [152]杨淑蕙.植物纤维化学[M].中国轻工业出版社,2001:177.
    [153]姚春丽,蒲俊文.三倍体毛白杨化学组分纤维形态及制浆性能的研究[J].北京林业大学学报,1998,20(5):18-21.
    [154]姚春丽,吴宁,夏耀玲,陈瑶,杨玢.尾巨桉和尾赤桉KP-AQ制浆性能对比[J].纸利造纸,2007,5,26(3):21-24.
    [155]姚春丽,吴宁等.尾巨桉和尾赤桉KP-AQ制浆性能对比[J].2007,26(3):21-24.
    [156]姚光裕.澳大利亚桉木制浆造纸的技术进展[J].造纸信息,2003(12):29.
    [157]姚光裕.金合欢木碱性过氧化物机械浆的性质及其造纸应用潜力[J].纸和造纸,2003(1):35-37.
    [158]姚献平,郑丽萍.表面活性剂在造纸工业中的应用现状与发展建议[J].日用化学品科学,2002,25(5):29.
    [159]姚献平,郑丽萍.淀粉衍生物及其在造纸中的应州技术[M].北京:中国轻工业出版社,1999.
    [160]游贤德.国内过氧化氢用丁纸浆漂白研究进展[J].化学推进剂与高分子材料,2000(3):6-8.
    [161]余家鸾.桉木制浆方法及其纸浆特性的比较[J].广东造纸,1993(1):9-14.
    [162]詹怀宁,李建军,黄方.桉术硫酸盐浆术聚糖酶辅助漂白生产试验[J].造纸科学与技术,2001,20(2):1-2.
    [163]詹怀宇,李建军,黄方等.桉木硫酸盐浆木聚糖酶辅助漂白生产试验[J].造纸科学与技术,2001,20(2):1-7.
    [164]詹怀宇等.Study on the LMS Biobleachirg ofEucalyptus Kraft Pulps[J].华南理工大学学报2000,28(12):5-11.
    [165]张光华,杨建洲.造纸工业中表面活性剂的应用现状与发展[J].精细化工,2001,18(4):193.
    [166]张光华。表面活性剂在树脂控制中的应用[J].西南造纸,2000(3):17-18.
    [167]张洪涛,李友明等.表面活性剂在蒸煮中的应刚[J].纸利造纸,2001,1(1):39-40.
    [168]张家喜,薛国新,周小芳.改性蒽醌的制备及其在碱法蒸煮中的应用[J].中华纸业,2003,24(3):30-32.
    [169]张菊先,郭勇为.几种典型造纸速生材的纤维特性及其用途[J].湖南造纸,2003(2): 27-31.
    [170]张乃钧.桉木半化学浆配抄箱纸板研究[J].天津轻工业学院学报,1995(2):28-32.
    [171]张伟广,刘亮.十二烷基苯磺酸钠在木片浆蒸煮中的应用[J].黑龙江造纸,2006(1):46.
    [172]张学铭,张运展.己烯糖醛酸在纸浆中的存在及其影响[J].中国造纸,2005,24(4):45-49.
    [173]张学谦.碱性过氧化氢机械浆(APMP)简介[J].纸和造纸,1991(1):38.
    [174]张岳,北京林业大学硕士学位论文[D],2006.
    [175]张运展,于俊杰,张鹏,穆红英.碱性和中性亚硫酸盐法制浆废液作水泥减水剂的研究[J].2004,19(2):81.
    [176]张志芬,刘世海,聂勋载.APSP超短期黑杨小径材化机浆的研制[J].中华纸业,2005,26(2):37-38.
    [177]赵建,李雪,康从宝等.桉木RDH硫酸盐法制浆性能的研究[J].中国造纸学报,2002,17(1):14-21.
    [178]赵建,李雪芝,曲音波等.助剂改善的桉木硫酸盐浆的H202漂白[J].西南造纸,2000(6):5-7.
    [179]赵建,李雪芝,石淑兰等.桉木常规KP浆和RDH浆的氧脱木素研究(Ⅱ)——预处理和强化[4].对常规KP浆氧脱木素的改善效果[J].中国造纸学报,2003,18(2).
    [180]赵建,李雪芝,石淑兰等.蓝按硫酸盐法制浆和漂白性能研究[J].中国造纸,2003,22(6):1-4.
    [181]赵建,李雪芝,石淑兰等.柠檬桉、尾叶桉、柳桉制浆性能研究[J].中国造纸,2003,22(11):8-10.
    [182]赵建,石淑兰,胡惠仁.杨木与桉木KP浆的无元素氯漂白[J].中国造纸,1997(5):30-34.
    [183]赵建,石淑兰,胡惠仁等.铝酸盐对按木KP浆H_2O_2漂白的改善效果[J]_中国造纸,2001(1):18-21.
    [184]赵荣军.桉树人工林木材居室环境学特性及木材性质与加工工艺对胶合板质量影响的研究[D].中国林业科学研究院博士后研究报告,2002.
    [185]赵宇,陈中豪,李友明桉木硫酸盐浆木聚糖酶漂白的研究[J].黑龙江造纸,2006(1):26-30.
    [186]郑丽萍,姚献平.纸用变性淀粉的新发展[J].国际造纸,1999,18(4):5-7.
    [187]中国造纸协会,中国制浆造纸研究所编,1999年中国造纸年鉴[M].中国制浆造纸研究院,1999:108.
    [188]中国造纸协会,中国制浆造纸研究所编.中国纸业大全(2003-2004)[M].中国轻工出版社,2004.
    [189]中国纸业网,《加快林纸一体化以缓解浆纸依赖进口局面》[J].2003,12.
    [190]周学飞,陈嘉翔,余家莺.鳌合剂与木聚糖酶预处理对桉木KP浆含氧漂白的影响[J].中国造纸学报,1997,(12):53-56.
    [191]周学飞,陈嘉翔.桉木硫酸盐浆木聚糖酶预处理及其对H_2O_2漂白影响的研究[J].中华纸业,1998(4):23-26.
    [192]周学飞,余家鸾,陈嘉翔.桉木碱性亚钠一葸醌制浆工艺及其机理研究[J].广东造纸,1992(3):7-10.
    [193]周学飞.桉木碱性亚硫酸钠—蒽醌法制浆及其机理[J].中国造纸学报,2003,18(2):24-26.
    [194]周学飞.硫酸盐浆小聚糖酶—过氧化氢生物漂白研究[J].西南造纸,2003,32(5):23-25.
    [195]朱勇强..纸页增强的机理与增强剂[J].上海造纸,2004,35(4):40-46.
    [196]Stig Andtbacka,Hakan Dahhof,张孝军,桉小制浆新技术,国际造纸,2004.23(4):49-52
    [197]Arias M Enriqueta,etc.Kraft pulp biobleaching and mediated oxidation of a nonphenolic substrate by laccase from Streptomyces cyaneus CECT 3335[J].Applied and Environmental Microbiology,2003,69(4):1953-1958.
    [198]Bajpai,Bhardwaj.Use of xylanase in bleaching of eucalypt kraft pulp[J].Appita,1993,46(4):274-276.
    [199]Barzky D,Page D H,Ragauskas A.Carboxylic acid groups and fiber bonding[C]//Fundamental of papemaking Materials,Transactions of the Fundamental Research Symposium 11~(th),1997.
    [200]Beq Qasim Khalil,etc.Enhanced production of a thermostable xylanase from Streptomyces sp.QG-11-3 and its application in biobleaching of eucalyptus kraft pulp[J].Enzyme and Microbial Technology,2000,27(7):459-466.
    [201]Binotto A P,Nicholls G A.Tappi,1977,60(6):91.
    [202]Bourbonnais R,Leech D,Paice M G.Electrochemical Analysis of the Interactions of Laccase Mediators with Lignin Model Compunds[J].Biochim Biophus Acta,1998,1379(3):381-390.
    [203]Bourbonnais R,Paice M G,Demethylation and delignification of kraft pulp by Trametaes versicolor laccase in the presence of 2,2'-azino-bis-(3-ethulbenzthiazoline-6-sulphonate)[J].Appl Microbiol Biotechnol,1992,36:823-827.
    [204]C.A.Raymond and L.R.SchimLeck,Development of near infrared reflectance analysis calibrations for estimating genetic parameters for cellulose content in Eucalyptus globules,NRC.Canada,2002.32:170-176.
    [205]Call H.P and Mucke I.State of the art of enzyme bleaching and disclosure of a breakthrough process[C].Proceedings International Non-Chlorine Bleaching Conference,Amelia Island,Florida,1994:117-123
    [206]Call H.P.1987,EP 327 576.
    [207]Call H.P.1990,DE 40 08 893.
    [208]Call.H.P.1992,WO 92/20857.
    [209]Chavonda J Jacobs.Effect of enzyme pretreatments on conventional kraft pulping[J].Tappi Journal,1998,81(2):143.
    [210]Chen,T,Z.Wang,Y.Zhou,C.Breuii,O.K.Aschim,E.Yee,and L.Nadeau.1995.Using solid-phase extraction to assess why aspen causes more pitch problems than softwoods in Kraft pulping[J].TAPPI(Tech.Assoc.Pulp Pap.Ind.)J.78:143.
    [211]Chirat C,Lachenal D,Angelier R,et all.(DZ) and(ZD) bleaching:fun damentais and application[C]11996 Inter1 Pulp Bleaching Conference,Washington:197.
    [212]Daniel A I,Evtaguin D V,Silvestre A J D,et al.Chemical Features of Hardwood unbleached kraft pulps and their ECF bleached[J].lity JJPPS,2004,30(4):94.
    [213]Detlev Glittenberg,Starch alternatives for improved strength,retention,and sizing.Tappi,76(11):215-219.
    [214]Dhillon Ashita,etc.Cellulase-poor thermostable alkalitolerant xylanase produced by Bacillus circulans AB 16 grown on ricestraw and its application in biobleaching of eucalyptus pulp[J].Bioresource Technology,2000,73(3):273-277.
    [215] E. Ratnieks, J.W. Ventura, M.R. Mensch, R.A.Zanchin, Acid stage improves production in Eucalyptus fibre line, Pulp and Paper Canada, 2001.12: 93-96.
    [216] E.C Xu, Chemical treatment in mechanical pulping, Part 2:North American aspen, Pulp and Paper Canada, 1999.2: 40-45.
    [217] E.C Xu, Chemical treatment in mechanical pulping, Part 3:South American Eucalyptus, Pulp and Paper Canada, 1999.2: 40-45.
    [218] E.C Xu, P-RC alkaline peroxide mechanical pulping of hardwood, Part 1:aspen, beech, birch, cottonwood and maple, Pulp and Paper Canada, 2001.2: 44-47.
    [219] Eric C. Xu and Marc J. Sabourin, Evaluation of APMP and BCTMP for market pulps from South American Eucalyptus, Tappi,1999, 82(12): 75-82.
    [220] Favis B D, Choi PMK, Adler P M, et al. The leaching of lignin from unbleached kraft fibres suspended in water[J]. Pulp and paper science, 1981,1 (2): 35-40.
    [221] G.Garrote, M.E.Eugenio, M.J.Diaz, J.Ariza, F.Lopez, Hydrothermal and pulp processing of Eucalyptus, Bioresource Technology, 2003(88): 61-68.
    [222] Hans U, Sulse, Chreeson Moodley. Progress in bleaching to top brightensswith low reservision[J]. TAPPSA Journal, 2005 (3): 89.
    
    [223] Higgins H G, Deyong J, Balodis V et al. Tappi, 1973, 56(8): 127.
    [224] Ibarra David, etc. Integrating laccase - Mediator treatment into an industrial-type sequence for totally chlorine-free bleaching of eucalypt kraft pulp[J]. Journal of Chemical Technology and Biotechnology, 2006,81 (7): 1159-1165.
    [225] Isam Y. Qudsieh, et al. Preparation and characterization of poly (methylm ethacrylate)grafted sag starch using potassium persulfates as redax initiator[J]. Applied polym erscience, 2004, 94(5):1891-1897.
    [226] Ingruber, O,.V.et.al. 1982,Alkaline Sulphite -Anthraquinone pulping of Eastern Canadian Woods[J]. Pulp&Paper Canada 83(12): 79-88.
    [227] Isabel Miranda, Helena Pereira, The Variation of Chemical Composition and Pulping Yield With Age and Growth Factors in Young Eucalyptus Globulus, Wood and Fiber Science, 2002. 34(1): 140-145.
    [228] Isam Y. Qudsieh, et al. Preparation and characterization of poly (methylm ethacrylate)grafted sago starch using potassium persulfates as redax initiator[J].
    [229] J·M·Dinwoodie , Tappi, J, 1965(8): 440-450.
    [230] James.d, A·clark. Tappi, J, 45 1962, 8: 154A-157A.
    [231] Jiang JE. Extended modified cooking of southern pine with polysulfide :effects on pulp yield and physical properties[J]. Tappi Journal, 1994, 77(2): 120.
    [232] Justin Toland, Old Name Dominat, PPI, 2003. 45(9): 25-34.
    [233] Kaiser M, Pitre R. Beloit's (RDH) displacement heating at Owens-Illinois, Valdosta, Georgia[J]. Tappi, 1986,69: 45-48.
    [234] Kocurek M J, Stevens ed. CFB. Pulp and Paper Manufacture(ED3). Properties of fibrous raw materials and their preperation for pulping. Published by the Joint Textbook Committee of the Paper Industry, 1983, 1.
    [235] Koljonen K, Mustranta A, Stenius P. Surface characterization of mechanical pulps by Polyelecteolyte adsorption[J]. Nordic Pulp and Paper,2004,19(4):495.
    [236] Korpela A. Improving the strength of PGW Pine pulp by alkaline peroxide treatment [J]. Nordic Pulp and Paper Reseach Jounal, 2002, 17(2): 183
    [237] Laurel E Falk. The effect of anthraquinone and anthrahydroquione penetration on delignification in the soda pulping of noway spruce[J]. wood Chem.&Technol, 1992, 5(3): 97.
    [238] Leclerc D F, Hogikyan R M. Rapid determination of effective alkali and dead-load concentrations in kraft liquors by attenuated total reflectance infrared spectroscopy[J]. J Pulp Paper Sci, 1995,21:231-237.
    [239] Mera F, Chamberlin J. Extended delignification, an alternative to conventional kraft pulping[J]. Tappi J, 1988, 71: 132-136.
    [240] Moreira etc. Biobleaching of oxygen delignified kraft pulp by several white rot fungal strains[J]. Journal of Biotechnology, 1997, 53 (2/3 ): 237-251.
    [241] Paice M G, Gurnagul N, Page D H, et al. Mechanism of hemicellulose directed prebleaching of kraft pulps[J]. Enzyme microbial technology, 1992(14): 272-276.
    [242] Patrick C, Biotechnology in the pulp and paper industry:a review part 1:tree improvement pulping and bleaching and dissolving pulp applications.Troter[J]. Tappi J, 1990, 73(4): 198-204.
    [243] Pearson A J. An unified theory of refining, Published by the Joint Textbook Committee of the Paper Industry, 1990:44.
    [244] Pranee Lertsutthiwong, Suwalee Chandrkrachang, MousaM.Nazhad and WillemF.Stevens. Chitosanasa dry strength agent for paper. Appita Journal, 55(3): 2002.
    [245] Pratinea Bajpai, Parmod Bajpai. Time for Enzymes in Pulp Bleaching in paper[J]. International Paper, 1999, 3(4 ): 17.
    
    [246] R·S·Seth, D·H·page, Tappi, J, 71 1988.2: 103-107.
    [247] Shen Q, Rosenholm J B. Kraft black liquors properties in relation to delignification[J]. Nordic Pulp Paper Res J, 1998, 13(3): 40-44.
    [248] Stenius,P. Chapter 2:Basic chemistry of wood delignification. In frost products chemistry [J] .Tappi Press: Atlanta, 2000, 61-72.
    
    [249] Stig Andtbacka,Hakan Dahhof, 张孝军,桉木制浆新技术,国际造纸, 2004, 23(4): 49-52.
    [250] Tichy T,Wong A.Sulphite Pulping of Aloizia Falcate fromEast Kalimantan[C]. Tropical Pulp Conferences, Jakarts, 1991, 2: 328-348.
    [251] Tormund D, Teder A. New findings on sulfide chemistry in kraft pulping liquors[J]. Tappi J, 1989,72:205-210.
    [252] Turner J. C Howard J. C Howard J. C . Bleaching with enzyme instead of chlorine-mill trails Tappi J, 1992, 75(12): 83-89.
    [253] V.R.Parthasarathy, Glen C, Smith et al. Application of anthraquinone in extending the delignification of kraft and polysulfide pulp[J]. Tappi Journal, 1995, 78(2): 113.
    [254] Vera Sacon, etc. Improved Technology for Light Bleaching of Eucalyptus Pulp[J]. 2007 国际造纸技术报告会论文集, 2007: 167-178.
    [255] Virkola.N-E,et.al.1981,Neurtral Sulfite AQ Pulping as an Alternative to kraft pulping[J]. Tappi. 64(5): 103-107.
    [256] Xianming Wei and Nuno N.G. Borralho, Genetic gains and levels of relatedness from best linear unbiased prediction selection of Eucalyptus urophylla for pulp production in southeastern China, NRC. Canada, 2000(30): 1601-1607.
    [257] Yang Maoxian. Starting from forest is a major strategy for the sustaining development of paper industry in China[J]. CPPI 2007,1(1 ):12-17.
    [258] Zhang D, Chai X-S,Pu Y, et al. Lignocellulosic fiber charge enhancement by catalytic oxidation during oxygen delignification[J] . Journal of Colloid and Interface Science, 2007, 306(2):248