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理想和无气泡流态化 版权信息
- ISBN:9787030224422
- 条形码:9787030224422 ; 978-7-03-022442-2
- 装帧:暂无
- 册数:暂无
- 重量:暂无
- 所属分类:>
理想和无气泡流态化 本书特色
When fluidization was first employed industrially, e.g.,in the Winkler gasifjer,we had only the bubbling nuidized bed as shown in the middle diagram 0f the figure,in which gas bypasses as bubbles,thUS leading t0 poor SOlid—gas contact and incurring large pressure drop.What is ideal is the high dispersion Of SOlids shown as the background of the b00k jacket.Short 0f SUCh an ideal state,we may resort t0 suppressing bubbles by the use Of shallOw fluidized bed as shown on the lefthand side diagram achieved through redUCing the SOlid content Of the fludized bed.or the fast nuidized bed with continuous recyc“ng 0f SO“ds t0 the bOttom Of the bed,as shown on the righthand side diagram.All these diagrams 0f nuidization were generated through computer mode“ng by Professor Wei Ge,and from hOSts 0fthese diagrams,four were selected by Xue Bai, Jianxing Lu and Ying Ren tO portray the principal thesis nfthis book
理想和无气泡流态化 目录
1.1 The Fluidized State and How It Is Achieved
1.2 Nature of Hydrodynamic Suspension
1.3 Particle-Particle Forces
1.4 Species of Fluidization
1.5 Regimization of the Fluidized State
Chapter 2 IDEALIZATION OF THE FLUIDIZING PROCESS:Empirical Deductions from L/S Systems
Chapter 3 GENERALIZED FLUIDIZATION
3.1 Steady-State Motion
3.2 Moving Bed
3.3 Accelerative Motion
3.4 Polydisperse Systems
3.5 Computer Software
Chapter 4 FLUIDIZED LEACHING AND WASHING
4.1 Characteristics
4.2 Uniform Particles
4.3 Mixed Particles
4.4 Experimental Findings
4.5 Staging
4.6 Rate Measurement for Solids Leaching and Washing
Chapter 5 SOLIDS MIXING AND SEGREGATION
5.1 Phase Juxtaposition
5.2 Operation Shifts
5.3 Reversal Points
5.4 Degree of Segregation
5.5 Mixing-Segregation Equilibrium
5.6 Generalized Fluidization of Polydisperse Systems
Chapter 6 CONICAL FLUIDIZED BEDS
6.1 Phenomenological Description and Physical Modeling
6.2 The Basic Parameters
6.3 The Fully Fluidized State
6.4 With Hyperfluidized Fixed Bed
6.5 Ranges for Conical Fluidized Bed Operation
6.6 Charting Conical Fluidized Bed Operation and Experimenta Verification
6.7 Instability
Chapter 7 APPLICATION OF THE MOVING BED
7.1 Moving Bed Uptransport with Compressible Media
7.2 The Pneumatically Controlled Downcomer
Chapter 8 BUBBLELESS GAS/SOLID CONTACTING
8.1 Bubbling Fluidization and G/S Contacting Efficiency
8.2 Species of Bubbleless G/S Contacting
Chapter 9 SYSTEMS WITH DILUTE RAINING PARTICLES
9.1 Raining-Particles Heat Exchanger
9.2 Polydisperse Particles
9.3 Experimental Verification
9.4 Baffling and Particles Distribution
9.5 Countercurrent Staging of Cocurrent Systems
9.6 Pilot Plant Demonstration
Chapter 10 VOIDAGE DISTRIBUTION IN FAST FLUIDIZATION
10.1 Modeling Longitudinal Voidage Distribution
10.2 Evaluation of Parameters
10.3 Computing Voidage Distribution
10.4 Regime Diagram
10.5 Generalized Fluidization of Nonideal Systems
10.6 Radial Voidage Distribution
Chapter 11 SHALLOW FLUIDIZED BED
11.1 Relevant Work on Distributor
11.2 Fluid Flow above Distributor
1 1.3 Particle Behavior above Distributor
11.4 Assessment of Distributor Performance
11.5 Particle-Gas Transfer in Shallow Fluid Bed
11.6 Activated Solids Shallow Fluid Bed Heat Exchanger
11.7 Cocurrent Multi-Stage Shallow Fluid Bed
11.8 The co-MSFB as a Chemical Reactor
Chapter 12 FLUIDIZATION WITH NO NET FLUID FLOW
12.1 Levitation of Discrete Particles
12.2 Semi-Fluidization through Oscillatory Flow
12.3 Application to Pseudo Solid-Solid Reaction
Chapter 13 A COHERENT ANALYSIS FOR L/S AND G/S SYSTEMS
13.1 From Phenomena through Hypothesis to Modeling
13.2 The Multi-Scale Energy-Minimization Model
13.3 Charting StatUS Parameters
13.4 Reconciling L/S and G/S Systems
13.5 Regimes of Fluidization
Chapter 14 PoWDER ASSESSMENT
14.1 Geldart’s Classification
14.2 Powder Characterization by Bed Collapsing
14.3 Modeling the Three-Stage Bed Collapsing Process
14.4 Instrument for Automatic Surface Tracking and Data Processing
14.5 Qualitative Designation for Bed Collapsing。
14.6 Quantifying Fluidizing Characteristics of Powders
14.7 Improving Fluidization by Partide Size Adjustment
14.8 Fluidizing Quality and Particle-Particle Interaction
14.9 Measure of Synergism for Binary Particle Mixtures
Chapter 15 FUTURE PROSPECTS
15.1 Basic Mechanism
15.2 Further Reconciliation between G/S and L/S Systems
15.3 Polydisperse Systems and Powder Design
15.4 Intensification of L/S Operations
15.5 Staged Operation
15.6 Existing and New L/S Processes
15.7 Examples of Opportunities for Bubbleless G/S Contacting
NoTATIoNS
References
SUBJECT INDEX
ADDENDA
Chapter 16 FAST FLUIDIZATION AND ITS APPLICATIoNS
16.1 Types ofFast Fluidized Bed
16.2 Gas.solid Flow in Riser
16.3 Gas.solid Flow in Downcomer
16.4 Applications ofFast Fluidization
References
Chapter 17 MAGNEToFLUIDIZATIoN
17.1 Types ofMagnetofluidized Bed
17.2 Structure ofMagnetofluidized Bed
17.3 Hydroelynamics ofMagnetofluidization
17.4 Mixing Behaviors
17.5 Mass andHeatTransfer
17.6 Applications ofMagnetofluidization
References
理想和无气泡流态化 作者简介
p>Mooson Kwauk graduated from Univetsity of Shanghai in 1 943 and researched in fluidization under the late Professor Richard WIlhelm at Princeton UniVeTSitv from 1945 t0 1947.He has continued wotking in this field both in the United States and in China,and is now Professor and Director Emetitus of the Institute of Process Eng4neeririg of the Chino..se Academy 0f Scienccs。to which he was elected Member in 1980.In 1989 he reccived an International Fluidization Award 0f Achievement at the Sixth Interna— tional Fluidization Confefence held in Banff,Canada. The author postulates an idea“zed system of complete homogeneity that can be used in the 8.nalysis of many engineeting problems,e.g., · generalized fl uidization with both solids and fluid in flow ·fluidized leaching and washing ·SOlids mixing and segregation ·operation of conical fluidized beds These problems arise in hydtaulic classification according to particle size and den$itv,sedimentation and classification,continuous ion exchange or adsorption,water treatment,fluid—bed electrolysis,and biochemical processes involving granular particles and supercritical extraction of solid materials. Professor Kwauk also expounds alternative bubbleless gas—SOlid contacting systems,e.g.,d讣ute raining particles,fast fluidization, shallow fluidized beds, and particles fluidized under the influence of oscillating flow--some of these techniques are already replacing their bubbling predecessors. He proposes further a method for assessing the fluidizing performance of powdeTS with a view to improving their gas-sohd contacting behavior in the direction of the idea“zed state through particle design. Youchu Li graduated from Tianjin University in 1 962 and was appointed to the Institute of Chemical Metallurgy(now Process Engineeting)of the Chinese Academy of Sciences. He is now a retired professor. As a researcher and director of the Fluidization Laboratory,he developed correlations for the dynamics of fast fluidization,multi—layer fluidized bed, gas—SOlid mixing,mass and heat transfer in fluidization,and he developed processes for magnetizing roasting of low- grade and complex iron ores。 calcination of non-metaUic ores,clean coal combustion and pyrolysis and preparation 0f various powdered functional materials. Professor Li received several awards from the State and the Chinese Academy of Scieaces,and he summaTized in 2008 his more than 40 years’R&D in fluidization in a monograph,“Introduction t0 Fluidization Process Engineering’’(in Chinese). In the present pub“cation,he contributed two addenda:one on recent studies on gas-solid flOW and applicatious of fast fluidization and the other on the more recent area of
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