期刊文献+

纤维素热裂解反应机理及中间产物生成过程模拟研究 被引量:20

Simulation of cellulose pyrolysis mechanism and formation process of intermediate products
下载PDF
导出
摘要 基于改进的B-S机理模型,通过求解物料内部和气相空间两段反应过程,对纤维素热裂解过程中一些化合物(活性纤维素、左旋葡聚糖(LG)、乙醇醛、丙酮醇等组分)的生成和演变情况进行了模拟。结果发现,自由水的脱除过程使物料前期升温速率发生了下降,并未影响热解期间温度分布以及反应过程。热裂解过程中,由于一次反应的强烈吸热,物料在长时间内局限于中温范围,其内部各组分质量浓度分布的区别主要体现出一次反应竞争能力的强弱。物料厚度的增加使热裂解时间延长,并加剧物料内部的二次分解。左旋葡聚糖和其竞争产物乙醇醛的生成出现一个大量生成、快速逃逸的过程,相比于左旋葡聚糖,乙醇醛质量浓度的积累具有更快的速度,体现出较高温度下的竞争优势。对于小尺寸反应物,挥发分二次反应主要发生在气相空间,随着气相停留时间的增加,其二次分解的程度提高,该效果随辐射源温度的提高而加剧。相比于LG产率随反应时间的快速下降趋势,高温下生物油产率的降低略显缓和,其变化主要是组分分布的改变,即从大分子结构降解为小分子结构。 Based on the modified Brodio-Shafizadeh mechanism, a two-stage model was proposed to simulate the formation and decomposition of intermemediate products including active cellulose (AC), levoglucosan (LG), hydroxyl-acetaldehyde (HAA), acetol and furfural in the cellulose pyrolysis. Results show that the water evaporation only decreases the heating rate of the pyrolysis prophase, while it has no effects on the temperature distribution and reaction process in the main pyrolysis stage. Cellulose material stays for a long time in the middle temperature due to the endothermic effect of primary cracking. The concentration of LG and other competitive compounds in the fabric structure is primarily determined by its competitive reaction of formation. The rising of material thickness would prolong the decomposition time of cellulose, and enhance the secondary cracking within the fabric structure. The formation process both LG and HAA shows the characteristic of fast formation and rapid escape, but HAA presents a faster accumulating tendency that will be enhanced at high temperature. For small size materials, the secondary reaction of volatile occurs largely in the gaseous phase rather than in the solid phase. The longer residence time of volatile in the high temperature region will induce deep decomposes of LG. Compared with the rapid decrease of LG yield with reaction time, the yield of tar falls slowly at high temperature. The major change exists in the distribution of components, i.e. the large molecule compounds being decomposed into small ones.
出处 《燃料化学学报》 EI CAS CSCD 北大核心 2006年第2期184-190,共7页 Journal of Fuel Chemistry and Technology
基金 国家自然科学基金(50476057) 广东省自然科学基金(003045) 华南理工大学自然科学基金(323-E5040240)
关键词 纤维素 热裂解 机理 模拟 中间产物 cellulose pyrolysis mechanism simulation intermediate product
  • 相关文献

参考文献15

  • 1YAMAN S. Pyrolysis of biomass to produce fuels and chemical feedstocks[J]. Energy Convers Manage, 2004, 45 (5): 651-671.
  • 2LAPPAS A A, SAMOLADA M C, IATRIDIS D K, VOUTETAKIS S S, VASALOS I A. Biomass pyrolysis in a circulating fluid bed reactor for the production of fuels and chemicals[J]. Fuel, 2002, 81 (16): 2087-2095.
  • 3BRIDGEWATER A V, PEACOCKE G V C. Fast pyrolysis processes for biomass[J]. Renewable Sustainable Energy Rev, 2000, 4(1): 1-73.
  • 4LUO Z Y, WANG S R, LIAO Y F, ZHOU J S, GUY L, CEN K F. Research on biomass fast pyrolysis for liquid fuel[J]. Biomass Bioenergy, 2004, 26(5): 455-462.
  • 5LUO Z Y, WANG S R, LIAO Y F, CEN K F. Mechanism study of cellulose rapid pyrolysis[J], Ind Eng Chem Res, 2004, 43(18): 5605-5610.
  • 6LEDE J, BLANCHARD F, BOUTIN O. Radiant flash pyrolysis of cellulose pettets: Products and mechanisms involved in transient and steady state conditions[J]. Fuel, 2002, 81(10): 1269-1279.
  • 7廖艳芬,王树荣,骆仲泱,岑可法.氯化钙催化纤维素热裂解动力学研究[J].燃料化学学报,2005,33(6):692-697. 被引量:24
  • 8廖艳芬,骆仲泱,王树荣,余春江,岑可法.纤维素快速热裂解机理试验研究 Ⅰ.试验研究[J].燃料化学学报,2003,31(2):133-138. 被引量:38
  • 9王树荣,廖艳芬,文丽华,骆仲泱,岑可法.钾盐催化纤维素快速热裂解机理研究[J].燃料化学学报,2004,32(6):694-698. 被引量:31
  • 10BRADBURY A G W, SAKAI Y, SHAFIZADEH F. A kinetic model for pyrolysis of cellulose [J]. J Appl Polym Sci, 1979, 23 (11): 3271-3280.

二级参考文献30

  • 1王树荣,廖艳芬,文丽华,骆仲泱,岑可法.钾盐催化纤维素快速热裂解机理研究[J].燃料化学学报,2004,32(6):694-698. 被引量:31
  • 2SALO K,MOJTAHEDI W.Fate of alkali and trace metals in biomass gasification[J].Biomass Bioenergy,1998,15(3):263-267.
  • 3STEENARI B-M,KARLSSON L G,LINDQVIST O.Evaluation of the leaching characteristics of wood ash and the influence of ash agglomeration[J].Biomass Bioenergy,1999,16(2):119-136.
  • 4SUTTON D,KELLEHER B,ROSS J R H.Review of literature on catalysts for biomass gasification[J].Fuel Process Technol,2001,73(3):155-173.
  • 5BROWN R C,LIU Q,NORTON G.Catalytic effects observed during the co-gasification of coal and switchgrass[J].Biomass Bioenergy,2000,18(6):499-506.
  • 6ARTHURJrJC 陈德峻.纤维素化学与工艺学[M].北京:轻工业出版社,1983..
  • 7VOLKER S,RIECKMANN Th.Thermokinetic investigation of cellulose pyrolysis-impact of initial and final mass on kinetic results[J].J Anal Appl Pyrolysis,2002,62(2):165-177.
  • 8KOGA N A.Review of the mutual dependence of Arrhenius parameters evaluated by the thermoanalytical study of solid-state reactions:the kinetic compensation effect[J].Thermochim Acta,1994,244:1-20.
  • 9BRADBURY A G W,SAKAI Y,SHAFIZADEH F.A kinetic model for pyrolysis of cellulose[J].J Appl Polym Sci,1979,23(11):3271-3280.
  • 10LUO Z,WANG S,LIAO Y,CEN K.Mechanism study of cellulose rapid pyrolysis[J].Ind Eng Chem Res,2004,43(18):5605-5610.

共引文献114

同被引文献218

引证文献20

二级引证文献205

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