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Experimental and modelling studies of coal/biomass oxy-fuel combustion in a pilot-scale PF combustor

机译:中试PF燃烧室中煤/生物质氧燃料燃烧的实验和模型研究

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摘要

This thesis focuses on enhancing knowledge on co-firing oxy-combustion cycles to boost development of this valuable technology towards the aim of it becoming an integral part of the energy mix. For this goal, the present work has addressed the engineering issues with regards to operating a retrofitted multi-fuel combustor pilot plant, as well as the development of a rate-based simulation model designed using Aspen Plus®. This model can estimate the gas composition and adiabatic flame temperatures achieved in the oxy-combustion process using coal, biomass, and coal-biomass blends. The fuels used for this study have been Daw Mill coal, El Cerrejon coal and cereal co-product. A parametric study has been performed using the pilot-scale 100kWth oxy-combustor at Cranfield University and varying the percentage of recycle flue gas, the type of recycle flue gas (wet or dry), and the excess oxygen supplied to the burner under oxy-firing conditions. Experimental trials using co-firing with air were carried out as well in order to establish the reference cases. From these tests, experimental data on gas composition (including SO3 measurement), temperatures along the rig, heat flux in the radiative zone, ash deposits characterisation (using ESEM/EDX and XRD techniques), carbon in fly ash, and acid dew point in the recycle path (using an electrochemical noise probe), were obtained. It was clearly shown during the three experimental campaigns carried out, that a critical parameter was that of minimising the air ingress into the process as it was shown to change markedly the chemistry inside the oxy-combustor.Finally, part of the experimental data collected (related to gas composition and temperatures) has been used to validate the kinetic simulation model developed in Aspen Plus®. For this validation, a parametric study considering the factor that most affect the oxy-combustion process (the above mentioned excess amount of air ingress) was varied. The model was found to be in a very good agreement with the empirical results regarding the gas composition.
机译:本文的重点是增强关于共燃氧燃烧循环的知识,以促进这项有价值的技术的发展,以使其成为能源组合的组成部分。为了实现这一目标,目前的工作已解决了与改造多燃料燃烧器试验装置的运行有关的工程问题,以及使用AspenPlus®设计的基于速率的仿真模型的开发。该模型可以估计在使用煤,生物质和煤生物质混合物的氧气燃烧过程中达到的气体成分和绝热火焰温度。这项研究使用的燃料是Daw Mill煤,El Cerrejon煤和谷物副产品。使用Cranfield大学的中试规模100kWth氧燃烧器进行了参数研究,并改变了循环烟气的百分比,循环烟气的类型(湿式或干式)以及在氧气条件下供应给燃烧器的过量氧气射击条件。为了建立参考案例,还进行了使用空气共烧的实验。通过这些测试,获得了有关气体成分(包括SO3测量),沿钻机的温度,辐射区的热通量,烟灰沉积特征(使用ESEM / EDX和XRD技术),粉煤灰中的碳和酸露点的实验数据。获得了循环路径(使用电化学噪声探头)。在进行的三个实验过程中清楚地表明,关键参数是最大程度地减少进入过程的空气,因为它被证明会显着改变氧燃烧器内部的化学性质。最后,部分实验数据得到了收集(与气体组成和温度相关的参数)已用于验证AspenPlus®中开发的动力学模拟模型。为了进行此验证,对考虑了最影响氧气燃烧过程的因素(上述过量进气量)的参数研究进行了更改。发现该模型与关于气体成分的经验结果非常吻合。

著录项

  • 作者

    Jurado Pontes Nelia;

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  • 年度 2014
  • 总页数
  • 原文格式 PDF
  • 正文语种 {"code":"en","name":"English","id":9}
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