Results Conclusion C Results CFD study on heat transfer and pressure drop characteristics of an offset strip-fin heat exchanger in helium systems Objectives.

Slides:



Advertisements
Similar presentations
Master’s Dissertation Defense Carlos M. Teixeira Supervisors: Prof. José Carlos Lopes Eng. Matthieu Rolland Direct Numerical Simulation of Fixed-Bed Reactors:
Advertisements

University of Western Ontario
VISCOUS CFD ANALYSIS OF GENERIC MISSILE WITH GRID FINS By Swapnil. D
Kern’s Description of Shell Side Flow in SHELL-AND-TUBE HEAT EXCHANGER P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Another.
Chapter 4.2: Flow Across a Tube Bundle Heat Exchanger (Tube Bank)
Chapter 3.2: Heat Exchanger Analysis Using -NTU method
AIR FLOW IN DUCTS Shaharin Anwar Sulaiman
Who Wants to Be a CFD Expert? In the ME 566 course title, CFD for Engineering Design, what does the acronym CFD stand for? A.Car Free Day B.Cash Flow Diagram.
Internal Convection: Fully Developed Flow
Experimental and Numerical Study of the Effect of Geometric Parameters on Liquid Single-Phase Pressure Drop in Micro- Scale Pin-Fin Arrays Valerie Pezzullo,
Internal Flow: Heat Transfer Correlations
1 Dept. of Energy Technology, Div. of Applied Thermodynamics and Refrigeration Tube diameter influence on heat exchanger performance and design. Single.
Jennifer Tansey 12/15/11. Introduction / Background A common type of condenser used in steam plants is a horizontal, two- pass condenser Steam enters.
Wind Chill Factor Regie Hyppolite and Justin Hyatt.
Monroe L. Weber-Shirk S chool of Civil and Environmental Engineering Manifold Hydraulics Cayuga Lake Ithaca WWTP Outfall Cayuga Lake Ithaca WWTP Outfall.
Engineering H191 - Drafting / CAD The Ohio State University Gateway Engineering Education Coalition Lab 4P. 1Autumn Quarter Transport Phenomena Lab 4.
MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 9: FLOWS IN PIPE
Closure of Kern’s Method
Kern’s Description of Shell Side Flow in SHELL-AND-TUBE HEAT EXCHANGER
Correlations for INTERNAL CONVECTION P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Essential Part of Exchanging Heat……..
Cayuga Lake Ithaca WWTP Outfall
EdF meeting 18 May 2009 Review of all the work done under the framework of Code_Saturne by S. Rolfo School of Mechanical, Aerospace & Civil Engineering.
Kern Method of SHELL-AND-TUBE HEAT EXCHANGER Analysis
Hydraulic Analysis of STHE Using Bell Delaware Method
Thermo-economic Optimization of STHE P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Minimizing capital and operating costs of shell.
Results Conclusion Methods Application of plate-fin heat exchangers with different UAs for mitigating the effects of pulsed heat load Objectives Background.
Chapter 4.3: Compact Heat Exchangers
Stable Running Result of the Refrigerator FB41 Digital Controller in PLC S7-300 The Research of PID Control in a Large Scale Helium Refrigerator Objectives.
ME421 Heat Exchanger and Steam Generator Design Lecture Notes 6 Double-Pipe Heat Exchangers.
Numerical and Experimental Study on Bed-to-Wall Heat Transfer in Conical Fluidized Bed Reactor 17 th International Conference on Mechatronics, Electrical.
1 Calorimeter Thermal Analysis with Increased Heat Loads September 28, 2009.
Experiment 5 Pipe Flow-Major and Minor losses ( review)
1 MER Design of Thermal Fluid Systems Project 3 Heat Exchanger Optimization Professor Anderson Spring 2012.
© 2011 Autodesk Freely licensed for use by educational institutions. Reuse and changes require a note indicating that content has been modified from the.
Quality of Curve Fitting P M V Subbarao Professor Mechanical Engineering Department Suitability of A Model to a Data Set…..
Bryan S. Wang 3S103 Chew Hanson 3S109 Lim Han Xin 3S119.
Double Pipe HEAT EXCHANGERS with Finned Inner Tube P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Ideas for Creation of Compact.
30 th June 20111Enrico Da Riva, V. Rao Parametric study using Empirical Results June 30 th 2011 Bdg 298 Enrico Da Riva,Vinod Singh Rao CFD GTK.
A WEIGHTED CALIBRATION METHOD OF INTERFEROMETRIC SAR DATA Yongfei Mao Maosheng Xiang Lideng Wei Daojing Li Bingchen Zhang Institute of Electronics, Chinese.
FLOW THROUGH GRANULAR BEDS AND PACKED COLUMN
Internal Flow: Heat Transfer Correlations. Fully Developed Flow Laminar Flow in a Circular Tube: The local Nusselt number is a constant throughout the.

Mike Cheadle PhD Graduate Student Mechanical Engineering Thesis: Determination of Oscillating Flow Heat Transfer and Hydrodynamic Parameters for a Cryogenic.
Indian Institute of Space Science and Technology STUDY OF EFFECT OF GAS INJECTION OVER A TORPEDO ON FLOW-FIELD USING CFD.
Thermal Considerations in a Pipe Flow (YAC: 10-1– 10-3; 10-6) Thermal conditions  Laminar or turbulent  Entrance flow and fully developed thermal condition.
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Internal Flow: Heat Transfer Correlations
First Law of Thermodynamics applied to Flow processes
Heat Transfer in a Packed Bed Reactor with Downflow of Air and Water
From: Hydraulic Loss of Finite Length Dividing Junctions
Gas bearing engineering design Optimization design method
Figure 1. Flow chart of the helium liquefier
Flow mal-distribution study in cryogenic counter-flow plate fin heat exchangers Geet Jain1, Sharad Chaudhary1, Prabhat Kumar Gupta2, P.K. Kush2 1Institue.
Simulation of Pipe Flow Using FlowLab 1.1 (PreLab 1)
超臨界CO2在增強型地熱系統儲集層中取熱之研究-子計畫三 CO2在增強型地熱系統取熱模型之建構及效能分析
Influence on the performance of cryogenic counter-flow heat exchangers due to longitudinal conduction, heat in-leak and property variations Qingfeng Jiang.
The inner flow analysis of the model
Revolutionizing heat transport enhancement with liquid metals: Proposal of a new industry of water-free heat exchangers Haiyan LI 1 ;Jing LIU 2 ; 1. Key.
Revolutionizing heat transport enhancement with liquid metals: Proposal of a new industry of water-free heat exchangers Haiyan LI 1 ;Jing LIU 2 ; 1. Key.
Extended Surface Heat Transfer
Chapter 5 The First Law of Thermodynamics for Opened Systems
Pipe Components, Piping System.
Simulation of turbulent airfoil Flow Using FlowLab 1.1 (CFD PreLab 2)
Comparison between Serrated & Notched Serrated Heat Exchanger Fin Performance Presented by NABILA RUBAIYA.
Andreas Gubner University of Applied Science Munich
Heat Transfer from Extended Surfaces (Fins)
Thermal behavior of the LHCb PS VFE Board
Air-conditioner -IDU Air-conditioner 2D Simplified model for Analysis.
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Introduction results Forced Convection Excel Linear Regression tool
Presentation transcript:

Results Conclusion C Results CFD study on heat transfer and pressure drop characteristics of an offset strip-fin heat exchanger in helium systems Objectives Background 1 Key Laboratory of Cryogenics, Technical Institute of Physics and Chemistry Chinese Academy of Sciences, Beijing ,China 2 State Key Laboratory of Technologies in Space Cryogenic Propellants,Technical Institute of Physics and Chemistry Chinese Academy of Sciences, Beijing ,China 3 University of Chinese Academy of Sciences, Beijing ,China Presented at the CEC/ICMC, 2015 June 28- July , Tucson Arizona; Session:C2PoG-Heat Exchangers; Program I.D. number: 86 Plate-fin heat exchanger is a kind of the compact heat exchangers, which has high coefficient of heat transfer and large specific surface. The offset strip fins are widely used in the large scale cryogenic helium plants to meet the demands for saving energy and sources. In dynamic simulation of the large scale helium cryogenic systems, the j and f factors are needed parameters. However, the current available correlations were obtained on the occasion that air was taken as heat transfer medium. Moreover, the correlations in the open literatures are quite different even with same Re and geometries of fins. Therefore, it’s necessary to derive the suitable correlations in helium systems.  The correlations for j and f factors of helium offset strip-fin heat exchanger had been developed by the multiple regression analysis, which can predict 90% simulation data within ±20% derivation.  The simulation results denoted that orthogonal experimental method was applicable in solving the heat transfer and fluid flow problems.  The comparison between the present and the open literatures’ correlations revealed that the fluid medium will affect the j and f factors.  The simulation results will provide a selection in the design and dynamic simulation of the offset strip fin heat exchangers in helium systems.  To obtain the suitable correlations of j and f factors used in helium offset strip – fin heat exchangers.  To verify the applicability of orthogonal experimental method in solving the heat transfer and fluid flow problems. Cui Lv 1,3, Jihao Wu 1,2, Qing Li 1,2, Xiujuan Xie 1,2 Lai Feng Li 1,2 and Huiming Liu 1 Contact information: Methods Usually, the fin-channel is assumed to be rectangular, and the fin offset is uniform and equal to half-fin spacing. The top view and axonometric drawing of the offset strip fins In order to neglect the entry effect, the model total length was chosen that the ratio of flow length to the hydraulic diameter was more than 60. Mesh independence and the model verification The pressure drop of model is tend to constant when the grid number is more than Hence, this grid number was chosen to calculate the j and f factors. The model verification used air as the heat transfer medium was carried out. The comparison between simulation results and the experimental data revealed that the maximum relative error of j and f factors were 9.1% and 17% respectively. The inner flow analysis of the model The characteristics of the inner flow of the model:  The inlet velocity increased when it passed the minimum cross-section.  The contour of velocity showed the periodicity until the ninth fin because of the entrance effect. The comparison between the regression data and the CFD results  The data in the orthogonal table was fitted by multiple regression method to derive the correlations of j and f factors. The comparison between present results and the available empirical correlations The trends between different correlations are same, this results can be proved that the orthogonal experimental method is the effective way to solve the multifactor problems of the thermodynamic filed. There exists difference between different correlations because the fin geometries used in the experiment and fluid medium were not same.  The orthogonal experimental design was used to reduce the number of the simulation.