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Essentials of Fluidization Technology最新文献

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Circulating Fluidized Beds 循环流化床
Pub Date : 2020-03-27 DOI: 10.1017/CBO9780511530142.011
L. Fan, C. Zhu
Introduction As discussed in Chapter 9, dense-phase fluidization other than particulate fluidization is characterized by the presence of an emulsion phase and a discrete gas bubble/void phase. At relatively low gas velocities in dense-phase fluidization, the upper surface of the bed is distinguishable. As the gas velocity increases, the bubble/void phase gradually becomes indistinguishable from the emulsion phase. The bubble/void phase eventually disappears and the gas evolves into the continuous phase with further increasing gas velocities. In a dense-phase fluidized bed, the particle entrainment rate is low and increases with increasing gas velocity. As the gas flow rate increases beyond the point corresponding to the disappearance of the bubble/void phase, a drastic increase in the entrainment rate of the particles occurs such that a continuous feeding of particles into the fluidized bed is required to maintain a steady solids flow. Fluidization at this state, in contrast to dense-phase fluidization, is denoted lean-phase fluidization. Lean-phase fluidization encompasses two flow regimes, i.e. , the fast fluidization regime and the dilute transport regime. The fast fluidization regime is characterized by a heterogeneous flow structure, whereas the dilute transport regime is characterized by a homogeneous flow structure. The circulating fluidized bed (CFB) is a fluidized bed system in which solid particles circulate between the riser and the downcomer. The fast fluidization regime is the principal regime under which the circulating fluidized bed is operated. The operating variables for a circulating fluidized bed system include both the gas flow rate and the solids circulation rate, in contrast to the gas flow rate only in a dense–phase fluidized bed system. The solids circulation is established by a high velocity of gas flow. Note that the dilute transport regime is discussed in Chapter 11, in the context of pneumatic conveying.
如第9章所述,致密相流化的特点是存在乳液相和离散的气泡/空隙相,而不是颗粒流化。在致密相流化过程中,在相对较低的气速下,床层的上表面是可区分的。随着气速的增加,气泡/空洞相逐渐与乳状相难以区分。随着气速的进一步增大,气泡/空洞相最终消失,气体演化为连续相。在密相流化床中,颗粒夹带率较低,且随气速的增加而增加。当气体流速增加到气泡/空洞相消失时,颗粒的夹带速率急剧增加,因此需要连续向流化床输送颗粒以保持稳定的固体流动。在此状态下的流化,与密相流化相反,被称为细相流化。贫相流化包括两种流态,即快速流态化和稀输运。快速流化的特点是非均质流动结构,而稀输输的特点是均质流动结构。循环流化床(CFB)是一种固体颗粒在上升管和下降管之间循环的流化床系统。快速流化工况是循环流化床运行的主要工况。循环流化床系统的操作变量包括气体流速和固体循环速率,而致密相流化床系统只有气体流速。固体循环是由高速气体流动建立的。请注意,稀释输送制度将在第11章气力输送中讨论。
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引用次数: 22
Liquid Fluidization 液体流化
Pub Date : 2020-03-27 DOI: 10.1002/9783527699483.ch3
R. Di Felice, A. Di Renzo
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引用次数: 1
Slug Flow 弹状流
Pub Date : 2020-03-27 DOI: 10.1002/9783527699483.ch8
J. R. Grace
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引用次数: 6
Downer Reactors 唐纳反应堆
Pub Date : 2020-03-27 DOI: 10.1002/9783527699483.ch20
Changning Wu, Yi Cheng
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引用次数: 2
Heat and Mass Transfer 传热传质
Pub Date : 2020-03-27 DOI: 10.1002/9783527699483.ch14
Dening Jia
Why heat and mass transfer ................................................................................................................................1 Fundamentals of heat transfer (what is it) ..........................................................................................................2 Thermodynamics of heat transfer .................................................................................................................. 3 Physical transport phenomena ....................................................................................................................... 5 Thermal conductivity ................................................................................................................................. 7 Heat equation ............................................................................................................................................... 10 Modelling space, time and equations ........................................................................................................... 11 Case studies ................................................................................................................................................. 12 Nomenclature refresh ................................................................................................................................... 12 Objectives of heat transfer (what for) ...............................................................................................................13 Relaxation time ............................................................................................................................................ 14 Conduction driven case (convection dominates) ..................................................................................... 15 Convection driven case (conduction dominates) ..................................................................................... 16 Heat flux ...................................................................................................................................................... 17 Temperature field ......................................................................................................................................... 19 Dimensioning for thermal design ................................................................................................................ 20 Procedures (how it is done) ..............................................................................................................................21 Thermal design ............................................................................................................................................ 21 Thermal analysis .......................................................................................................................................... 21 Mathematical modelling .............................................................
何必heat, and弥撒transfer ................................................................................................................................ 1这是Fundamentals of heat transfer(的一些东西整合起来的小队,☆ ) .......................................................................................................... 2Thermodynamics of heat transfer ..................................................................................................................三在transport phenomena .......................................................................................................................五Thermal conductivity .................................................................................................................................七Heat equation ...............................................................................................................................................10 Modelling太空,与时代,and equations ...........................................................................................................Case总署11 .................................................................................................................................................12 Nomenclature refresh ...................................................................................................................................美国小妞12 Objectives of heat transfer(的一些东西整合起来 ) ............................................................................................................... 13休息是美国在线与时代 ............................................................................................................................................14 Conduction driven case (convection dominates ) .....................................................................................15 Convection driven case (conduction dominates ) .....................................................................................16 Heat flux ......................................................................................................................................................17 Temperature战地警卫 .........................................................................................................................................19岁的美国小妞Dimensioning thermal设计学院 ................................................................................................................没说20 Procedures(如何学习我们还 ) .............................................................................................................................. 21Thermal设计学院 ............................................................................................................................................21 Thermal analysis ..........................................................................................................................................21 Mathematical modelling ..............................................................................................
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引用次数: 0
Operating Challenges 操作的挑战
Pub Date : 2020-03-27 DOI: 10.1002/9783527699483.ch13
P. Mehrani, A. Sowinski
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引用次数: 0
Turbulent Fluidization 湍流流化
Pub Date : 2020-03-27 DOI: 10.1002/9783527699483.ch9
X. Bi
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引用次数: 0
Index 指数
Pub Date : 2020-03-27 DOI: 10.1002/9783527699483.index
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引用次数: 0
期刊
Essentials of Fluidization Technology
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