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辐射松预水解对后续蒸煮及氧脱木素过程木素脱除效果的影响 被引量:4

The Effects of Radiata Pine Prehydrolysis on the Lignin Removal of the Subsequent Kraft Pulping and Oxygen Delignification
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摘要 本文研究了辐射松木片预水解对蒸煮和后续氧脱木素过程的影响。结果表明,预水解温度为168℃,预水解时间在60~90 min时,半纤维素脱除率大于50%,而纤维素的损失率小于10%,且纤维素聚合度不降低;同时也能促进蒸煮过程及后续氧脱木素过程木素的脱除,蒸煮后纸浆卡伯值降低至16.3,氧脱木素后纸浆卡伯值降低至2.8。当预水解时间超过120 min,预水解则会对后续的蒸煮起阻碍作用,造成蒸煮困难,表现在纸浆卡伯值急剧上升,甚至出现生煮现象。预水解时间控制在180 min之内,预水解可以提高氧脱木素过程中木素的脱除率,预水解时间超过180 min,预水解对氧脱木素的影响则不明显。预水解对蒸煮过程的影响大于对氧脱木素过程的影响,尤其是过度预水解对蒸煮有阻碍作用,但是对后续氧脱木素的影响则不显著。 The radiata pine chips was treated by consecutive prehydrolysis, kraft pulping and oxygen delignification and the effects of prehydrolysis time on the lignin removal efficiency of the subsequent kraft pulping and oxygen del- ignification were investigated. The results showed that prehydrolysis within 60 ~ 90 min could not only remove more than 50% hemicellulose without serious cellulose loss and degradation ( cellulose loss was less than 10% ) ; but also promote the subsequent lignin removal efficiency both in kraft pulping and oxygen delignification. Upon the above prehydrolysis conditions, the Kappa number of the prehydrolysis kraft pulp decreased to 16.3 and the final Kappa number of the oxygen delignified pulp lowered to 2.8. Alternatively, extensive prehydrolysis could retard the lignin removal and even cause difficulties in the kraft pulping process, indicating as high Kappa number of the pre- hydrolysis kraft pulp. Although the extensive prehydrolysis had an obvious inhibition effects on the subsequent kraft pulping, the lignin removal was still substantial during the oxygen delignification process; revealing that prehydroly- sis was more critical for kraft pulping than oxygen delignification.
出处 《造纸科学与技术》 2015年第2期1-6,共6页 Paper Science & Technology
基金 国家自然科学基金项目(31270638) 华南理工大学制浆造纸工程国家重点实验室开放基金项目(201403)
关键词 辐射松 预水解 蒸煮 氧脱木素 radiata pine, prehydrolysis, kraft pulping, oxygen delignification
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参考文献20

  • 1Yoon H. Pretreatment of lignocellulosic biomass by autohydrolysis and aqueous ammonia percolation [J]. Korean Journal of Chemical Engineering, 1998, 15(6) : 631 -637.
  • 2Nitsos C K, Matis K A, Triantafyllidis K S. Optimization of hydro- thermal pretreatment of lignocellulosic biomass in the bioethanol pro-duction process [J]. ChemSusChem, 2013, 6( 1 ) : 110 - 122.
  • 3Donohoe B S, Decker S R, Tucker M P, et al. Visualizing lignin coalescence and migration through maize cell walls following thermo- chemical pretreatment [ J ]. Biotechnology and Bioengineering, 2008, 101(5) : 913 -925.
  • 4Selig M J, Viamajala S, Decker S R, et al. Deposition of lignin droplets produced during dilute acid pretreatment of maize stems re- tards enzymatic hydrolysis of cellulose [ J ]. Biotechnology Progress, 2007, 23(6) : 1333 -1339.
  • 5Donohoe B S, Decker S R, Tucker M P, et al. Visualizing lignin coalescence and migration through maize cell walls following thermo- chemical pretreatment [ J]. Biotechnology and Bioengineering, 2005, 101(5) : 913 -925.
  • 6Cao S L, Pu Y Q, Studer M, et al. Chemical transformations of Populus trichocarpa during dilute acid pretreatment [ J ]. RSC ad- vance, 2012, 2: 10925- 10936.
  • 7Leschinsky M, Zuckerstotter G, Weber H K, et al. Effect of auto- hydrolysis of Eucalyptus globulus wood on hgnin structure. Part 2 : Influence of autohydrolysis intensity [ J ]. Holzforschung, 2008, 62 (6) : 653 -658.
  • 8曹石林,马晓娟,林玲,黄六莲,陈礼辉.竹材草酸预水解过程木质素的溶出规律[J].农业工程学报,2014,30(5):277-284. 被引量:6
  • 9Ma X J, Cao S L, Luo X L,et al. Lignin removal and benzene -al- cohol extraction effects on lignin measurements of the hydrothermal pretreated bamboo substrate [ J]. Bioresource Technology, 2014,151 : 244 -248.
  • 10Tasman J E and Berzins V. The permanganate consumption of pulp materials: IV. The Kappa correction coefficient [ J ]. Pulp and Pa- per Canada, 1959, 60:231 -235.

二级参考文献63

  • 1马伟良,臧贻朋.竹材用于生产溶解浆的试验研究[J].合成纤维,2012,41(8):27-30. 被引量:1
  • 2Hiett L A. Dissolving cellulose: its present position and prospects for future development[J]. Tappi J. , 1985, 68(2) : 42.
  • 3Do,an I, Giirtiz G. Dimensionless parameter approach for oxygen del- ignification kinetics [ J ]. Ind. Eng. Chem. Res., 2008, 47 (16) : 5871.
  • 4Pan Xiaofeng, Ma Lefan, Qu Qinqin, et al. The Kinetics of Oxygen Delignification of Reed Kraft Pulp ( I )-Kinetics of Delignification [ J]. Advanced Materials Research, 2011, 236 - 238 : 1420.
  • 5Johansson E, Ljunggren S. The Kinetics of lignin reactions during oxygen bleaching, Part IV: Reactivities of different lignin model compounds and the influence of metal ions on the rate of degradation[ J]. Journal of Wood Chemistry and Technology, 1994, 14(4) : 507.
  • 6Herbert Sixta. Handbook of Pulp[ M]. Weinheim, 2006.
  • 7Paice M G, Bourbonnais R, Reid I D, et al. Oxidative bleaching enzymes: a review[ J ]. Journal of Pulp and Paper Science, 1995, 21 (8) : 280.
  • 8Sixta H,Iakovlev M,Testova L,et al.Actual and futuretrends in dissolving pulp manufacture[C]//The 4th NordicWood Biorefinery Conference,Helsinki,Finland,2012:71-81.
  • 9Garrote G,Dominguez H,Parajó J C.Generation ofxylose solutions from Eucalyptus globulus wood byautohydrolysis-posthydrolysis processes:Posthydrolysiskinetics[J].Bioresource Technology,2001,79(2):155-164.
  • 10Lavarack B P,Griffin G J,Rodmanc D.Measuredkinetics of the acid-catalysed hydrolysis of sugar canebagasse to produce xylose[J].Catalysis Today,2000,63(2/3/4):257-265.

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