The inner flow analysis of the model

Slides:



Advertisements
Similar presentations
Outline Overview of Pipe Flow CFD Process ANSYS Workbench
Advertisements

Convection in Flat Plate Turbulent Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Extra Effect For.
University of Western Ontario
Design Analysis of Plate Heat Exchangers
VISCOUS CFD ANALYSIS OF GENERIC MISSILE WITH GRID FINS By Swapnil. D
Computational Modeling of Flow over a Spillway In Vatnsfellsstífla Dam in Iceland Master’s Thesis Presentation Chalmers University of Technology 2007.
Chapter 4.2: Flow Across a Tube Bundle Heat Exchanger (Tube Bank)
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.
© 2011 Autodesk Freely licensed for use by educational institutions. Reuse and changes require a note indicating that content has been modified from the.
Computer Aided Thermal Fluid Analysis Lecture 10
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.
Monroe L. Weber-Shirk S chool of Civil and Environmental Engineering Manifold Hydraulics Cayuga Lake Ithaca WWTP Outfall Cayuga Lake Ithaca WWTP Outfall.
Design of Systems with INTERNAL CONVECTION P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Essential Part of Exchanging.
Anoop Samant Yanyan Zhang Saptarshi Basu Andres Chaparro
CHE/ME 109 Heat Transfer in Electronics LECTURE 17 – INTERNAL FORCED CONVECTION FUNDAMENTALS.
MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 9: FLOWS IN PIPE
Preliminary Assessment of Porous Gas-Cooled and Thin- Liquid-Protected Divertors S. I. Abdel-Khalik, S. Shin, and M. Yoda ARIES Meeting, UCSD (March 2004)
Correlations for INTERNAL CONVECTION P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Essential Part of Exchanging Heat……..
Hydraulic Analysis of STHE Using Bell Delaware Method
Chapter 7 Sections 7.4 through 7.8
Design Analysis of Plate Heat Exchangers
Results Conclusion Methods Application of plate-fin heat exchangers with different UAs for mitigating the effects of pulsed heat load Objectives Background.
Results Conclusion C Results CFD study on heat transfer and pressure drop characteristics of an offset strip-fin heat exchanger in helium systems Objectives.
ME421 Heat Exchanger and Steam Generator Design Lecture Notes 6 Double-Pipe Heat Exchangers.
1 Calorimeter Thermal Analysis with Increased Heat Loads September 28, 2009.
Experiment 5 Pipe Flow-Major and Minor losses ( review)
Pressure drop prediction models o Garimella et al. (2005) o Considered parameters o Single-phase pressure gradients o Martinelli parameter o Surface tension.
© 2011 Autodesk Freely licensed for use by educational institutions. Reuse and changes require a note indicating that content has been modified from the.
1 CHAPTER 6 HEAT TRANSFER IN CHANNEL FLOW 6.1 Introduction (1) Laminar vs. turbulent flow transition Reynolds number is where  D tube diameter  u mean.
Chapter 6 Introduction to Forced Convection:
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.
CLIC Prototype Test Module 0 Super Accelerating Structure Thermal Simulation Introduction Theoretical background on water and air cooling FEA Model Conclusions.
Convection: Internal Flow ( )
Convection in Flat Plate Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A Universal Similarity Law ……
Reynolds Analogy It can be shown that, under specific conditions (no external pressure gradient and Prandtle number equals to one), the momentum and heat.
Distributed Resistances and Fan Models Chapter 4.
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.
Pipe flow analysis.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 7 External flow.
Indian Institute of Space Science and Technology STUDY OF EFFECT OF GAS INJECTION OVER A TORPEDO ON FLOW-FIELD USING CFD.
CFD Simulation Investigation of Natural Gas Components through a Drilling Pipe RASEL A SULTAN HOUSSEMEDDINE LEULMI.
DCLL He Thermal Hydraulics Edward Marriott UW – Madison Mo Dagher UCLA Clement Wong General Atomics Presented at the FNST Meeting August 12-14, 2008, UCLA.
CFD Simulation & Consulting Services Hi-Tech CFD | Voice: Optimizing Designs of Industrial Pipes, Ducts and.
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: General Considerations. Entrance Conditions Must distinguish between entrance and fully developed regions. Hydrodynamic Effects: Assume.
KIT – University of the State of Baden-Wuerttemberg and National Research Center of the Helmholtz Association Institute for Technical Physics (ITEP), KIT.
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Internal Flow: Heat Transfer Correlations
Figure 1. Flow chart of the helium liquefier
Internal Convection: Overview
Chapter 8: Internal Flow
Numerical Investigation of Turbulent Flows Using k-epsilon
Influence on the performance of cryogenic counter-flow heat exchangers due to longitudinal conduction, heat in-leak and property variations Qingfeng Jiang.
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.
Date of download: 11/15/2017 Copyright © ASME. All rights reserved.
Pipe Components, Piping System.
Pressure drop prediction models
The application of an atmospheric boundary layer to evaluate truck aerodynamics in CFD “A solution for a real-world engineering problem” Ir. Niek van.
Comparison between Serrated & Notched Serrated Heat Exchanger Fin Performance Presented by NABILA RUBAIYA.
Step change in the boundary condition of conduction problems
Thermal behavior of the LHCb PS VFE Board
Internal Flow: General Considerations
Air-conditioner -IDU Air-conditioner 2D Simplified model for Analysis.
Heat Transfer Correlations for Internal Flow
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Presentation transcript:

The inner flow analysis of the model CFD study on heat transfer and pressure drop characteristics of offset strip-fin heat exchangers in helium systems C Lv1,2, J Z Wang1, 3, J H Wu1,2, Q Li1,2 and X J Xie1,2  1 Key Laboratory of Cryogenics, Technical Institute of Physics and Chemistry, Chinese Academy of Sciences, Beijing 100190, China 2 State Key Laboratory of Technologies in Space Cryogenic Propellants, Beijing 100190, China 3University of Chinese Academy of Sciences, Beijing 100049, China Conclusion Objectives Background 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 94.5% of the f data and 92.7% of the j data for laminar region, and 95.4% of the f data and 90.9% of the j data for the turbulent regime within ±20% derivation. . The simulation results denoted that extraction section was applicable in solving the heat transfer and fluid flow problems to ignore the entrance effect. 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 in low temperature. To study the inner flow pattern of the offset strip – fin heat exchangers Methods C Results The inner flow analysis of the model Mesh independence and the model verification The top view and axonometric drawing of computation domain One of the advantages of the numerical method is that it can be used to observe the flow pattern in every part of the model The contour of velocity didn’t show the periodicity for the first eight fins because of the entrance effect. After the 8th fins, the flow field features get steady. . The length of the model was confirmed by increasing the number of fins along the flow direction. The friction factor had no evident change until 20 fins, therefore 20 was chosen as the number of fins in simulation.. Flow velocity contours when Re=462 Usually, the fin-channel is assumed to be rectangular, and the fin offset is uniform and equal to half-fin spacing. In order to ignore the entrance effect, the extension section is established at the inlet and outlet of the fluid domain. Upstream section locates at 1.5 times hydraulic diameter from first fin in the flow direction while the downstream section sets as 5 times hydraulic diameter from the last fin. The pressure drop of model is tend to constant when the grid number is more than 800000. Hence, this grid number was chosen to calculate the j and f factors.   Flow velocity contours when Re=4560 Results The comparison between the regression data and the CFD results in laminar and turbulent region The above correlations predict 94.5% of the f data and 92.7% of the j data for laminar region, and 95.4% of the f data and 90.9% of the j data for the turbulent regime within ±20% derivation.. Comparison of correlation for f and j by correlations with CFD results in laminar region Comparison of correlation for f and j by correlations with CFD results in turbulent region Contact information: wujihao@mail.ipc.ac.cn; clv@mail.ipc.ac.cn Presented at the CEC/ICMC, 2017 July 9- July 13 2017, Madison Wisconsin; Presentation ID:C2PoL-01