Simple CFD Estimate of End Flange Tuner Finger Cooling.

Slides:



Advertisements
Similar presentations
New Plate Baffle Water Flow. Quick Simulation Use triangular prism as rough estimate of a vane Uniform heat flux on each surface –600 kWm -2 on end face.
Advertisements

RFQ Cooling Studies.
RFQ End Flange Dipole Tuner Finger Cooling. Basis of Study Need multi-purpose end flange –Adjustable dipole mode suppression fingers –Beam current transformer.
Chapter 7 : Convection – External Flow : Cylinder in cross flow
CFD Simulations of a Novel “Squirt-Nozzle and Water Bath” Cooling System for the RFQ.
Thermal Energy. Temperature  Measures the “hotness” (higher temperatures) or “coldness” (lower temperatures)  Gives very little information on the energy.
Longitudinal Expansion of RFQ Vane Ends at Section-to-Section Interface.
Chapter 3.2: Heat Exchanger Analysis Using -NTU method
Mike Fitton Engineering Analysis Group Design and Computational Fluid Dynamic analysis of the T2K Target Neutrino Beams and Instrumentation 6th September.
Analysis of Simple Cases in Heat Transfer P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Gaining Experience !!!
1 Dept. of Energy Technology, Div. of Applied Thermodynamics and Refrigeration Tube diameter influence on heat exchanger performance and design. Single.
First Wall Thermal Hydraulics Analysis El-Sayed Mogahed Fusion Technology Institute The University of Wisconsin With input from S. Malang, M. Sawan, I.
Fluid Flow and Continuity Imagine that a fluid flows with a speed v 1 through a cylindrical pip of cross-sectional area A 1. If the pipe narrows to a cross-
Main Points All matter is made up of invisible particles Particles have spaces between them Particles are moving all the time Particles move faster when.
CO2 cooling pressure drop measurements R. Bates, R. French, G. Viehhauser, S. McMahon.
Fouling Factor: After a period of operation the heat transfer surfaces for a heat exchanger become coated with various deposits present in flow systems,
1 Calorimeter Thermal Analysis with Increased Heat Loads September 28, 2009.
RFQ Thermal Analysis Scott Lawrie. Vacuum Pump Flange Vacuum Flange Coolant Manifold Cooling Pockets Milled Into Vanes Potentially Bolted Together Tuner.
Heat load study of cryomodule in STF
Bias Magnet for the Booster’s 2-nd Harmonic Cavity An attempt to evaluate the scope of work based of the existing RF design of the cavity 9/10/2015I. T.
Calorimeter Analysis Tasks, July 2014 Revision B January 22, 2015.
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.
ME421 Heat Exchanger Design
Stress and Cool-down Analysis Yun HE MLC Internal Review 9/5/2012Yun HE, MLC Internal Review1.
July 4 th 20061Moritz Kuhn (TS/CV/DC/CFD) CERN July 4 th 2006 Moritz Kuhn Cooling of the P326 Gigatracker silicon pixel detector (SPIBES) CFD – Cooling.
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.
Consideration of Baffle cooling scheme
CLIC Prototype Test Module 0 Super Accelerating Structure Thermal Simulation Introduction Theoretical background on water and air cooling FEA Model Conclusions.
Convection: Internal Flow ( )
Heat Transfer Equations. Fouling Layers of dirt, particles, biological growth, etc. effect resistance to heat transfer We cannot predict fouling factors.
Replies to Spanish RFQ Questions (slides re-used from previous talks)
M. Gomez Marzoa1 13th December 2012 PSB-Dump: first CFD simulations Enrico DA RIVA Manuel GOMEZ MARZOA 13 th December 2012.
Specific Heat and Thermal Flow. Specific Heat The heat required to raise the temperature of the unit mass of a given substance (usually one gram) by a.
1 Monophase Measurements on Prototype Pixel Structures D. Bintinger, M. Gilchriese, J. Taylor and J. Wirth and contributions from D. Cragg, E. Perrin and.
DCLL ½ port Test Blanket Module thermal-hydraulic analysis Presented by P. Calderoni March 3, 2004 UCLA.
Mitglied der Helmholtz-Gemeinschaft Jörg Wolters, Michael Butzek Focused Cross Flow LBE Target for ESS 4th HPTW, Malmö, 3 May 2011.
M. Yoda, S. I. Abdel-Khalik, D. L. Sadowski, B. H. Mills and M. D. Hageman G. W. Woodruff School of Mechanical Engineering Correlations for Divertor Thermal-Hydraulic.
AAE 450 – Spacecraft Design Sam Rodkey 1 Active Thermal Control Design Sam Rodkey March 1 st, 2005 Project Management Project Manager.
E. Da Riva1 ITS Upgrade - Air cooling Layers Geometry Change!
NSTX OH Coil Optimization Ali Zolfaghari. Optimization Parameters: Coolant channel diameter –Larger coolant diameter will lead to coil temp above 100°
Cooling of GEM detector CFD _GEM 2012/03/06 E. Da RivaCFD _GEM1.
Simulation of heat load at JHF decay pipe and beam dump KEK Yoshinari Hayato.
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.
Exercises for Q1. Insulated copper tube A thin walled 10 mm copper tube is used to transport a low-temperature refrigerant with a temperature that is.
AP Physics B: Lecture #21 Second Law of Thermodynamics “Heat will not flow spontaneously from a colder body to a warmer body AND heat energy cannot be.
Date of download: 5/28/2016 Copyright © ASME. All rights reserved. From: Forced Convection Heat Transfer in Spray Formed Copper and Nickel Foam Heat Exchanger.
Heat Transfer by Convection
LHCb Muon Station Cooling Studies (done by Ricardo Antunes Rodrigues (ST/CV)) This simulations were made for the Muon Station 1, with the follow assumptions:
A. Lambert: Thermal and Mechanical Analysis PXIE RFQ Design Review, Berkeley, CA April 12, 2012 Thermal and Mechanical Analysis of the PXIE RFQ Andrew.
RFQ Cooling Schemes and Instrumentation PXIE RFQ Fabrication Readiness Review LBNL – June 26, 2013 Andrew Lambert - Engineering Division Lawrence Berkeley.
TUTORIAL 1 7/3/2016.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 8 Internal flow.
704 MHz cavity design based on 704MHZ_v7.stp C. Pai
Chopper Beam Dump Thermal Problem 10/27/20101PX Linac FE Technical Discussions.
704 MHz cavity folded tuner Thermal Analysis C. Pai
Under floor heating Designing underfloor heating (UFH) system must always comply with the system suppliers instructions.
BCP Analysis Update Thomas Jones 22/7/16.
Stress and cool-down analysis of the cryomodule
CFD-Team Weekly Meeting - 8th March 2012
Aachen Status Report: CO2 Cooling for the CMS Tracker at SLHC
TBM thermal modelling status
Date of download: 3/4/2018 Copyright © ASME. All rights reserved.
Chapter 6: Thermal Energy
Heat As Energy Transfer
Heat Transfer Coefficient
Thermal Energy.
Topic: Temperature and Heat
Heat-transfer Equipment
12. Heat Exchangers Chemical engineering 170.
Chapter 3, Lesson 4, Conduction, Convection, and Radiation
Presentation transcript:

Simple CFD Estimate of End Flange Tuner Finger Cooling

Estimated Dimensions 2cm 1cm 3cm 5cm 6mm 4cm 5cm

Estimated Heat Load FETS RFQ: 62 Wcm -2 at vane cut-back Assume less than half this on fingers? So 25 Wcm -2 is reasonable. IPHI RFQ end flange: 26 Wcm -2 on fingers (CW RFQ, though, so ours will have much less than this in reality, but 25 Wcm -2 will allow large safety margin)

15°C Water in at 1 ms -1 flow rate Water out with temperature raised and at 0 Bar relative pressure 25 Wcm -2 heat flux load on finger High mesh density in region between finger and pipe Copper starting temperature = 22°C

Flow Estimates Total power, P, to be removed from each finger ≈ 160 W Water mass flow rate,, per pipe = kgs -1 (assuming flow speed = 1 ms -1 = 1.7 l min -1 ) Estimated temperature rise, ΔT, of cooling water = 1.35 °C Pipe length, L, within copper = 10 cm Average water flow rate v av = 1 ms -1 Pipe diameter, D H = 6 mm Estimated pressure drop, Δp = Bar Nusselt number, N u, of water flow = Thermal conductivity of water, k = 0.6 Wm -1 K -1 Estimated heat transfer coefficient = 5500 Wm -2 K -1

Intersection of drilled pipes slightly disrupts smooth flow

Faster, disrupted flow round corner increases local HTC Average HTC ~ 6000 Wm -2 K -1 which agrees with estimate

Temperature rise of water ~ 2 °C which agrees with estimate

Pressure drop is slightly higher than estimate because the pipe doesn’t have a smooth bend at corner, but it’s still nice and low

Bulk copper in end flange is ~ 40 °C Finger gets pretty warm (100 °C) but that shouldn’t matter at all

Summary Majority of heat removed ok Indirect cooling means finger gets hot …but not enough to worry about Assumes 25 Wcm -2 heat load (OVERESTIMATE!) Will proceed with RF simulation to get better estimate of heat load on fingers Overall, this cooling strategy should be fine