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Application of different diffusion approaches in oxy-fuel combustion of single coal char particles

机译:不同扩散方法在单煤焦炭颗粒含氧燃烧中的应用

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The paper elaborates the influence of the non-equimolar and equimolar counterdiffusion on combustion of single coal char particles in the oxy-fuel combustion conditions. The phenomenon of the non-equimolar counterdiffusion is usually neglected and superseded by the equimolar counterdiffusion. Such a replacement can lead to results, e.g. to char burnout, particle temperature and species concentrations, which do not agree with the real process. The paper presents the numerical results of single coal char particle combustion in the oxy-fuel combustion conditions at which the effect of the equimolar and non-equimolar counterdiffusion has been taken into consideration. It has been assumed that the char carbon heterogeneously reacts with O_2, CO_2 and H_2O forming CO or CO_2 and H_2 depending on the combustion conditions. The reactions in the gas phase have been neglected to achieve the state of pure diffusion. The combustion of the particle is described by the mass and energy conservation equations commonly used in Euler-Lagrange computations of pulverized coal combustion. Numerical simulations performed for various values of the particle diameter and reagent concentrations clearly show that the use of the equimolar counterdiffusion model always overpredicts the non-equimolar one. Since the molar fluxes of the equimolar counterdiffusion are not coupled each other, the mass transfer towards the particle burning is higher which gives particle temperature and reaction rates too high compared to the non-equimolar counterdiffusion. Occurring discrepancy further develops during combustion also for other quantities describing the process, i.e. char burnout and gas concentrations at the particle surface. A simple correction which is proposed consists in reducing the value of the equimolar mass transfer coefficient that decreases the mass transfer and consequently letting the equimolar counterdiffusion model to be effortlessly used and get results which well follow the non-equimolar model. Such a simplified treatment of complex non-equimolar counterdiffusion can be easily implemented into numerical codes and needs no numerical solution of coupled non-linear equations describing the non-equimolar counterdiffusion.
机译:本文阐述了在氧气-燃料燃烧条件下,非等摩尔和等摩尔反扩散对单个煤焦颗粒燃烧的影响。非等摩尔反扩散现象通常被等摩尔反扩散所忽略并取代。这样的替换可以导致结果,例如。炭烧尽,颗粒温度和物质浓度与实际过程不一致。本文介绍了在考虑了等摩尔和非等摩尔反扩散影响的氧-燃料燃烧条件下单煤焦颗粒燃烧的数值结果。已经假定,取决于燃烧条件,焦炭碳与O_2,CO_2和H_2O异质反应形成CO或CO_2和H_2。气相中的反应被忽略以实现纯扩散状态。颗粒的燃烧由粉煤燃烧的Euler-Lagrange计算中常用的质量和能量守恒方程描述。对粒径和试剂浓度的各种值进行的数值模拟清楚地表明,等摩尔反扩散模型的使用总是高估了非等摩尔模型。由于等摩尔反扩散的摩尔通量彼此不耦合,因此与非等摩尔反扩散相比,朝着颗粒燃烧的传质更高,这使得粒子温度和反应速率过高。在燃烧过程中,对于描述该过程的其他数量,即炭烧尽和颗粒表面的气体浓度,还会出现差异。提出的简单校正包括减小等摩尔传质系数的值,该系数降低了质量传递,结果是毫不费力地使用了等摩尔反扩散模型,并获得了很好地遵循非等摩尔模型的结果。复杂的非等分反扩散的这种简化处理可以轻松地实现为数字代码,并且不需要描述非等分反扩散的耦合非线性方程的数值解。

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