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Transient studies in fast-fluidized beds.

机译:快速流化床中的瞬态研究。

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An important characteristic of fast-fluidized beds (FFBs) is the tendency of the solid particles to aggregate into clusters. Such clusters can strongly affect operational characteristics such as particle holdup, pressure drop, wall heat transfer, and axial mixing. Though the phenomenon has been known to occur in fluidized beds for more than two decades, very little cluster characteristic data is available. Therein lies the motivation for the current work. The primary research goals of this thesis are to (a) gather transient solid concentration data in both upflow and downflow fast-fluidized beds, hence determining cluster properties as functions of operating conditions; and (b) model the dynamics of cluster formation and disintegration using a simple discrete particle model. Needle capacitance probes were used to determine cluster characteristics in a 15-cm I.D. upflow FFB (riser) at Lehigh University, and in a 15-cm I.D. downflow FFB (downer) at Universitat Erlangen-Nürnberg. Experiments were conducted using two particle sizes (70, 120-μ m) at gas velocities warying from 4.0 to 6.6-m/ s. Solid flax was varied from 50 to 120-kg/ m2/s.; Results are presented that indicate the parametric effects of particle size, superficial gas velocity, and solid flux on cluster characteristics, such as solid volume fraction in clusters, cluster duration time, time-fraction of cluster existence, local cluster velocity, cluster length, and cluster flux, in both the riser and downer. For identical flow conditions, average solid density (and solid density in clusters) in the riser was higher than that in the downer. Number-averaged solid volume fraction in clusters was found to be 2.38 times the time-averaged local solid volume fraction. Interestingly, time fraction of cluster existence was found to be independent of flow conditions. Knowledge of clusters and dispersed phase density and velocity allowed us to calculate the relative contribution of solid-flux through cluster and dispersed phase. Both of these generalizations point toward a self-similarity in flow characteristics of fast fluidized beds. It was found that the ratio of local time averaged cluster flux to local total time-averaged solid flux was in the range of 0.3–0.6.; A discrete particle model was developed to examine the effect of particle-particle collision on clustering tendencies in particle systems. The model answers a fundamental question: Can inelastic particle-particle collisions alone give rise to particle clusters? One-dimensional results showed that systems with elastic collisions never induced clusters, while inelastic collisions always led to clustering.
机译:快速流化床(FFB)的一个重要特征是固体颗粒倾向于聚集成团。这样的团簇会严重影响操作特性,例如颗粒滞留,压降,壁传热和轴向混合。尽管已经知道该现象在流化床中发生了二十多年,但几乎没有可用的簇特征数据。这就是当前工作的动力。本论文的主要研究目标是(a)收集上流和下流快速流化床中的瞬时固体浓度数据,从而确定簇的性质作为操作条件的函数; (b)使用简单的离散粒子模型对团簇形成和分解的动力学进行建模。针电容探针用于确定内径15厘米的簇特征。利哈伊大学(Lehigh University)和内径15厘米的上流FFB(上升管)厄兰根-纽伦堡大学的下流式FFB(下降器)。实验使用了两种粒径(70、120-μm)在从4.0到6.6μm/ italic / italic警惕的气体速度下进行。固体亚麻的含量从50到120- kg / m 2 / s 。结果表明颗粒大小,表观气体速度和固体通量对团簇特性的参数影响,例如团簇中的固体体积分数,团簇持续时间,团簇存在的时间分数,团簇局部速度,团簇长度和提升管和下降管中的簇通量。对于相同的流动条件,立管中的平均固体密度(和簇中的固体密度)高于下管中的平均固体密度。发现簇中的数均固体体积分数是时间平均局部固体体积分数的2.38倍。有趣的是,发现簇存在的时间分数与流动条件无关。通过了解团簇以及分散相的密度和速度,我们可以计算通过团簇和分散相的固相通量的相对贡献。这两种概括都指向快速流化床的流动特性的自相似性。发现局部时间平均簇通量与局部总时间平均固体通量之比在0.3-0.6之间。建立了离散粒子模型以检查粒子间碰撞对粒子系统中聚集趋势的影响。该模型回答了一个基本问题:仅非弹性粒子-粒子碰撞是否会引起粒子团簇?一维结果表明,具有弹性碰撞的系统从不诱导聚类,而非弹性碰撞始终导致聚类。

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