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Biomass torrefaction in a standard retort: A study on oil palm solid residues

机译:标准干馏罐中的生物质干馏:油棕固体残留物的研究

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摘要

This study evaluates the torrefaction of oil palm empty fruit bunches (EFB) and mesocarp fiber in a standard retort at laboratory scale (according to standard ISO 647). The influence of torrefaction temperature (220 degrees C-270 degrees C), residence time (up to 60 min) and reactor heating rate (5 K/min-15 K/min) are determined on solid, liquid and gas yields, as well as their chemical and fuel properties. Torrefaction yielded between 64 wt-% and 92 wt-% solid that exhibited lower heating value increase between 11 % and 28 % compared to the original biomass. The liquid fraction ranges between 6 wt-% and 26 wt-% of the raw biomass, containing 26 wt-%-42-wt% of water and LHV up to 11 MJ/kg. The gas fraction represents 1 wt-%-9 wt-% of the original biomass with LHV between 0,6 MJ/kg-2,4 MJ/kg. Optimum trade-offs for solid yields and lower heating values were obtained for torrefaction with a heating rate of 10 K/min and a residence time of 30 min at 272 degrees C for EFB (62,8 wt-% solid yield and 17,7% increase in the original LHV) and at 282 degrees C for fiber (65,3 wt-% solid yield and 25,8% increase in LHV). A formal reaction kinetic model for pyrolyis coupled to a thermal model of the retort has been tested and used to simulate the solid mass yield and lower heating value during torrefaction and to determine the optimum trade-offs between both parameters. Simulated temperature gradients inside the retort solid bed are as high as 55 degrees C during heating up at a torrefaction temperature of T-torr = 250 degrees C and around 25 degrees C after a residence time of 30 min at this temperature. These results are relevant and decisively influence the solid yield during torrefaction in the retort.
机译:这项研究在实验室规模下(根据标准ISO 647)评估了油棕空果串(EFB)和中果皮纤维的烘焙度。还要确定焙干温度(220摄氏度至270摄氏度),停留时间(长达60分钟)和反应器加热速率(5 K / min-15 K / min)对固体,液体和气体产率的影响作为它们的化学和燃料特性。焙干得到的固体含量在64重量%至92重量%之间,与原始生物质相比,其显示出较低的热值增加量在11%至28%之间。液体部分的范围为原始生物质的6重量%至26重量%,包含26重量%-42重量%的水和高达11MJ / kg的LHV。气体分数代表原始生物质的1 wt%-9 wt%,LHV在0.6 MJ / kg-2,4 MJ / kg之间。对于EFB,以10 K / min的加热速率和272℃的停留时间为30 min的焙干获得了固体收率和较低发热量的最佳平衡(固体收率为62.8 wt%,17.7原始LHV增加了5%,而纤维在282摄氏度下(固含量65.3 wt%,LHV增加了25.8%)。已经测试了用于热解的正式反应动力学模型与干馏瓶的热模型,并将其用于模拟烘焙过程中的固体质量产率和较低的热值,并确定这两个参数之间的最佳折衷。在T-torr = 250摄氏度的烘焙温度下加热,在此温度下停留30分钟后,在加热过程中,脱水锅固体床内部的模拟温度梯度高达55摄氏度。这些结果是相关的,并决定性地影响杀菌罐中烘焙过程中的固体收率。

著录项

  • 来源
    《Fuel》 |2019年第15期|366-378|共13页
  • 作者单位

    Univ Nacl Colombia, Fac Ingn, Dept Ingn Mecan & Mecatron, Grp Invest Biomasa & Optimizat Term Proc BIOT,Sed, Carrera 30 45A-03 Edificio 453 Of 400, Bogota, Colombia;

    Univ Nacl Colombia, Fac Ingn, Dept Ingn Mecan & Mecatron, Grp Invest Biomasa & Optimizat Term Proc BIOT,Sed, Carrera 30 45A-03 Edificio 453 Of 400, Bogota, Colombia;

    Univ Nacl Colombia, Fac Ingn, Dept Ingn Mecan & Mecatron, Grp Invest Biomasa & Optimizat Term Proc BIOT,Sed, Carrera 30 45A-03 Edificio 453 Of 400, Bogota, Colombia;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Torrefaction; Biomass; Empty fruit bunches; Mesocarp fiber; Oil palm; Retort;

    机译:烘焙;生物质;空果串;中果皮纤维;油棕;Re;

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