Handbook of Conveying and Handling of Particulate Solids
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Handbook of Conveying and Handling of Particulate Solids

  1. 870 pages
  2. English
  3. ePUB (mobile friendly)
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eBook - ePub

Handbook of Conveying and Handling of Particulate Solids

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About This Book

This handbook presents comprehensive coverage of the technology for conveying and handling particulate solids. Each chapter covers a different topic and contains both fundamentals and applications. Usually, each chapter, or a topic within a chapter, starts with one of the review papers. Chapter 1 covers the characterization of the particulate materials. Chapter 2 covers the behaviour of particulate materials during storage, and presents recent developments in storage and feeders design and performance. Chapter 3 presents fundamental studies of particulate flow, while Chapters 4 and 5 present transport solutions, and the pitfalls of pneumatic, slurry, and capsule conveying. Chapters 6, 7 and 8 cover both the fundamentals and development of processes for particulate solids, starting from fluidisation and drying, segregation and mixing, and size-reduction and enlargement. Chapter 9 presents environmental aspects and the classification of the particulate materials after they have been handled by one of the above-mentioned processes. Finally, Chapter 10 covers applications and developments of measurement techniques that are the heart of the analysis of any conveying or handling system.

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DEM simulation of industrial issues in fluidized bed reactors

M. Horio a
S. Kajikawa b
aDept. Chemical Engineering, Graduate School BASE, Tokyo University of A&T, Koganei, Tokyo, 184-8588 Japan.
bDMaterial Science Lab., Mitsui Chemicals, Inc., Sodegaura, Chiba 299-0125.
Simulation issues on fluidized beds are discussed from both industrial and academic viewpoints. Some state of arts of DEM simulation is reviewed focusing on agglomerating fluidization, high temperature and pressurized reactor operations. For the future investigation, research needs are discussed.

1 INTRODUCTION

In industrial fluidized beds, engineers always face problems associated with agglomeration, sintering, attrition and/or erosion. These factors can be closely related to both surface characteristics and the dynamic motion of particles in the bed. Engineers who want to reduce risks in the developments of particulate processes have to choose a simulation engine that is capable of taking into account the trouble causing factors. This is why the author’s group (since Mikami et al. [1]) decided to get involved, not very much in the TFM (Two Fluid Model), but in the DEM (Discrete Element Method) modeling. Table 1 summarizes these models and numerical codes available at present. TFM is the most macroscopic and of a largest capacity model that still can simulate bubbles. In the TFM the stress tensor has to be determined by either experimentally or theoretically. The kinetic theory provides a theoretical foundation for the tensor but even for the simplest case of uniformly sized non-cohesive particles, there have been several different expressions. As Witt and Perry [2] demonstrated, depending on the difference schemes, different bubble shapes can be obtained due to numerical diffusion and other effects. For more realistic cases with cohesive interaction and/or particles of a wide size distribution, TFM tend to loose its capability. On the contrary DEM is able to take into account those trouble-causing factors directly. However, DEM also faces serious difficulties concerning the total operable number of particles as well as those phenomena that require detailed information in the vicinity of particles, such as heat transfer and the lubrication effects.
Table 1
Numerical Fluidized Bed Models and Codes
image
Balzer, G., A. Boelle and O. Simonin, Fluidization VIII, ed. by J.F. Large and C. Laguerie, AIChE, 409–418 (1996) Cundall P.A. and O.D.L. Struck Geotechnique, 29, 47–65(1979) Ding, J., and D. Gidaspow, AIChE J, 36, 523–538 (1990) Feng, J., P.Y. Huang and D.D, Joseph, J. Fluid Mech., 63, 63–88(1996) Gidaspow, D., and B. Ettehadieh, I&EC Fund., 22, 193–201(1983) Huang, P.Y., J. Feng, H.H. Hu and D.D, Joseph, J. Fluid Mech., 343, 73–94 (1997) Ichiki, K., and H. Hayakawa, Phys. Rev. E, 52, 658–670(1995) Kuipers, W.J. Briels and W.P.M. van Swaaij, Chem. Eng. Sci., 51, 99- (1996) Pritchett, J.W., T.R. Blake and S.K. Garg, AIChE Symp. Ser., 74, 134–148 (1978) Sinclair, J.L., and R. Jackson, AIChE J., 35, 1473 (1989) Syamlal, M., W. Rogers and T. J. O’Brien, MFIX Docummentation, Theory Guide, US DOE Technical Note, US DOE/METC-94/1004 (DE94000087) (1993) Tanaka, Yonemura and Tsuji, Nihonkikaigakkaironbunshuu (Ser.B) 59, No.565, 2982–2989(1993) Yu, Nohara, Umekage, Nihonkikaigakkaironbunshuu (Ser.B) 62, No.601, 3300...

Table of contents

  1. Cover image
  2. Title page
  3. Table of Contents
  4. Handbook of Powder Technology
  5. Front Matter
  6. Copyright page
  7. Preface
  8. Solids flowability measurement and interpretation in industry
  9. Flow properties of bulk solids -which properties for which application
  10. Investigation on the effect of filling procedures on testing of flow properties by means of a uniaxial tester
  11. Characterization of powder flow behavior with the Flexible Wall Biaxial Tester
  12. From discrete element simulations towards a continuum description of particulate solids
  13. Vibrational flow of cohesive powders
  14. Influence of the stress history on the time dependent behaviour of bulk solids
  15. Evaluation of the mechanical properties of powder for storage
  16. Particle adhesion and powder flow behaviour
  17. Determination of the influence of surface coating and particle size on flow properties of organic pigment powders
  18. The conversion of the analytical simple shear model for the Jenike failure locus into principal stress space and implication of the model for hopper design
  19. Modelling flooding in a small vessel compared with experiments and numerical calculation
  20. Analysis and application of powder compaction diagrams
  21. Axial porosity distribution in a packed bed of deformable particles: A numerical study based on DEM
  22. Flow properties of bulk solids and their use in solving industrial problems
  23. Silo failures: case histories and lessons learned
  24. The relationship between flow behaviour in a plane flow hopper and the jenike design method
  25. Full scale silo tests and numerical simulations of the „cone in cone” concept for mass flow
  26. Stress condition of sliding bulk solids on silo walls
  27. Studies on thermal actions and forces in cylindrical storage silo bins
  28. Silo discharge: Dynamic effects of granular flow
  29. Recent developments in feeder design and performance
  30. Recent developments in belt conveying - bulk solid and conveyor belt interactions
  31. Putting the pedal to the metal
  32. Mesoscopic nature of granular flows
  33. Using a kinetic theory approach incorporating interaction with the air to model granular flow down a chute
  34. Numerical and experimental studies for the impact of projectiles on granular materials
  35. Implementation of 3D frictional contact condition
  36. Numerical simulation of 3D iron ore flow
  37. Pneumatic conveying: transport solutions, pitfalls, and measurements
  38. Dilute-phase pneumatic conveying problems and solutions
  39. Latest development of the direct technique for measurement of the pneumatic conveying characteristics of bulk materials
  40. Dense phase (plug) conveying – observations and projections
  41. Operating limits of low-velocity pneumatic conveying
  42. Granular jump in low velocity pneumatic conveying of solid particles in a horizontal pipeline
  43. Two-layer model for non-suspension gas-solids flow of fine powders in pipes
  44. Pressure drop prediction of low-velocity slug-flow materials in the unstable zone
  45. Transportation boundaries for horizontal slug-flow pneumatic conveying
  46. The use of high pressure blow tanks for the pneumatic conveying of pelletised materials
  47. Pneumatic conveying with TurbuflowÂŽ-advantages against conventional dense phase conveying
  48. The influence of a bend on the flow characteristics in pneumatic conveying systems
  49. A novel analytical model for the acceleration of particles following bends in pneumatic conveying systems
  50. The design of pipeline systems for transporting ice into deep mines
  51. Experimental studies on pneumatic conveying of wet snow
  52. Deposition velocities for slurry flows
  53. Particle motion in sheared non-Newtonian media
  54. Distribution and friction of particles in pipeline flow of sand-water mixtures
  55. Laminar and turbulent flow of dense kaolin and ash hydromixtures 
  56. Rheological characterization of industrial kaolin slurries
  57. Net positive suction head requirement for centrifugal slurry pumps
  58. Slurry and tip clearance effects on the performance of an open impeller centrifugal pump
  59. Pneumatic capsule pipelines in Japan and future developments
  60. Drag reduction in hydraulic capsule pipeline
  61. A contribution to hydrotransport of capsules in bend and inclined pipeline sections 
  62. Recent developments in the drying technologies for the production of particulate materials
  63. DEM simulation of industrial issues in fluidized bed reactors
  64. Rheologic and flow properties of fluidised bulk solids
  65. Drying kinetics simulation by means of artificial neural networks
  66. Production of powder-like material from suspension by drying on inert particles
  67. Segregation of powders - mechanisms, processes and counteraction
  68. Countering segregation
  69. An investigation of degradation and segregation in typical coal handling processes
  70. A system for the reduction of air current segregation in silos
  71. Segregation-free particle mixing
  72. Bulk-solids mixing: overview
  73. A double stochastic model of the mixing of solid particles
  74. Investigation of flow regimes in continuous mixer tubes
  75. Description of grinding in a ball mill using statistical moments
  76. A Markov chain model to describe the Residence Time Distribution in a stirred bead mill
  77. Simulation of interaction of opposed gas-particle jets
  78. Simulation of gas-particle flows in jet-vortex mills
  79. Contribution to the theory of roll press design
  80. Drum granulation conditions for raw material with different particle size distributions
  81. Fugitive and non-fugitive dust generation and control in eonveying of powders: reality, technology and human attitude
  82. Evaluation of air pollution level by means of artificial neural network - multilayer perceptron
  83. Dust explosion hazard considerations for materials handling plants
  84. A de-dusting device for removing fines from pellets and granules
  85. Assessment of a multistage gravity separation in turbulent air flow
  86. TriboMechanical classification: A new technology for size classification of bulk powders
  87. Particle surface inspection with Fourier-wavelets transform
  88. The crucial role of on-line measurement in bulk solids handling
  89. Application of non-invasive techniques for imaging fluidized beds – A review
  90. Electrical tomography techniques for multiphase flow applications
  91. Sedimentation kinetics monitor
  92. Effect of mass loading on gas-solids motion and particle segregation patterns
  93. Measurement of the dynamic behavior of bulk solids using optical flow analysis