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Computational Investigations of Low-Emission Burner Facilities for Char Gas Burning in a Power Boiler

机译:低排放燃烧器设备对焦炉煤气燃烧的计算研究

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Various variants for the structure of low-emission burner facilities, which are meant for char gas burning in an operating TP-101 boiler of the Estonia power plant, are considered. The planned increase in volumes of shale reprocessing and, correspondingly, a rise in char gas volumes cause the necessity in their cocombustion. In this connection, there was a need to develop a burner facility with a given capacity, which yields effective char gas burning with the fulfillment of reliability and environmental requirements. For this purpose, the burner structure base was based on the staging burning of fuel with the gas recirculation. As a result of the preliminary analysis of possible structure variants, three types of early well-operated burner facilities were chosen: vortex burner with the supply of recirculation gases into the secondary air, vortex burner with the baffle supply of recirculation gases between flows of the primary and secondary air, and burner facility with the vortex pilot burner. Optimum structural characteristics and operation parameters were determined using numerical experiments. These experiments using ANSYS CFX bundled software of computational hydrodynamics were carried out with simulation of mixing, ignition, and burning of char gas. Numerical experiments determined the structural and operation parameters, which gave effective char gas burning and corresponded to required environmental standard on nitrogen oxide emission, for every type of the burner facility. The burner facility for char gas burning with the pilot diffusion burner in the central part was developed and made subject to computation results. Preliminary verification nature tests on the TP-101 boiler showed that the actual content of nitrogen oxides in burner flames of char gas did not exceed a claimed concentration of 150 ppm (200 mg/m~3).
机译:考虑了低排放燃烧器设施的结构的各种变体,这些变体用于在爱沙尼亚电厂运行的TP-101锅炉中燃烧焦炭。页岩后处理量的计划增加,以及相应的炭气量的增加,导致其共燃烧的必要性。在这方面,需要开发具有给定容量的燃烧器设备,该燃烧器设备在满足可靠性和环境要求的情况下产生有效的焦炭燃烧。为此,燃烧器结构的基础是基于气体再循环的阶段性燃烧。作为对可能的结构变型的初步分析的结果,选择了三种类型的运行良好的早期燃烧器设施:涡流燃烧器,其向二次空气中供应再循环气体;涡流燃烧器,其挡板在空气流之间提供再循环气体。一次和二次空气,以及带有涡流引燃燃烧器的燃烧器设备。使用数值实验确定了最佳的结构特征和操作参数。使用ANSYS CFX捆绑的计算流体力学软件对这些实验进行了模拟,混合,着火和燃烧炭气的燃烧。数值实验确定了每种燃烧器设备的结构和运行参数,这些参数可有效燃烧焦炭并符合氮氧化物排放所需的环境标准。开发了在中央部分采用先导扩散燃烧器燃烧炭气的燃烧器设备,并使其受计算结果的影响。在TP-101锅炉上进行的初步验证性质测试表明,炭气燃烧器火焰中氮氧化物的实际含量未超过所声称的150 ppm(200 mg / m〜3)的浓度。

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