期刊文献+

生物质焦油热裂解动力学参数实验研究 被引量:3

Experimental study on kinetic parameters of thermal cracking of biomass tar
下载PDF
导出
摘要 基于进样过程中焦油蒸发的不稳定性以及反应温度的测定和控制难度,设计了移动床焦油进样系统,使用样品槽携带焦油进入具有线性温度分布的炉膛空间,以样品槽的运动进样代替焦油流动进样,以获得稳定的焦油蒸发进样和更容易控制的反应温度。在此基础上,研究了不同进样速率下的焦油热裂解及其动力学特性。结果表明,在573~1 123 K,焦油的裂解率随温度的升高而加速升高,并在1 123 K时达到58%的裂解率;焦油热裂解遵循一级动力学反应,其平均活化能为39.5 kJ/mol,指前因子为1.58 min-1。 For the reason of the unstable evaporation in the tar sampling process and the difficulty of measuring and controlling reaction temperature,a moving bed as the tar sample introduction system was designed.A sample tray carrying tar was moved into the furnace with linear temperature distribution of the entrance zone.The movement of the tray instead of that of the tar,makes the tar sample introduction process more stable and the temperature easer to control.On this basis,tar cracking process and kinetic characteristics with the different sample introduction rate were studied.The results indicate the tar cracking rate is accelerated with increasing temperature at 573~1 123 K.The tar cracking rate reaches 58% at 1 123 K.The tar thermal cracking reaction is a first order reaction.On average,the activation energy is 39.5 kJ/mol and the pre-exponential factor is 1.58 min-1.
出处 《燃料化学学报》 EI CAS CSCD 北大核心 2012年第9期1060-1066,共7页 Journal of Fuel Chemistry and Technology
基金 重庆市重点自然科学基金(CSTC2013JJB0021) 重庆大学211工程"三期建设"项目(s-09101)
关键词 进样方式 加热方式 焦油 热裂解 动力学参数 sample introduction methord; heating mode; tar; thermal cracking; kinetic parameters
  • 相关文献

参考文献21

  • 1PARK H J, PARK S H, SOHN J M. Steam reforming of biomass gasification tar using benzene as a model compound over various Ni supported metal oxide catalysts[ J]. Bioresour Technol, 2010, 101 ( 1 ) : S101-S103.
  • 2GRANOVSKII M, GERSPACHER R, PUGSLEY T. An effect of tar model compound toluene treatment with high-temperature flames [ J ]. Fuel, 2012, 92( 1 ): 369-372.
  • 3LI C, HIRABAYASHI D, SUZUKI K. Development of new nickel based catalyst for biomass tar steam reforming producing H2-rich syngas [J]. Fuel Process Technol, 2009, 90(6) : 790-796.
  • 4YOON S J, CHOI Y-C, LEE J-G. Hydrogen production from biomass tar by catalytic steam reforming [ J ]. Energy Convers Manage, 2010, 51 ( 1 ) : 42-47.
  • 5TAO K, OHTA N, LIU G, YONEYAMAY, WANG T, TSUBAKI N. Plasma enhanced catalytic reforming of biomass tar model compound to syngas[J]. Fuel, 2010, 34(9) : 1363-1374.
  • 6VIRGINIE M, COURSON C, KIENNEMANN A. Toluene steam reforming as tar model molecule produced during biomass gasification with an iron/olivine catalyst[J]. C R Chim, 2010, 13(10) : 1319-1325.
  • 7FOURCAULT A , MARIAS F, MICHON U. Modelling of thermal removal of tars in a high temperature stage fed by a plasma torch [J]. Biomass Bioenergv. 2010. 34(9) : 1363-1374.
  • 8NOICHI H, UDDIN A, SASAOKA E. Steam reforming of naphthalene as model biomass tar over iron-aluminum and iron-zirconium oxide catalyst catalysts[J]. Fuel Process Technol, 2010, 91( 11 ) : 1609-1616.
  • 9ABU EL-RUB Z, BRAMER E A, BREM G. Experimental comparison of biomass chars with other catalysts for tar reduction[ J ]. Fuel, 2008, 87 ( 10/11 ) : 2243-2252.
  • 10FAUNDEZ J M, GARCiA X A, GORDON A L. A kinetic approach to catalytic pyrolysis of tars[ J ]. Fuel Process Technol, 2001,69 (3) : 239-256.

同被引文献13

引证文献3

二级引证文献16

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