Electrodes of heater are perforated - cross flow from lateral channels should improve uniformity of temperatures in central channel. However, R.Žitný,

Slides:



Advertisements
Similar presentations
Heat Transfer/Heat Exchanger
Advertisements

Introduction to Plasma-Surface Interactions Lecture 6 Divertors.
Lesson 17 HEAT GENERATION
FEMLAB Conference Stockholm 2005 UNIVERSITY OF CATANIA Department of Industrial and Mechanical Engineering Authors : M. ALECCI, G. CAMMARATA, G. PETRONE.
On-Set of EHD Turbulence for Cylinder in Cross Flow Under Corona Discharges J.S. Chang, D. Brocilo, K. Urashima Dept. of Engineering Physics, McMaster.
Foundations for Heat Exchanger Development P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Understand the Concept to Know Better.
Momentum Heat Mass Transfer
Analysis of Simple Cases in Heat Transfer P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Gaining Experience !!!
The geometry of capillary columns is fairly simple, consisting of length, internal diameter, and stationary phase thickness. Nevertheless, there are endless.
Foam Enhancement of sweep in Fracture System Wei Yan George J. Hirasaki Clarence A. Miller Chemical Engineering Department, Rice University.
Fluid Dynamics.
Experimental Verification of Gas- Cooled T-Tube Divertor Performance L. Crosatti, D. Sadowski, S. Abdel-Khalik, and M. Yoda ARIES Meeting, UCSD (June 14-15,
A Study of Fluid Flow and Heat Transfer in a Liquid Metal in a Backward-Facing Step under Combined Electric and Magnetic Fields E. Gutierrez-Miravete and.
University of South Carolina FCR Laboratory Dept. of Chemical Engineering By W. K. Lee, S. Shimpalee, J. Glandt and J. W. Van Zee Fuel Cell Research Laboratory.
CHE/ME 109 Heat Transfer in Electronics LECTURE 8 – SPECIFIC CONDUCTION MODELS.
P M V Subbarao Professor Mechanical Engineering Department I I T Delhi
One Dimensional Polar Geometries For Conduction with Heat Generation P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A.
Computation of FREE CONVECTION P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Quantification of Free …….
Chapter 7 Sections 7.4 through 7.8
Writing Technical Reports A technical report is used to convey important findings or test results to a controlled audience. A technical report is used.
Momentum Heat Mass Transfer
Design Analysis of Plate Heat Exchangers
RTD and FLOWs at steady and pulsatile flow in systemic circulation
Enhancement of Heat Transfer P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Invention of Compact Heat Transfer Devices……
Chapters Thermodynamics Introduction 1. Equilibrium of mechanical systems: the concept of temperature Three parameters were needed to describe the.
OCT , 2006 COMSOL USERS CONF BOSTON, MA 1 Use of COMSOL Multiphysics for Optimization of an All Liquid PEM Fuel Cell MEA George H. Miley (Speaker),
Electrohydrodynamics Laboratory Y. Feng and J. Yagoobi Heat Transfer Enhancement and Two-Phase.
1 Liquid-crystal thermography method for the study of stages of instability developing in the cross- flow on the leading edge of the oblique wing Tolkachev.
20 th June 20111Enrico Da Riva, V. Rao Project Request and Geometry constraints June 20 th 2011 Bdg 298 Enrico Da Riva,Vinod Singh Rao CFD GTK.
One Dimensional Non-Homogeneous Conduction Equation P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A truly non-homogeneous.
CHROMATOGRAPHY Chromatography basically involves the separation of mixtures due to differences in the distribution coefficient.
Analytical Modeling of Forced Convection in Slotted Plate Fin Heat Sinks P. Teertstra, J. R. Culham & M. M. Yovanovich Microelectronics Heat Transfer Laboratory.
SAHPA ® South African Heat Pipe Association Energy Postgraduate Conference EPC2013, Aug 2013 iThemba LABS EPC Investigating Instabilities.
R.Žitný, J.Thýn Department of Process Engineering CTU in Prague, Faculty of Mechanical Engineering Acknowledgement: Research.
One-Dimensional Steady-State Conduction
Order of Magnitude Scaling of Complex Engineering Problems Patricio F. Mendez Thomas W. Eagar May 14 th, 1999.
Convective heat exchange within a compact heat exchanger EGEE 520 Instructor: Dr. Derek Elsworth Student: Ana Nedeljkovic-Davidovic 2005.
INTRODUCTION Many heat and mass transfer processes in column apparatuses may be described by the convection – diffusion equation with a volume reaction.
E3 Teacher Summer Research Program. Willie L. Smith - IPC, Physics Tidehaven ISD Tidehaven High School.
Convection in Flat Plate Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A Universal Similarity Law ……
Mitglied der Helmholtz-Gemeinschaft Jörg Wolters, Michael Butzek Focused Cross Flow LBE Target for ESS 4th HPTW, Malmö, 3 May 2011.
Kinetics and Reactor Design Kinetics and Reactor Design CHE-402 INSTRUCTOR: Dr. Nabeel Salim Abo-Ghander Chemical Reactions and Rate of Reactions Chapter.
Air filmcooling through laser drilled nozzles STW project CASA-dag
1 Control of maldistribution of flow in parallell heat exchangers Magnus G. Jacobsen, Sigurd Skogestad Nordic Process Controi workshop, Porsgrunn
Dynamic visualisation of the combustion processes in boilers Marek Gayer Computer Graphics Group Department of Computer Science and.
Chapter Three Sections 3.1 through 3.4
Convection Heat Transfer in Manufacturing Processes P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Mode of Heat Transfer due to.
Professor: Eduardo Cabrera Thermal Engineering Laboratory
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 6 Introduction to convection.
CONVECTION : An Activity at Solid Boundary P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Identify and Compute Gradients.
Professor Eduardo Cabrera
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 11 Heat Exchangers.
Chapter 8: Internal Forced Convection
EXAMPLE OF REDUCED CRYOMODULE HEAT CAPACITY DUE TO HELIUM PRESSURE RETURN LEVELS 0L04 CASE HISTORY.
CFD Simulation & Consulting Services Hi-Tech CFD | Voice: Optimizing Designs of Industrial Pipes, Ducts and.
Copyright INVESTIGATION THE FLOW BEHAVIOR OF CONTINUOUS PULPING DIGESTER USING RADIOTRACER TECHNIQUE TO OPTIMIZE THE OPERATING CONDITIONS (Paper.
The 3 Types of Heat Transfer
Thermag VII, Turin, Italy
Unit 42: Heat Transfer and Combustion
EXTENDED SURFACE HEAT TRANSFER EXPERIMENT
Date of download: 11/9/2017 Copyright © ASME. All rights reserved.
Design Analysis of Plate Heat Exchangers
Analysis of the Simplest Flow
ELECTRODE ARRANGEMENT IMPACT ON HEAT TRANSFER IN HORIZONTAL CHANNELS
R.Žitný, J.Thýn Czech Technical University in Prague
Experimental techniques of the study of vortex structures caused by point injection on the leading edge of the oblique wing Tolkachev S.N. Gorev V.N. Zharkova.
Heat Exchange in Condensing Systems James DiLiegro, Donatus Obot-Etiebet, Katherine Pavlik Department of Chemical Engineering, University of New Hampshire.
P M V Subbarao Professor Mechanical Engineering Department I I T Delhi
12. Heat Exchangers Chemical engineering 170.
National Chung Cheng University
Presentation transcript:

Electrodes of heater are perforated - cross flow from lateral channels should improve uniformity of temperatures in central channel. However, R.Žitný, J.Thýn Department of Process Engineering CTU in Prague, Faculty of Mechanical Engineering Acknowledgement: Research is subsidized by J04/98: EXPERIMENTAL SET-UP DIRECT OHMIC HEATER Problem: Parallel flows are typical for many apparatuses of process industries, e.g. shell&tube or plate heat exchangers, heaters, reactors. Sometimes instabilities or just only non-uniform distribution of flow in parallel channels occur if the apparatus operates at non-isothermal conditions. Parallel flow instabilities have been observed also in lateral channels of ohmic heater. One parallel stream is delayed or even stopped if the temperature increase is too high. Cross-flow through perforation of electrodes is also suppressed. These unpleasant effects are caused by natural convection. Mathematical description Theoretical analysis predicts two solutions of temperature and flow-fields:  Symmetric solution (flow-rates and temperatures in lateral channels are equal)  Asymmetric solution exists within a certain range of flow-rates and heating power. Asymmetric solution can be interpreted as a magnitude of disturbance causing instability of flow. Mathematical model enables to identify parameters having significant influence upon the stability limits, e.g. width of lateral channels. Experiments: Stimulus - response technique (injection of a tracer and measurement responses) has proved to be useful for detection of cross-flow. As tracers KCl (conductivity method), KMnO 4 (visualisation), Tc99 (radioisotope) were used. Conductivity method is superior at isothermal flows, while radioisotopes are better when the liquid is heated (KCl solution increases conductivity and therefore electric power). Asymmetries of flow are better observed by thermometers arranged along the lateral channels. Experiments were performed for 3 different widths of lateral channels (18, 10, 7.5 mm), full and perforated electrodes, flow-rates ml/s, heating power kW. Conclusions: Control volume model of natural convection can describe asymmetry and instability of parallel flow. Instabilities depend upon flow-rate, power, geometry and can be suppressed by narrowing lateral channels. Model and experiments predict that the cross-flow is suppressed (or even reversed) at non-isothermal flow. 15 x 21 Impulse response measured by conductivy method (KCl) radioisopes (Tc 99) Temperatures measured by 12 Pt100 thermometers Fast optical probes ReFlex H L Warm liquid (T e ) stands in the right channel if p 1 -p 0 =  0 gL[1-  (T e -T 0 )] T 0,p 0,Q Control volumes are characterised by: parabolic velocity profile linear increase of temperature residence times - serie of mixers Linear relationship between pressure drop and flow-rate through slits in electrodes Mass balances Heat transfer Momentum Tracer balances Narrow lateral channels increase cross-flow, but only at isothermal flow Cross-flow is lower for wide lateral channels.