期刊文献+

木材亚-超临界流体非等温萃取特性研究 被引量:2

STUDY ON CHARACTERISTICS OF NON-ISOTHERMAL EXTRACTION OF WOOD WITH SUB-AND SUPERCRITICAL FLUID
下载PDF
导出
摘要 在半连续实验装置上 ,运用非等温动态萃取技术 ,进行了木材亚 超临界乙醇 (有或无水 )萃取特性的研究 ,主要考察了压力和水对木材亚 超临界乙醇萃取过程的影响。研究结果表明 ,木材主要萃取过程可分为两个阶段 ,第 1阶段温度范围为 2 0 0℃~ 2 80℃ ,在 2 5 0℃左右萃取物生成速率有极大值 ;第 2阶段温度范围为 2 80℃~ 380℃ ,在 35 0℃左右萃取物生成速率有极大值 ,该阶段同时生成大量气体。提高压力或增加混合溶剂中水的摩尔分数均能使木材转化率和萃取物产率增加 ,气体产率降低。压力效应主要体现在 2 5 0℃以后 ,而水效应主要体现在 30 0℃以前。通过温度、压力和混合溶剂中水的摩尔分数等过程变量的调控 ,亚 The characteristics of sub and supercritical extraction of wood with ethanol or ethanol water were studied in a semi continuous experimental apparatus using the non isothermal dynamic extraction technique,the effects of pressure and water on the sub and supercritical extraction of wood with ethanol were mainly investigated.The results showed that the main extraction process of wood could be classified as two phases roughly,the temperature range in the first phase was from 200℃ to 280℃,and the extract formation rate had the maximum value at about 250℃.The temperature range in the second phase was from 280℃ to 380℃,and the extract formation rate had the maximum value at about 350℃,a great quantity of gas was generated in this phase simultaneously.Wood conversion and extract yield increased and gas yield decreased with the increasing of pressure and the molar fraction of water in ethanol water mixture.The effect of pressure mainly reflected after 250℃,and the effect of water mainly reflected before 300℃.From an engineering standpoint,the sub and supercritical extraction technology could be suited to the different conversion ways of wood resources through regulating and controlling process variables such as temperature,pressure and the molar fraction of water in ethanol water mixture.
作者 钱学仁 李坚
出处 《林业科学》 EI CAS CSCD 北大核心 2002年第4期117-124,共8页 Scientia Silvae Sinicae
基金 国家自然科学基金资助项目 (3 9670 5 91)
关键词 木材 亚临界萃取 超临界萃取 非等温萃取技术 压力 水分 木质素衍生物 Wood, Subcritical extraction, Supercritical extraction, Ethanol, Water
  • 相关文献

参考文献10

  • 1潘学军,谢来苏,隆言泉.麦草Soda-AQ黑液中木素的紫外特性及其定量测定[J].天津造纸,1992,14(4):7-11. 被引量:4
  • 2钱学仁,李坚.超临界流体在林产工业中的应用[J].世界林业研究,1996,9(1):28-34. 被引量:17
  • 3钱学仁 李坚.木材超临界乙醇萃取物的GC-MS分析[J].中国学术期刊文摘,1999,5(8):1058-1060.
  • 4钱学仁,李坚.兴安落叶松木材超临界乙醇萃取研究[J].东北林业大学学报,2000,28(4):21-24. 被引量:16
  • 5钱学仁 李坚.不同树种木材的超临界乙醇萃取液化行为[J].中国学术期刊文摘,2000,6(2):252-253.
  • 6Goto M,Smith J M and McCoy B J.Kinetics and mass transfer for supercritical fluid extraction of wood.Ind.Eng.Chem.Res.,1990,29(2):282~289
  • 7Hicks C P and Young C L.Gas-liquid critical properties of binary mixtures.Chemical Reviews,1975,75(2):139~175
  • 8Ni Y and Van Heinigen A R P.The swelling of pulp fibers derived from the ethanol-based organsolv process.Tappi J.,1997,80(1):211~213
  • 9Poirier M G,Ahmed A,Grandmaison J L et al.Supercritical gas extraction of wood with methanol in a tubular reactor.Ind.Eng.Chem.Res.,1987,26(9):1738~1743
  • 10Reaves J T and Roberts C B.Subcritical solvent effects on a parallel Diels-Alder reaction network.Ind. Eng.Chem.Res.1999,38(3):855~964

二级参考文献2

共引文献31

同被引文献20

  • 1DEMIRBAS A. Biomass resource facilities and biomass conversion processing for fuels and chemicals[ J ]. Energy Conversion and Management,2001, 42 : 1357 - 1378.
  • 2FIERZ H E. Chemistry of wood utilization[J] .Chemistryand Industry Review, 1925,44:942.
  • 3CELEGHINI E A,CELEGHINI D S,RENATA M,et al. Experimental variables and their effects on the liquefaction of cellulose from sugar cane bagasse[J]. Energy Sources,2001,23:93 -99.
  • 4CELEGHINI R M S,LANCAS F M. Optimization of the direct liquefaction of lignin obtained from sugar cane bagasse[J]. Energy Sources,2001,23: 369 -375.
  • 5Peter McKendry.Energy production from biomass (part2):conversion technologies[J].Bioresource Technology,83 (2002):47-54.
  • 6Demirbas A.Biomass resource facilities and biomass conversion processing for fuels and chemicals[J].Energy Conversion and Management,2001,(42):1357-1378.
  • 7Caglar A,Demirbas A.Conversion of cotton cocoon shell to liquid products by supercritical fluid extraction and low pressure pyrolysis in the presence of alkalis[J].Energy Conversion and Management,2001 (42):1095-1104.
  • 8Reaves J T,Toberts C B.Sub-critical solvent effects on a parallel Diels-Alder reaction network[J] Ind.Eng.Chem.Res,1999,38(3):855.
  • 9Jerry W King.Critical fluid technology for the processing of lipid-related natural products[J].C.R.Chimie 2004 (7):647-659.
  • 10Kabyemela B M,Adschiri T.Rapid and selective conversion of glucose to erythrose in supercritical water[J].Ind Eng Chem Res,1997,36:5063-5067.

引证文献2

二级引证文献34

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部