Drag in Low-Re Polydisperse Gas-Solid Suspensions

Slides:



Advertisements
Similar presentations
Motion of particles trough fluids part 1
Advertisements

Motion of particles trough fluids part 2
Computer Simulations of Wind Tunnel Experiments
Analyzing the Results of a Simulation and Estimating Errors Jason Cooper.
Systems of magnetic dipolar particles with shifted dipoles Details to be found in the poster.
External Flow: Flow over Bluff Objects (Cylinders, Sphere, Packed Beds) and Impinging Jets.
©2002 Regents of University of Minnesota Fluidization of 1204 Spheres 1 Direct Numerical Simulation (DLM) of 1204 Spheres in a Slit Bed zSphere Diameter.
Continuous Time Monte Carlo and Driven Vortices in a Periodic Potential V. Gotcheva, Yanting Wang, Albert Wang and S. Teitel University of Rochester Lattice.
Chapter 7 Sections 7.4 through 7.8
Entrained Bed Reactor Quak Foo Lee Department of Chemical and Biological Engineering.
Fixed and Fluidized Beds
Two-fluid models for fluidized bed reactors: Latest trends and challenges Yassir Makkawi Chemical Engineering.
Engineering 1182 College of Engineering Engineering Education Innovation Center Solid Modeling Introduction Rev: , AJPSolid Modeling Introduction1.
Sampling and Measurement for Respirable Particulates.
Numerical Analysis of Flow and Mixing Phenomena of Municipal Solid Waste Particles on a Reverse Acting Grate Masato R. Nakamura, Marco J. Castaldi, and.
Generalized Indirect Fourier Transformation (GIFT) (see B. Weyerich, J. Brunner-Popela & O. Glatter, J. Appl. Cryst. (1999) 32, Small- angle scattering.
Minimum Fluidizing Velocities for Various Bed Packings By Andrew Maycock.
Lecture Objectives Unsteady State Simulation Example Modeling of PM.
FLOW THROUGH GRANULAR BEDS AND PACKED COLUMN
Actuated cilia regulate deposition of microscopic solid particles Rajat Ghosh and Alexander Alexeev George W. Woodruff School of Mechanical Engineering.
1 Characterizing Molecular Weight Brazel & Rosen Ch. 5 Number average molecular weight: M n.
Sediment Transport Modelling Lab. The Law of the Wall The law of the wall states that the average velocity of a turbulent flow at a certain point is proportional.
SOLID,LIQUID,GAS BY: Sajedah Ghizawi 6E. Solid Solid Is one of the three classical states of matter, the others being gas and liquid. Solid Is one of.
Fluid Mechanics, KU, 2007 Chap. 4: Flow of Particulates Dimensional analysis & experimentation Physical phenomena do not depend on the frame of reference.
New Topic P4 Simple kinetic molecular model of matter.
Heat Transfer in a Packed Bed Reactor with Downflow of Air and Water
1. Relative motion between a fluid and a single particle
On the understanding of self-assembly of anisotropic colloidal particles using computer simulation methods Nikoletta Pakalidou1✣ and Carlos Avendaño1 1.
TUTORIAL 3.
Chemical Engineering Department
2 Master of the Department of Civil Engineering, NTUT, Taipei, Taiwan.
Environmental Engineering Lecture Note Week 11 (Transport Processes)
Effects of Air Pressure and Wettability on Drop Impact on Dry Surfaces Taehun Lee, Department of Mechanical Engineering, City University of New York,
On the understanding of self-assembly of anisotropic colloidal particles using computer simulation methods Nikoletta Pakalidou1✣ and Carlos Avendaño1 1.
Chemical Engineering Explained
Combined Cycles Using Coal & Other Solid Fuels
Lecture Objectives Unsteady State Ventilation Modeling of PM.
Lecture Objectives Learn about particle dynamics modeling
STOICHIOMETRIC RELATIONS
Study of Hydrogen/Syngas Combustion and NO Emissions
Clarkson UNIVERSITY defy convention
Particle (s) motion.
MIT Microstructural Evolution in Materials 2: Solid Solutions
انواع المخاليط (التدريس الابداعي )
Drag laws for fluid-particle flows with particle size distribution
Jos Derksen & Radompon Sungkorn Chemical & Materials Engineering
Connecting Catalytic Chemistry to External Particle Conditions via CFD Anthony G. Dixon, Department of Chemical Engineering, Worcester Polytechnic Institute.
Department of Chemical Engineering
Controlling Segregation via Flow Perturbations and/or Cohesion Joseph J. McCarthy, Department of Chemical Engineering, University of Pittsburgh Alternatively,
DIMENSIONAL AND MODEL ANALYSIS
אביבה אלקלעי, ראש היחידה לכניסה להוראה, המכללה האקדמית אחווה
מהו הסטאז'? המכללה האקדמית תלפיות.
Fluidization Reading Materials: Perry’s Handbook, Chapter 17
Development of a Hybrid VOF/Level Set Technique to Model Two-Phase Flows Two-Phase Flow: Movement of any mixture of liquid and gas or two liquids Need.
Mechanical Separation
قوانين برگزاري مناقصات و آيين نامه مالي و معاملاتي دانشگاه علوم پزشكي و خدمات بهداشتي ،درماني تهران
7.2 Objectives Describe the formation of ionic bonds and the structure of ionic compounds. Generalize about the strength of ionic bonds based on the physical.
Lecture Objectives Ventilation Effectiveness, Thermal Comfort, and other CFD results representation Surface Radiation Models Particle modeling.
Just for Kicks: a Molecular Dynamics Simulation by Dino B.
Link the scientific word with its definition
Jan Genzer (Department of Chemical & Biomolecular Engineering)
Chapter 2 Matter and Change 2.1 Properties of Matter 2.2 Mixtures
What is a Mixture? A mixture is a combination of 2 or more substances that have not been chemically bonded (no chemical reaction occurred)
Fluids and pressure.
Fixed and Fluidized Beds
Module 2 States of Matter with Properties
Drag in Polydisperse Gas-Solid Suspensions
Types of Errors And Error Analysis.
Effect of Elevated Pressure on the Rheology, Vitrification, and Aging of Nearly Hard Colloidal Spheres J. J. Magda & M. Alcoutlabi, Department of Chemical.
Energy and Matter.
Presentation transcript:

Drag in Low-Re Polydisperse Gas-Solid Suspensions Sankaran Sundaresan, Chemical Engineering Department, Princeton University Princeton, NJ 08648 Computationally generated drag correlations are available for monodisperse suspensions, but not for fixed beds and suspensions containing particles of different sizes. We use lattice-Boltzmann method to simulate low-Re flow in binary assemblies of spherical particles and characterize the drag forces. Fixed beds: Suspensions: Average error: 13% Average error: 3.9% In the next year, we will study the drag forces in suspensions with finite Reynolds numbers.