共查询到18条相似文献,搜索用时 375 毫秒
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燃烧高水分低热值燃料的内旋流流化床燃烧技术研究 总被引:7,自引:2,他引:7
内旋流型流化床炉利用非均匀布风产生高温气-固两相旋流,使燃料在炉内运动、相互碰撞、干燥、破碎、燃烧,并可通过改变布风控制燃料加热与挥发份析出速率、燃烧温度与热负荷,适合多种高水分劣质煤及城市垃圾的洁净燃烧,是一种高效低污染流化床燃烧技术。本文研究该型燃烧器床内空气运动、燃烧、传热及排放规律,发展新型清洁燃烧技术。 相似文献
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稠密气固两相流动过程模拟的改进模型与应用 总被引:2,自引:0,他引:2
提出了模拟稠密气固两相流动的改进模型。湍流流场采用改进的k-ε-εe模型,颗粒的聚合效应采用聚合力的当量直径折算模型计算。将颗粒团作为离散相,研究颗粒团的运动、碰撞、破碎与合并。应用上述模型数值模拟了循环流化床内的稠密气固两相流动。得到了床内气相速度、颗粒团分布、颗粒浓度分布及颗粒团大小分布等详细两相流场信息。计算结果合理,与前人实验结果相符。模拟结果详细揭示了循环流化床内稠密气固两相流动的基本特征。图8表2参8 相似文献
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流化床内气固两相流动一直是实验研究和数值模拟的热点。基于Eulerian双流体模型,本文建立了流化床内的气固两相流动模型,采用FLUENT软件对流化床密相区两相流动特性、床内气泡的产生运动和爆裂等特性进行了数值模拟。模型中,将颗粒相看作是连续介质,建立与气相相同形式的数学模型;采用了离散介质动力理论,引入颗粒温度来描述固相粘性应力,并用气固曳力进行气固两相耦合。模拟得到了气泡产生、运动和爆裂的变化过程,与实验结果相一致。采用不同的曳力模型对流化床稠密两相流动进行了模拟,与Kuipers实验对比,结果表明采用Gidaspow曳力模型描述流化床稠密两相流动特性更准确。 相似文献
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《International Journal of Heat and Mass Transfer》2006,49(19-20):3338-3342
A new particle image technique was developed to analyze the dispersion of tracer particles in an internally circulating fluidized bed (ICFB). The movement course and the concentration distribution of tracer particles in the bed were imaged and the degree of inhomogeneity of tracer particles was analyzed. The lateral and axial dispersion coefficients of particles were calculated for various zones in ICFB. Results indicate that the lateral diffusion coefficient in the fluidized bed with uneven air distribution is significantly higher than that in uniform bubbling beds with even air distribution. The dispersion coefficients are different along bed length and height. 相似文献
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复合床式低倍率循环流化床锅炉的研制开发 总被引:1,自引:0,他引:1
本文全面分析了较高循环倍率循环流化床锅炉所存在的技术问题,提出采用设计经验成熟、运行稳定可靠、热效率高、电耗低的低循环倍率循环流化床锅炉技术来实现循环流化床锅炉的大型化的新技术思想,并据此研制开发出复合床式低倍率循环流化床锅炉新技术。通过介绍和分析复合床式低倍率循环流化床锅炉的技术原理及技术特点,展示新炉型所具有的锅炉主要部件的灵活布置方式,为循环流化床锅炉的大型化指出了新的发展方向。 相似文献
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Nobuyuki Gokon Tetsuro MatagaNobuyuki Kondo Tatsuya Kodama 《International Journal of Hydrogen Energy》2011,36(8):4757-4767
Thermochemical two-step water splitting using a redox system of iron-based oxides or ferrites is a promising process for producing hydrogen without CO2 emission by the use of high-temperature solar heat as an energy source and water as a chemical source. In this study, thermochemical hydrogen production by two-step water splitting was demonstrated on a laboratory scale by using a single reactor of an internally circulating fluidized bed. This involved the successive reactions of thermal-reduction (T-R) and water-decomposition (W-D). The internally circulating fluidized bed was exposed to simulated solar light from Xe lamps with an input power of 2.4-2.6 kWth for the T-R step and 1.6-1.7 kWth for the subsequent W-D step. The feed gas was switched from an inert gas (N2) in the T-R step to a gas mixture of N2 and steam in the W-D step. NiFe2O4/m-ZrO2 and unsupported NiFe2O4 particles were tested as a fluidized bed of reacting particles, and the production rate and productivity of hydrogen and the reactivity of reacting particles were examined. 相似文献
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采用三准则相似理论设计了循环流化床烟气脱硫气固两相流动试验台.通过对循环流化床脱硫反应器试验装置内沿高度方向阻力分布和不同高度截面上局部颗粒质量通量的测量,详细地研究了脱硫反应器内气固两相流动规律和内循环特性.结果表明:脱硫反应器阻力主要集中在文丘里管段,而且随着循环物料量和气体流量的增加,系统阻力显著增加;脱硫反应器内气固两相流动呈典型的环核流动结构,边壁下降流颗粒浓度高,中心区域上升流颗粒浓度低,且固体质量回流比率随着脱硫反应器高度的上升而下降.研究结果为循环流化床烟气脱硫系统的设计与放大提供了依据. 相似文献