MECO Production Target Developments James L. Popp University of California, Irvine NuFact ’ 03 Columbia, June, 2003.

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Presentation transcript:

MECO Production Target Developments James L. Popp University of California, Irvine NuFact ’ 03 Columbia, June, 2003

June, 2003J.L.Popp, UCI MECO Production Target2 MECO Collaboration Institute for Nuclear Research, Moscow V. M. Lobashev, V. Matushka New York University R. M. Djilkibaev, A. Mincer, P. Nemethy, J. Sculli, A.N. Toropin Osaka University M. Aoki, Y. Kuno, A. Sato University of Pennsylvania W. Wales Syracuse University R. Holmes, P. Souder College of William and Mary M. Eckhause, J. Kane, R. Welsh Boston University J. Miller, B. L. Roberts, O. Rind Brookhaven National Laboratory K. Brown, M. Brennan, L. Jia, W. Marciano, W. Morse, Y. Semertzidis, P. Yamin University of California, Irvine M. Hebert, T. J. Liu, W. Molzon, J. Popp, V. Tumakov University of Houston E. V. Hungerford, K. A. Lan, L. S. Pinsky, J. Wilson University of Massachusetts, Amherst K. Kumar

June, 2003J.L.Popp, UCI MECO Production Target3 MECO Muon Beam Line at AGS Goal: stopped   / sec –1000-fold increase in  beam intensity over existing facilities High-intensity proton beam and high-density target Target, cooling, & support: compact to minimize  absorption Axially-graded 5 T solenoid field very effective at  collection Calorimeter Straw Tracker Stopping Target Foils  Production Target The Superconducting Solenoids Proton Beam Muon Beam 5 T 2.5 T 2 T 1 T

June, 2003J.L.Popp, UCI MECO Production Target4 Target Heating Target: High density cylinder, L = 16 cm, R = 3-4 mm 4.0* GeV protons / sec from AGS Slow extraction, 0.5 s spill, 1.0 s AGS cycle time 2 RF buckets filled: 30 ns pulses, 1350 ns apart Total on-spill power deposition: W On-peak energy deposition distribution: V. Tumakov

June, 2003J.L.Popp, UCI MECO Production Target5 Production Target Cooling Radiation – minimal material in production region to reabsorb  ’s – significant engineering difficulties to overcome high operating temperature, T operation = 2145 – 3000 K - high thermal stresses - target evaporation - little hope of raising production rate beyond current goals low-density materials: manageable stresses; but extended complex shapes, difficult to support & can lead to excessive pion reabsorption Forced Convection w/ water as coolant – low operating temperature, T operation < T boil - water - negligible thermal stresses - hope for achieving greater sensitivity – minor impact on MECO sensitivity: cooling system absorbs  ’s – modest engineering difficulties handling coolant (water activation)

June, 2003J.L.Popp, UCI MECO Production Target6 Production Target Physics Simulations All with 3 mm OD inlet/outlet pipes  Large inlet/outlet   Small water channel & thin containment tube costs 5% muon yield Inlet & outlet pipes and target radius should be reoptimized Tungsten target Simulations of design parameters with GEANT3 indicate that both production target cooling methods can meet MECO physics requirements GEANT Simulations of Muon Yield Target Water Titanium UCI: A. Arjad, W.Molzon, M.Hebert, V.Tumakov, J.Popp Radiation-cooled R = 3 mm, L = 16 cm

June, 2003J.L.Popp, UCI MECO Production Target7 Radiation Cooling: Lumped Analysis of Heating Cycles Tungsten cylinder R = 4 mm L = 16 cm Long time limit: W: T melting = 3683 K

June, 2003J.L.Popp, UCI MECO Production Target8 Radiation Cooling: On-Spill Temperature & Von Mises Stress beam direction C. Pai, BNL Tungsten cylinder, symmetry ¼ L = 16.0 cm, R = 4 mm Power distribution: gaussian Thermal dependence: Properties W Von Mises stress Temperature Region of maximum Von Mises stress,  Yield = 20 Mpa or less Dividing up target into 0.1 cm slices, slotting & to axis, spacing by 0.8 cm gives stability, but target size is unacceptable

June, 2003J.L.Popp, UCI MECO Production Target9 Current Water-Cooled Design Pt or Au cylinder: L = 16.0 cm, R = 3.0 mm Ti inlet & outlet pipes: 25 cm long, ID = 2.1 mm, OD = 3.2 mm Annular coolant channel: h = 0.3 mm Tapered inlet end reduces pressure drop across target Water containment shell: 0.5 mm wall thickness In MECO: Cut-away side view inletoutlet beam direction highest temperature location

June, 2003J.L.Popp, UCI MECO Production Target10 Target Installed in Production Solenoid 0.5” service pipes Slot in heat shield: - guide - positioning Simple installation: - robotic manipulation - no rotations need - total of 1 vertical & 2 horizontal translations required Opening in heat shield for beam entrance Target rotated slightly off-axis to be optimally oriented for the beam

June, 2003J.L.Popp, UCI MECO Production Target11 Target Fully Installed: Cut-Away Wide View of Production Solenoid W.Molzon, J.Popp, M.Hebert, B.Christensen Target Beam entrance Solenoid coil packs

June, 2003J.L.Popp, UCI MECO Production Target12 Water Cooling: Lumped Analysis of Heating Cycles Simple calculations and hydo code indicate large heat transfer coefficient Characteristic response time is of order AGS cycle time Target may reach steady state T on each cycle Time-dependent turbulent hydrodynamic simulations required to fully characterize the time behavior and more precisely the maximum coolant temperatures: CFDesign – suitable computational tool

June, 2003J.L.Popp, UCI MECO Production Target13 Turbulent Flow in Annular Water Channel Coolant containment wall Target surface r z 0.0 m/s 15.5 m/s Turbulent Flow Axial Velocity, V(r,z) Worst case: steady state, 9500 W Inlet water conditions – temperature= 20 C – flow rate= 1.0 gpm – velocity= 10.6 m/s at inlet Flow channel – length= 16.0 cm – radius= 3.0 mm – gap= 0.3 mm Design parameters – target pressure drop= 127 psi – inlet pressure= 207 psi – outlet pressure= 80 psi – max. local water temp= 71 C – max. target temp (Au)= 124 C (core) – mean discharge temp= 56 C –stopped muon yield> 95% of rad. cooled

June, 2003J.L.Popp, UCI MECO Production Target14 Steady State Temperature Distribution Water-cooled Target Coolant containment wall Target surface r z Water gap, 0.3 mm Target surface Target surface Axial position - z Zoom below Diffusion dominated heat transfer layer:  m Fully developed turbulence in about 7 gap thickness Re: C Titanium containment wall Target core K K

June, 2003J.L.Popp, UCI MECO Production Target15 Target and Water Temperature Under Turbulent Conditions Heat transfer calculations for turbulent flow conditions demonstrate feasibility of the cooling scheme Target Center Target/Water Interface Water Channel Center 397 K 293 K Water Inlet Titanium Tube Inner Surface Target Core J.Carmona, R.Rangel, J.LaRue, J.Popp, W.Molzon Turbulence calculation - unstable flow - - local fluctuations - - solutions to N-S eqs - time averaged,  t - UCI:

June, 2003J.L.Popp, UCI MECO Production Target16 Target Cooling Test Stand Diagram Control: target geometry & flow rate Monitor: temperature & pressure: - target inlet & outlet - reservoir - target (not shown) Temperature probes: - thermistors - thermocouple Measurements of interest in heating tests: - power deposition in target - heat transfer coefficients target heat exchanger - target surface temperature - response times for power cycling

June, 2003J.L.Popp, UCI MECO Production Target17 Target Prototype Tests Two right-turns Tapered ends Water cooling effectiveness is being demonstrated via prototypes Pressure drop vs. flow rate tests completed First induction heating test completed, next test June 2003 Comparison of Prototype Data with HD Simulations Actual pressure drop is lower than simulations predict UCI: J.Popp, B.Christensen, C.Chen, W.Molzon

June, 2003J.L.Popp, UCI MECO Production Target18 Principle: Excite eddy currents which oppose changing magnetic flux, to obtain heating via Apply AC current to coil wrapped around work piece (e.g., solid rod, billet,…): H 0 = surface magnetic field intensity Solid cylinder: Induction Heating Ameritherm, Inc.; Induction Heat Treet, Co.; Huntington Beach, CA - 20 kW, 175 kHz - 30 kW, 10 kHz Example: Tensile test for metals at extreme temperatures

June, 2003J.L.Popp, UCI MECO Production Target19 Measured Power Deposition Solid rod: - R = 3.0 mm, L = 16.0 cm - Carpenter Technologies: High Permeability Alloy 49, 50/50 Fe/Ni Measured power deposited: - reservoir temperature rise - (outlet – inlet) temperature Approximately same result: 1450 W 264 W per K / unit discharge (gpm) Increase power deposition: - more turns per meter (coil w/ two close-packed layers) - reduce OD water containment shell - consider using higher-power unit Induction coil: turns/m - L = 23.6 cm, R = 3.8 cm - copper tubing: OD = cm Power supply - Lepel 20kW unit - f = 175 kHz

June, 2003J.L.Popp, UCI MECO Production Target20 Measured Target Surface Temperature Probe near max surface T position: cm in from outlet end - > 0.5 mm below surface T target - T inlet = 21.0 C Scaled to MECO: P MECO = 7500 W, (T target - T inlet )P MECO /P test = 108 C Good approx.: T surface = T inlet C To maintain non-boiling condition - raise outlet pressure - chill inlet water - increase discharge rate Annular water gap, h = 0.4 mm Flow rate = 1.0 gpm  P = 125 psi Skin depth:  = mm - f = 175 kHz - relative permeability    T target probe : - probe radial position not critical - T core - T surface << T target probe

June, 2003J.L.Popp, UCI MECO Production Target21 What next ? Opera calculations: redesign coil for greater power - two layers of coil windings - reduce OD of copper tubing, etc. - evaluate using 20 vs 30 kW unit (higher current & lower freq) 2 nd heating test in June improved sensor operation - higher power deposition - gap size 0.4 mm, run at higher flow rate - gap size 0.3 mm, run at various flow rates - more precise positioning for target surface temperature probe - characterize response time of target Opera calculations: design coil for MECO longitudinal heating profile Redesign water containment shell to improve pressure drop More heating tests in July 2003