Electrohydrodynamics Laboratory + - + + + + + + + + + + + + + + - - - - - - - - - - - - - - Y. Feng and J. Yagoobi Heat Transfer Enhancement and Two-Phase.

Slides:

Advertisements

Similar presentations

Boiling heat transfer of liquid nitrogen in the presence of electric fields P Wang, P L Lewin, D J Swaffield and G Chen University of Southampton, Southampton,

Advertisements

Using Heat Chapter 16.3.

Erik Björk, M.Sc. Dept. of Energy Technology Div. of Applied Thermodynamics and Refrigeration Royal Institute of Technology Sweden Effektivare kylsystem.

The First Law of Thermodynamics

ENGR 2213 Thermodynamics F. C. Lai School of Aerospace and Mechanical Engineering University of Oklahoma.

Electro-Hydro-Dynamics Enhancement of Multi-phase Heat Transfer

Section 16.3 Using Heat.

ENGR 2213 Thermodynamics F. C. Lai School of Aerospace and Mechanical

1 Dept. of Energy Technology, Div. of Applied Thermodynamics and Refrigeration Tube diameter influence on heat exchanger performance and design. Single.

Two-Phase Heat Transfer Laboratory Texas A&M University Experimental Study of Condensation on Micro Grooved Plates R. Barron-jimenez, H. Y. Hu, G. P. Peterson.

080125© M. Kostic Prof. M. Kostic Mechanical Engineering NORTHERN ILLINOIS UNIVERSITY Effective Thermal Conductivity Errors by Assuming Unidirectional.

Department of Mechanical Engineering ME 322 – Mechanical Engineering Thermodynamics Lecture 29 The Vapor Compression Refrigeration (VCR) Cycle.

EGR 334 Thermodynamics Chapter 4: Section 9-10

Meshal Khaled Al-Saeed Dr. Malik Al-Ahmad

Power Generation Cycles Vapor Power Generation The Rankine Cycle

By: Reuben Downs Faculty Advisor: Dr. Darin Nutter Graduate Student Advisor: Wei Guo.

An OHP consists of a capillary sized tube and a refrigerant. Most OHPs are formed in closed serpentine loops with multiple turns, but OHPs can operate.

Pacific School Of Engineering. Guided By:- Asst.Prof.Vatsal patel Submitted by:-  Kotadiya Reshma :  Ladva Piyush : 

HEAT EXCHANGER.

Refrigeration Basics 101.

STEAM TURBINE POWER CYCLES. The vast majority of electrical generating plants are variations of vapour power plants in which water is the working fluid.

Oceanic Thermal Energy Conversions Group Members: Brooks Collins Kirby Little Chris Petys Craig Testa.

So Far: Conservation of Mass and Energy Pressure Drop in Pipes Flow Measurement Instruments Flow Control (Valves) Types of Pumps and Pump Sizing This Week:

ENGR 2213 Thermodynamics F. C. Lai School of Aerospace and Mechanical Engineering University of Oklahoma.

1 FUNDAMENTAL PRINCIPALS OF In Situ THERMAL TREATMENT Professor Kent S. Udell Department of Mechanical Engineering Department of Civil and Environmental.

THERMAL ENERGY By Hannah Pelayic 1 st hour Picture of a solar flair.

REFRIGERATION SYSTEMS

Section 3 Using Heat.

Refrigeration Cycles (YAC: 7-13 trough 7-16)

Heat Transfer Equations For “thin walled” tubes, A i = A o.

Refrigeration Cycles A Carnot cycle in reverse QL QH T s 2

ENGR 2213 Thermodynamics F. C. Lai School of Aerospace and Mechanical Engineering University of Oklahoma.

1 Second Law of Thermodynamics Engines and Refrigerators.

Analysis of Flow Boiling

FORMS OF HEAT TRANSFER. CONDUCTION CONVECTION.

“The more we use renewable energy, the more we benefit the environment, strengthen our energy security, create jobs locally, and help improve our economy.

MULTI-COMPONENT FUEL VAPORIZATION IN A SIMULATED AIRCRAFT FUEL TANK C. E. Polymeropoulos Department of Mechanical and Aerospace Engineering, Rutgers University.

ENGR 2213 Thermodynamics F. C. Lai School of Aerospace and Mechanical Engineering University of Oklahoma.

Investigation of Thin Film Evaporation Limit in Single Screen Mesh Layers Presented to IMECE 2002 Nov. 19, 2002, New Orleans, LA Yaxiong Wang & G.P. “Bud”

Superheat Rankine Cycle Example Turbine pump condenser Q out Q in W out W in boiler Consider the superheat Rankine power cycle as we analyzed before.

Experiment 6: Rankine Cycle Yvette Triay Reporter Group 3.

Aachen Status Report: CO 2 Cooling for the CMS Tracker at SLHC Lutz Feld, Waclaw Karpinski, Jennifer Merz and Michael Wlochal RWTH Aachen University, 1.

Insulators vs. Conductors Conductors transfer thermal energy rapidly (metals) Insulators reduce the transfer of thermal energy (wood, foam) Insulation.

Heat Transfer by Convection

Refrigeration What's Refrigerated? What makes up a system?

Using Heat Part 2. Science Journal Entry 32 Explain the advantages and disadvantages of thermal expansion.

Continuous Sorption Cooling in Activated Carbon-Nitrogen Using Metal Foam as Regenerator Indranil Ghosh Cryogenic Engineering Centre, IIT Kharagpur ICEC.

Chem. Eng. Thermodynamics (TKK-2137) 14/15 Semester 3 Instructor: Rama Oktavian Office Hr.: M.13-15, Tu , W ,

Date of download: 6/3/2016 Copyright © ASME. All rights reserved. From: Review and Advances in Heat Pipe Science and Technology J. Heat Transfer. 2012;134(12):

Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 11 Heat Exchangers.

1 Julien Ramousse, Kodjo Agbossou, Yves Dubé and Pélopé Adzakpa Hydrogen Research Institute (IRH), Université du Québec à Trois-Rivières, C.P. 500, Trois-Rivières,

The Innovative Design of Piezoelectric Heat Pipe Generator Professor: David. T. W. Lin J.C. Hsieh Student: Cheng-Feng Shen 1.

Chapter 12B: PROPERTY TABLES, REFRIGERATION CYCLES AND HX 1) Boiling of pure substances: water and steam tables 2) Refrigerant tables 3) Binary mixtures.

Date of download: 10/2/2017 Copyright © ASME. All rights reserved.

Date of download: 10/10/2017 Copyright © ASME. All rights reserved.

Ocean Thermal Energy Conversion activities at Process & Energy

Net Power Production of a Heat Engine

Orientation Effects on Flow Boiling Silicon Nanowire Microchannels

SNS COLLEGE OF ENGINEERING Coimbatore-107 Subject: Thermal Engineering

Power and Refrigeration Systems

Energy- and mass flows in cooling and in heat pumps

Aachen Status Report: CO2 Cooling for the CMS Tracker at SLHC

The Basic Direct Expansion Refrigeration Cycle

Leonard Vasiliev, Alexander Zhuravlyov and Alexander Shapovalov

Second Law of Thermodynamics Engines and Refrigerators

Chapter 2 Energy Transfer by Heat, Work & Mass

Boiling is a liquid-to-vapor phase change process just like evaporation, but there are significant differences between the two. Evaporation occurs at.

Condensation in mini- and microchannels

Chapter 5-3 Using Thermal Energy.

Presentation transcript:

Electrohydrodynamics Laboratory Y. Feng and J. Yagoobi Heat Transfer Enhancement and Two-Phase Flow Laboratory Mechanical, Materials, and Aerospace Engr. Dept. Illinois Institute of Technology Chicago, USA Control of Liquid and Liquid/Vapor Flow Distributions With EHD Conduction Pumping

Electrohydrodynamics Laboratory thermal management of parallel evaporators and condensers correct liquid distribution required among parallel lines local hot areas and dry-outs due to mal- distribution EHD pumping as an active control method conduction pumping, a right choice Motivation

Electrohydrodynamics Laboratory EHD Conduction Pump Electrode Design Schematic

Electrohydrodynamics Laboratory Electrode Picture

Electrohydrodynamics Laboratory Working Fluid, R-123    e (S/m)  (m 2 /V. s) E-84.8E-8  (Pa. s)  (kg/m 3 ) h fg (kJ/kg) 417.6E

Electrohydrodynamics Laboratory Pressure Generation in the Absence of a Net Flow

Electrohydrodynamics Laboratory EHD Conduction Pump with Three Electrode Pairs

Electrohydrodynamics Laboratory Flow Distribution Control Apparatus Utilizing EHD Conduction Pump

Electrohydrodynamics Laboratory Experimental Results – Liquid Phase (mass flux = 100 kg/m 2 s, T = 25  C)

Electrohydrodynamics Laboratory Flow Distribution,  e = 10 kV

Electrohydrodynamics Laboratory Current Consumption,  e = 10 kV

Electrohydrodynamics Laboratory Flow Distribution,  e = 15 kV

Electrohydrodynamics Laboratory Current Consumption,  e = 15 kV

Electrohydrodynamics Laboratory Experimental Results – Liquid/Vapor Phases (mass flux = 50 kg/m 2 s, T sat = 25  C)

Electrohydrodynamics Laboratory Pressure Drop Along EHD Conduction Pump and Branch Tube, Vapor Quality = 6%

Electrohydrodynamics Laboratory Pressure Drop Along the Other Branch Tube, Vapor Quality = 6%

Electrohydrodynamics Laboratory Pressure Drop Along EHD Conduction Pump and Branch Tube, Vapor Quality = 20%

Electrohydrodynamics Laboratory Pressure Drop Along the Other Branch Tube, Vapor Quality = 20%

Electrohydrodynamics Laboratory Pressure Drop Along EHD Conduction Pump and Branch Tube, Vapor Quality = 26%

Electrohydrodynamics Laboratory Pressure Drop Along the Other Branch Tube, Vapor Quality = 26%

Electrohydrodynamics Laboratory Conclusions Electrically driven flow generated by the EHD conduction pump successfully controlled the flow distribution between two parallel branch lines.

Electrohydrodynamics Laboratory Acknowledgement American Society of Heating, Refrigerating and Air Conditioning Engineers.