期刊文献+

基于热重红外的硫酸盐法黑液热解特性分析 被引量:4

TG-FT-IR Analysis of Pyrolysis Characteristics of Sulfate Black Liquor
下载PDF
导出
摘要 为了深入地探讨黑液热解的反应机理以及黑液热解过程中产物的释放规律,采用热重-红外联用( TG-FT-IR)技术对竹子和桉木混合硫酸盐法制浆黑液固形物( BLS)的热裂解过程进行了研究。 TG-FT-IR结果显示,BLS热解产物的释放主要集中在500~2000 s,热解产物主要是 CO2、CH4、H2O、CO、醇酚类化合物和醛酮类化合物。 BLS的整个热解过程可分为3个阶段,第1阶段的失重主要是原料中结合水的挥发引起的,此阶段的最大失重速率出现在105℃;第2失重阶段主要发生在173~518℃,失重率约为25.19%,主要产物是CO2、CH4、H2O、醇酚类化合物、醛酮类化合物以及少量的CO,此阶段CO2的生成量最大;第3阶段主要发生在722~1000℃,失重率接近39.05%,产物主要是CO,其它小分子产物的产率都很低。 To investigate the pyrolysis mechanism and the release law of pyrolysis prodncts, the sulfate black liquor (BLS) from bamboo & eucalyptus was pyrolyzed and the process was investigated by thermogravimetric analyzer coupled with Fourier transform infrared spectrometry (TG-FT-IR). The results revealed that the release of BLS pyrolysis products, such as C02, CH4, H20, CO and alcohols & phenols, aldehydes & ketones, were mainly concentrated in 500 - 2 000 s. The BLS pyrolysis process could be divided into three stages. The weight loss in the first stage should be attributed to the release of bound water in the raw material and the maximum weight loss rate was observed at 105 ℃. During the second weight loss stage from 173 ℃ to 518 ℃, the weight loss rate was about 25. 19% , and the release products were CO:, CH4, H20, alcohols & phenols, aldehydes & ketones and a small amount of CO, and COs was the dominant product. The third weight loss stage was from 722 ℃ to 1 000 ℃, and the weight loss rate was nearly 39.05%. In this stage, CO was the dominant product and very few amounts of other small molecule products were observed.
出处 《林产化学与工业》 EI CAS CSCD 北大核心 2014年第3期22-26,共5页 Chemistry and Industry of Forest Products
基金 国家973计划资助(2013CB228101) 国家自然科学基金资助项目(31270635 21176095)
关键词 硫酸盐法 黑液 热解 热重红外 sulfate black liquor pyrolysis TG-FT-IR
  • 相关文献

参考文献19

  • 1LARSON E D,CONSONNI S,KATOFSKY R E, et al. A cost-benefit assessment of gasification-based biorefining in the kraft pulp and paper industry[ R]. New Jersey, USA:The U. S. Department of Energy and the American Forest and Paper Association,2006.
  • 2BHATTACHARYA P K, SHRINATH A S, KUNZRU D. Pyrolysis of black liquor[ J]. Journal of Chemical Technology and Biotechnology, 1985, 35 A ( 5 ) : 223 -233.
  • 3郭伊丽,武书彬,王少光,郭秀强.黑液热裂解行为的初步研究[J].中国造纸,2006,25(12):65-67. 被引量:3
  • 4BASSILAKIS R, CARANGELO R M, WOJTOWICZ M A, et al. TG-FTIR analysis of biomass pyrolysis [ J] . Fuel,2001,80 ( 12 ) : 1765-1786.
  • 5HAN Long, WANG Qin-hui, MA Qiang, et al. Influence of CaO additives on wheat-straw pyrolysis as determined by TG-FTIR analysis [ J ]. Journal of Analytical and Applied Pyrolysis ,2010,88 (2) :199-206.
  • 6JONG D W, PIRONE A, WOJTOWICZ M A, et al. Pyrolysis of miscanthus giganteus and wood pellets:TG-Kl'IR analysis and reaction kinetics [J]. Fuel,2003,82(9) :1139-1147.
  • 7MASCHIO G, KOUFOPANOS C, LUCCHESI A. Pyrolysis, a promising route for biomass utilization [ J ]. Bioresource Technology, 1992,42 (3 : 219-231.
  • 8KOUFOPANOS C A,LUCCHESI A,MASCHIO G. Kinetic modeling of the pyrolysis of biomass and biomass components [ J ]. The Canadian Journal of Chemical Engineering, 1989,67 ( 1 ) :75-84.
  • 9武书彬,赵玉双,郭大亮,李擘,阴秀丽.桉木APMP制浆废液固形物的热解特性[J].华南理工大学学报(自然科学版),2012,40(9):1-7. 被引量:2
  • 10I'APPI T 650 0M-2005 (R2009) Solids content of black liquor[ S]. 2009.

二级参考文献28

  • 1Antal M J.Cellulose pyrolysis kinetics:the current states of knowledge[J].J.Ind.Eng.Chem.Res,1995,34:703
  • 2Eriksson H,Harvey S.Black liquor gasification-consequences for both industry and society[J].Energy,2004,29:581
  • 3Alén R,Rytkonen S,Mckeough P.Thermogravimetric behavior of black liquors and their organic constituents[J].Journal of Analytical and Appiled Pyrolysis,1991,31:1
  • 4Olsson J,Joglid U,Hald P,et al.Alkali metal emission during pyrolysis of biomass[J].Energy & Fuel,1997,11(5):779
  • 5Zhang Y, Ashizawa M, Kajitania S, et al. Proposal of a semi-empirical kinetic model to reconcile with gasification reactivity profiles of biomass chars [ J ]. Fuel, 2008,87 (4/5) :475-481.
  • 6Towers M, Karidio I, Uloth V. The potential impact of black liquor gasification on the Canadian pulp and paper industry [ R]. Quebec :Pulp and Paper Research Institute of Canada ,2005 : 12-18.
  • 7Backman R, Frederick W J, Hupa M. Basic studies on black-liquor pyrolysis and char gasification [J]. Biore- source Technology, 1993,46 ( 1/2 ) : 153-158.
  • 8Demirbas A. Pyrolysis and steam gasification processes of black liquor [ J ]. Energy Conversion and Management, 2002,43 ( 7 ) : 877- 884.
  • 9Guo D L, Wu S B, Lou R, et al. Effect of organic bound Na groups on pyrolysis and CO2-gasification of alkali lig- nin [J]. Bioresourccs,2011,6(4) :4145-4157.
  • 10Lou R, Wu S B, Lv G J, et al. Pyrolytic products from rice straw and enzymatic/mild acidolysis lignin (EMAL) [ J ]. Bioresources,2010,5 (4) :2184-2194.

共引文献3

同被引文献56

  • 1李志,曹欣玉,王凤寅,俞海淼,周俊虎,周志军,岑可法.黑液水煤浆的燃烧和污染排放特性研究[J].环境科学学报,2005,25(5):661-664. 被引量:7
  • 2辛银花.棉浆粕黑液处理技术的展望[J].人造纤维,2005,35(3):23-25. 被引量:13
  • 3武书彬,谭扬,郭伊丽,刘江燕.黑液的热失重特性及其动力学分析[J].华南理工大学学报(自然科学版),2007,35(6):59-63. 被引量:17
  • 4周勇.生物质热裂解动力学研究进展[J].化学工程师,2007,21(9):23-26. 被引量:3
  • 5石淑兰,何福望.制浆造纸分析与检测[M].中国轻工业出版社,2010.
  • 6Ma Z Q,Zhang Y M ,Zhang Q S,et al. Design and experi- mental investigation of a 190 kW biomass fixed bed gasifi- cation and polygeneration pilot plant using a double air stage downdraft approach [ J ]. Energy, 2012, 46: 140 - 147.
  • 7Gn X L, Ma X, Li L X, et al. Pyrolysis of poplar wood sawdust by TG-FTIR and Py-GC/blS[ J]. Journal of Ana- lytical and Applied Pyrolysis, 2013, 102:16 -23.
  • 8Gao N B, Li A M, Quan C, et al. TG-FTIR and Py-GC/ MS analysis on pyrolysis and combustion of pine sawdust [ J]. Journal of Analytical and Applied Pyrolysis, 2013, 100 : 26 - 32.
  • 9Chen D Y, Zheng Y, Zhu X F. In-depth investigation on the pyrolysis kinetics of raw biomass. Part I: Kinetic a- nalysis for the drying and devolatilization stages [ J ]. Bioresource Technology, 2013, 131 : 40 - 46.
  • 10Zhang J, Chen T, Wu J, et al. A novel Gaussian- DAEM-reaction model for the pyrolysis of cellulose, hemicellulose and lignin[ J]. RSC Advances, 2014, 4 : 17513 - 17520.

引证文献4

二级引证文献35

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