Long Pulse Fusion Physics Experiments Without Superconducting Electromagnets

Similar documents
Possibilities for Long Pulse Ignited Tokamak Experiments Using Resistive Magnets

Chapter 3 NATURAL CONVECTION

Lectures on Applied Reactor Technology and Nuclear Power Safety. Lecture No 6

If there is convective heat transfer from outer surface to fluid maintained at T W.

Improved Magnetic Fusion Energy Economics Via Massive Resistive Electromagnets

Heat Transfer Predictions for Carbon Dioxide in Boiling Through Fundamental Modelling Implementing a Combination of Nusselt Number Correlations

Chapter 17 Temperature and heat

PHYS102 Previous Exam Problems. Temperature, Heat & The First Law of Thermodynamics

Material, Design, and Cost Modeling for High Performance Coils. L. Bromberg, P. Titus MIT Plasma Science and Fusion Center ARIES meeting

ME 331 Homework Assignment #6

Chapter: Heat and States

Convection Heat Transfer. Introduction

Ben Wolfe 11/3/14. Figure 1: Theoretical diagram showing the each step of heat loss.

Lesson 6 Review of fundamentals: Fluid flow

Innovative fabrication method of superconducting magnets using high T c superconductors with joints

Lecture 30 Review of Fluid Flow and Heat Transfer

ME 402 GRADUATE PROJECT REPORT ACTIVE BATTERY COOLING SYSTEM FOR ALL-ELECTRIC VEHICLES JINGWEI ZHU

Physics 5D PRACTICE FINAL EXAM Fall 2013

TankExampleNov2016. Table of contents. Layout

Studies of Next-Step Spherical Tokamaks Using High-Temperature Superconductors Jonathan Menard (PPPL)

8.1 Technically Feasible Design of a Heat Exchanger

Convection. forced convection when the flow is caused by external means, such as by a fan, a pump, or atmospheric winds.

Level 7 Post Graduate Diploma in Engineering Heat and mass transfer

GA A22677 THERMAL ANALYSIS AND TESTING FOR DIII D OHMIC HEATING COIL

SEM-2017(03HI MECHANICAL ENGINEERING. Paper II. Please read each of the following instructions carefully before attempting questions.

FE Fluids Review March 23, 2012 Steve Burian (Civil & Environmental Engineering)

A SUPERCONDUCTING TOKAMAK FUSION TRANSMUTATION OF WASTE REACTOR

Heat Transfer Coefficient Solver for a Triple Concentric-tube Heat Exchanger in Transition Regime

GA A23168 TOKAMAK REACTOR DESIGNS AS A FUNCTION OF ASPECT RATIO

Heat and Mass Transfer Prof. S.P. Sukhatme Department of Mechanical Engineering Indian Institute of Technology, Bombay

Physics of fusion power. Lecture 14: Anomalous transport / ITER

Coolant. Circuits Chip

Yuntao, SONG ( ) and Satoshi NISHIO ( Japan Atomic Energy Research Institute

Summary of Dimensionless Numbers of Fluid Mechanics and Heat Transfer

PROBLEM 8.3 ( ) p = kg m 1m s m 1000 m = kg s m = bar < P = N m 0.25 m 4 1m s = 1418 N m s = 1.

Chapter 1 INTRODUCTION AND BASIC CONCEPTS

Handout 10: Heat and heat transfer. Heat capacity

Analysis of the Cooling Design in Electrical Transformer

Available online at ScienceDirect. Physics Procedia 67 (2015 ) Superfluid helium heat pipe. P.

Lesson 7: Thermal and Mechanical Element Math Models in Control Systems. 1 lesson7et438a.pptx. After this presentation you will be able to:

Appendix C FIRE Coil Cooling Calculations

Tutorial 1. Where Nu=(hl/k); Reynolds number Re=(Vlρ/µ) and Prandtl number Pr=(µCp/k)

Heat processes. Heat exchange

Circle one: School of Mechanical Engineering Purdue University ME315 Heat and Mass Transfer. Exam #1. February 20, 2014

Lectures on Applied Reactor Technology and Nuclear Power Safety. Lecture No 7

Optimization of the Air Gap Spacing In a Solar Water Heater with Double Glass Cover

ELECTROMAGNETIC LIQUID METAL WALL PHENOMENA

CRYOGENIC HOSES & PAIN TS ACCESSORIES

Ch. 3. Pulsed and Water Cooled Magnets. T. J. Dolan. Magnetic field calculations

Design optimization of first wall and breeder unit module size for the Indian HCCB blanket module

Chapter 18 Temperature, Heat, and the First Law of Thermodynamics. Thermodynamics and Statistical Physics

10 minutes reading time is allowed for this paper.

In order to optimize the shell and coil heat exchanger design using the model presented in Chapter

GA A22689 SLOW LINER FUSION

(Heat capacity c is also called specific heat) this means that the heat capacity number c for water is 1 calorie/gram-k.

Applied Fluid Mechanics

PROBLEM Node 5: ( ) ( ) ( ) ( )

Technological design and off-design behavior of heat exchangers 26

4.1. Physics Module Form 4 Chapter 4 - Heat GCKL UNDERSTANDING THERMAL EQUILIBRIUM. What is thermal equilibrium?

8.21 The Physics of Energy Fall 2009

Specific heat capacity. Convective heat transfer coefficient. Thermal diffusivity. Lc ft, m Characteristic length (r for cylinder or sphere; for slab)

HEAT TRANSFER 1 INTRODUCTION AND BASIC CONCEPTS 5 2 CONDUCTION

Piping Systems and Flow Analysis (Chapter 3)

The Research of Heat Transfer Area for 55/19 Steam Generator

Chapter 3 PROPERTIES OF PURE SUBSTANCES. Thermodynamics: An Engineering Approach, 6 th Edition Yunus A. Cengel, Michael A. Boles McGraw-Hill, 2008

LEAKLESS COOLING SYSTEM V.2 PRESSURE DROP CALCULATIONS AND ASSUMPTIONS

ELEC9712 High Voltage Systems. 1.2 Heat transfer from electrical equipment

Developing a Robust Compact Tokamak Reactor by Exploiting New Superconducting Technologies and the Synergistic Effects of High Field D.

Thermodynamics I. Properties of Pure Substances

CRYOGENIC CONDUCTION COOLING TEST OF REMOVABLE PANEL MOCK-UP FOR ITER CRYOSTAT THERMAL SHIELD

Examination Heat Transfer

Chemical and Biomolecular Engineering 150A Transport Processes Spring Semester 2017

INTRODUCTION TO MAGNETIC NUCLEAR FUSION

Superconducting cables Development status at Ultera

MYcsvtu Notes HEAT TRANSFER BY CONVECTION

PROPERTIES OF PURE SUBSTANCES. Chapter 3. Mehmet Kanoglu. Thermodynamics: An Engineering Approach, 6 th Edition. Yunus A. Cengel, Michael A.

Mechanical Engineering. Postal Correspondence Course HEAT TRANSFER. GATE, IES & PSUs

UNIT II CONVECTION HEAT TRANSFER

Thermodynamics Introduction and Basic Concepts

Arctice Engineering Module 3a Page 1 of 32

Development of Remountable Joints and Heat Removable Techniques for High-temperature Superconducting Magnets

II/IV B.Tech (Regular) DEGREE EXAMINATION. (1X12 = 12 Marks) Answer ONE question from each unit.

Introduction to Heat Transfer

Temperature Thermal Expansion Ideal Gas Law Kinetic Theory Heat Heat Transfer Phase Changes Specific Heat Calorimetry Heat Engines

1. How much heat was needed to raise the bullet to its final temperature?

HT-7U* Superconducting Tokamak: Physics design, engineering progress and. schedule

Internal Forced Convection. Copyright The McGraw-Hill Companies, Inc. Permission required for reproduction or display.

University of Rome Tor Vergata

Feasibility of HTS DC Cables on Board a Ship

1/54 Circulation pump, safety valve, expansion vessel

CONVECTIVE HEAT TRANSFER

S.E. (Chemical) (Second Semester) EXAMINATION, 2012 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100

Thermal Field in a NMR Cryostat. Annunziata D Orazio Agostini Chiara Simone Fiacco

Status and Progress of a Fault Current Limiting HTS Cable To Be Installed In The Consolidated Edison Grid

Overview of Pilot Plant Studies

Heat Transfer Modeling using ANSYS FLUENT

Attempt ALL QUESTIONS IN SECTION A and ANY TWO QUESTIONS IN SECTION B Graph paper will be provided.

PROBLEM ρ v (kg/m 3 ) ANALYSIS: The critical heat flux can be estimated by Eq with C = 0.

(Refer Slide Time: 00:00:59 min)

PHYSICAL MECHANISM OF CONVECTION

Transcription:

Long Pulse Fusion Physics Experiments Without Superconducting Electromagnets Robert D. Woolley Princeton University Princeton Plasma Physics Laboratory* P.O. Box 45, Princeton, New Jersey 08543 (609) 43-330 *Supported by U.S.Department of Energy Contract No. DE-AC0-76CH03073. ABSTRACT Long pulse fusion physics experiments can be performed economically via resistive electromagnets designed for thermally steady-state operation. Possible fusion experiments using resistive electromagnets include long pulse ignition with DT fuel.,,3,4 Long pulse resistive electromagnets are alternatives to today s delicate and costly superconductors. 5 At any rate, superconducting technology is now evolving independent of fusion, so near-term superconducting experience may not ultimately be useful. High magnetic field copper coils can be operated for long pulses if actively cooled by subcooled liquid nitrogen, thermally designed for steady state operation. (Optimum cooling parameters are characterized herein.) This cooling scheme uses the thermal mass of an external liquid nitrogen reservoir to absorb the long pulse resistive magnet heating. Pulse length is thus independent of device size and is easily extended. This scheme is most effective if the conductor material is OFHC copper, whose resistivity at liquid nitrogen temperature is small. Active LN cooling also allows slow TF ramp-up and avoids high resistance during current flattop; these factors reduce power system cost relative to short pulse adiabatic designs. I. INTRODUCTION The main design issue for long pulse resistive electromagnets is heat removal (within stress limitations). Successful designs can employ thermally steady cooling via forced convection of a liquid coolant, pressurized to prevent film boiling. True steady-state operation would require the warmed coolant fluid to be continuously recooled, but for intermittent long pulse operation the warmed fluid can be stored in a reservoir and recooled later between pulses. Although choosing water as the coolant has some practical advantages (e.g., economy, high heat capacity, and the ability to exhaust steady magnet heat directly into the environment without any refrigeration system), the consequent room temperature magnet operation can require a costly electric power system capability. But since resistive power is proportional to conductor resistivity (see Figure ) the alternative use of a cryogen as combined coolant and thermal mass for intermittent long pulse operation can greatly reduce resistive electric power consumption, which eases the heat removal task while also reducing capital cost requirements for the electrical power system. Liquid nitrogen is a natural choice for the cryogen. A byproduct of industrial oxygen production, it is cheaply available by the truckload in many locations, and so does not necessarily require the purchase of a cryogenic refrigerator. Large insulated dewar tanks to store it are available and inexpensive. It is nontoxic and can be released safely into the environment. It is not chemically explosive as are some cryogens. It is almost inert chemically and will not attack any materials used in magnet construction. It is also an excellent electrical insulator. 6 0 Electrical Resistivity Vs. Temperature for BeCu (HighConductivityC750) and for Oxygen Free High Conductivity (OFHC) Copper (C0400-0700) LN Freezes LN Boils Electrical Resistivity (NanoOhm-Meters) BeCu C750 HighConductivityVersion OFHC Cu C0400-0700 50 00 50 00 50 300 Temperature (Kelvins) Figure :Copper Alloy and Copper Resistivity A particularly simple design concept is a once-through system employing two identical large storage dewars with interconnected gas spaces, as depicted in Figure. One dewar is initially filled with liquid nitrogen at atmospheric pressure but subcooled to nitrogen s 63. K triple point temperature, while the second dewar is initially empty. During the long pulse, liquid nitrogen from the first dewar is pumped through cooling passages in the electromagnets sufficiently fast that its exit temperature does not exceed liquid nitrogen s 77.4 K normal boiling point. Exiting liquid nitrogen flows into the second dewar at atmospheric pressure. During time intervals between pulses the nitrogen is returned to the first dewar and recooled to the triple point. Useful features of this long pulse scheme include: No real-time coolant release to the atmosphere is involved. (This safety feature is important if coolant nitrogen becomes temporarily activated by DT neutrons.)

Long pulse duration can be extended arbitrarily without reengineering the fusion experiment s magnet system, by simply installing more liquid nitrogen storage dewars. Coolant and thermal mass storage is, economically, at atmospheric pressure. No real-time heat transfer during the long pulse is required except inside the electromagnets. Steady electromagnet electric power is greatly reduced below that of water-cooled room-temperature designs. No on-site electrical energy storage system is required to quickly ramp up the toroidal magnetic field, i.e., the TF electric power system rating can be based on steady losses. Large Dewar 63. K LN atm Pump Copper Magnets for Burning Plasma Tokamak Pressure Reduction Large Dewar < 77.4 K LN atm Cryo Cooler Operates Between Pulses Pump Figure : Once-Through Long Pulse Concept Recooling of the 77.4 K liquid nitrogen can be unconventionally but cheaply implemented via a simple pumping system containing a section in which liquid pressure is reduced to nitrogen s /8 atmosphere triple point pressure. This evaporative recooling approach does not necessitate purchasing a cryogenic refrigerator nor even a heat exchanger. Energy released from the temperature reduction via liquid nitrogen s specific heat (c p ) is balanced by energy absorbed by its heat of vaporization (h fg ), as about 5% of the 77.4 K liquid nitrogen flashes to the gaseous state. Repressurization of the separated 63. K liquid stream does not significantly raise its temperature above the triple point, so the liquid emerges at atmospheric pressure near its freezing point temperature. Repressurization of the separated gas stream to atmospheric pressure raises its temperature to about 05 K. In the least capital cost implementation the nitrogen gas is exhausted into the atmosphere and replaced by purchased liquid nitrogen. In the least operating cost implementation a local cryogenic refrigerator reliquifies the 05 K nitrogen gas. Liquid 77.4 K atm. gas/liquid separator /8 atm. 63. K 0.7 m vertical column reduces pressure to triple point liquid gas pump Gaseous 05 K atm. Liquid 63. K atm. Figure 3: A Low Capital Cost Recooling Scheme Figure 3 depicts a version of this recooling concept in which gravity helps provide the required pressure changes and the process is driven by a single pressure reduction pump. II. SIMPLE THERMAL-HYDRAULIC RELATIONS Since design of an actively cooled electromagnet requires choosing many parameters, it is useful to review the relationships between them and how to choose them for best performance. This has been examined in the past, e.g. by R. Kronauer. 7 His approach is repeated here but is updated to use SI units and today s generally accepted models for pressure drop and heat transfer, specialized for subcooled liquid nitrogen active cooling as proposed herein. 8,9 It should be noted, however, that this development is incomplete since it requires conductor resistivity to be estimated a priori. Actually, increased active cooling will reduce conductor temperature, resistivity, and dissipated power, thus reducing the need for active cooling. D Figure 4: Schematic of Cooling Channels in Conductor We initially consider a conductor volume, V, carrying a specified average current density, J. Let η be the conductor s electrical resistivity. Then P, the resistive electric power density which would be dissipated if none of the conductor volume were removed, is P = η J () L

and the total power dissipated in the volume is η J V.Let a fraction of the volume, β, be removed to form some identical coolant channels. The volume of material removed is βv and the remaining volume of conductor is (- β)v. The average current density in the now smaller conductor is J=J /(- β). () Dissipated power in the volume is η (J /(- β)) (- β)v, so the new power density (based on the original volume, V) is P diss =P /(- β). (3) For noncircular coolant channel cross-sections (see Figure 5) with area A and perimeter C, the hydraulic diameter is D=4A/C (4) These cross-sections have the same hydraulic diameter, D. Figure 5: Noncircular Coolant Channel Cross-sections L is a coolant channel s length in the flow direction, so its heat transfer surface area is CL. The volume of a single coolant channel is AL, so the number of channels in the original volume is βv/(al). Total heat transfer surface area in the original volume is (CL)(βV/(AL))= 4βV/D, so total heat transfer surface area per cubic meter is 4β/D. U is the average velocity of coolant fluid flowing in a coolant channel, and the Reynolds number is Re=ρUD/µ where ρ and µ are LN s mass density and viscosity. Turbulent flow friction causes a pressure drop in the coolant channel given by the Darcy-Weisbach formula, p= (L/D) ρu f(re)/, (5) where the friction factor, f, depends on the Reynolds number through Colebrook s equation for smooth-walled passages: f=/( log 0 (Re)-0.8+log 0 f). (6) Pumping power for the original volume, V, is the product of pressure drop, p, and volumetric flow rate, βuv/l. Considering the pump efficiency, ζ, the power density per original cubic meter required for coolant pumping is P pump = p β U/(L ζ). (7) Total power consumed per original cubic meter is then P total = P diss +P pump =P /(- β) + β ρu 3 f(ρud/µ) /(Dζ) (8) Flow friction raises bulk coolant temperature as: T µ = p/(ρc p ) (9) where C p is LN s specific heat at constant pressure. The rise in bulk coolant temperature because of absorbed electrical dissipation power is T e = (L/(UρC p )) P /(β(- β)) (0) The heat transfer film drop is the heat flux divided by the heat transfer coefficient, h, i.e. T f = ((P /(- β)) /(4 β /D))/h = DP /( 4 h β (- β)) () where h is governed by the Dittus-Boelter correlation, Nu=0.043 Re 0.8 Pr 0.4 () where Nu=hD/k is the flowing coolant s Nusselt number, where Pr=µ C p /k is its Prandtl number, and where k is its thermal conductivity. Then the temperature difference between the the cold coolant supplied to the electromagnet and the conductor surface at the coolant channel exit is T 0 = T e + T µ + T f (3) Some liquid nitrogen property values useful in the evaluation of these formulas are given in Table. 0, Table : Relevant Liquid Properties Parameter 63. K 65 K 70 K 75 K 77.36 K p sat (kpa).8 7.4 38.5 76.0 0.3 ρ f (kg/m 3 ) 870 860.9 840.0 88. 807.3 h fg (kj/kg) 6 4.0 08.3 0.3 99.3 c p (J/kg K) 000 008 04 04 05 µ (µpa-s) 300 78 0 73 58 k (w/m K) 0.63 0.59 0.50 0.43 0.40 Pr 3.7 3.5.97.47.3 III. OPTIMIZATION The simple formulas above map from the five variables, P,L,D,U,β, and coolant properties into T 0, P total, and other parameters. For each specified (P, L) pair, the optimization procedure jointly varies D, U, β, in order to minimize P total while satisfying an equality constraint on T 0. For these calculations T 0 was held equal to 5 K since that resulted in LN bulk temperature rises near 0 K, a practical design target. LN coolant properties for 70 K were used. Figures 6-9 summarize the optimized results for a range of (P, L) values. Solid lines in these plots restrict coolant velocity to not exceed m/s, the highest velocity for which published heat transfer test data were found. (Technology exists for aggressive cryogenic pumping, e.g., developed for rocketry applications.)

IV. AN EXAMPLE - ACTIVE COOLING OF BPX-AT 00 0.0 0.00 0 Coolant Bulk Velocity (m/s) Channel Lengths 0 m 5 m m 0.5 m to Not Exceed m/s.) 0 5 0 6 0 7 0 8 0. Conductor Power Density WITHOUT Cooling Channels (w/m 3 ) Figure 6: Optimized Subcooled LN Coolant Velocity Size/Power Scaling 0 m 5 m m 0.5 m Total Fractional Power Increase Channel Lengths To Not Exceed m/s. Higher Velocity 0 5 0 6 0 7 0 8 Conductor Power WITHOUT Cooling Channels (w/m 3 ) Figure 7: Additional Per Unit Power Required, Including Both Coolant Pumping Power Plus Power From Heightened Current Density, With Coolant Channel Conductor Removed 0. 0.0 0m 5 m m 0.5 m (Channel Lengths) 0.00 0 5 0 6 0 7 0 8 Figure 8: Size/Power Scaling of Optimal Conductor Fraction Removed for Subcooled LN Cooling Channels Coolant Channel Volume/Original Conductor Volume to Not Exceed m/s. Higher Conductor Power Density WITHOUT Cooling Channels As an example, we consider the previously proposed BPX- AT design for a DT experiment, whose plasma parameters appear in Table. It turns out that it is even possible to modify the BPX-AT design to provide for arbitrarily long pulse operation, but perhaps with some increase in stress. The BPX-AT TF coil design (see Figure 0) relied on inner leg half-turns of strong BeCu conductor material, wedged in the nose region in order to be self-supportin for radial loads and thus not require significant additional support structure. OFHC copper conductor was planned for their lower stress outer leg half-turns. The two conductor materials were to be welded together at top and bottom to form each TF coil conductor turn. The TF coils were planned to operate without active cooling, adiabatically heating up during each pulse from liquid nitrogen temperature to near room temperature. At BPX-AT s full 0 Tesla design field, the expected flattop time duration available was limited to 0 seconds. Table : BPX-AT Parameters Parameter Value Plasma Major Radius R.0 meters Plasma Minor Radius a 0.5 meters Aspect Ratio 4 Elongation κ 95 Triangularity δ 95 0.-0.3 Toroidal Field B T 0 Ts Plasma Current I P 6.5 MA Fusion Multiplier Q 5 3 0 BeCu. OFHC Cu. 0.0 0.00 Cooling Channel Hydraulic Diameter (m) Channel Length=0 meters Channel Length= 5 meters Channel Length= meter Channel Length= 0.5 meter to Not Exceed Any Coolant Velocity) 0 5 0 6 0 7 0 8 Conductor Power Density WITHOUT Cooling Channels (w/m 3 ) Figure 9: Optimum Subcooled LN Cooling Channel Size/Power Relations 3 3 4 C L meters Figure 0: BPX-AT TF Coil Elevation View The designed maximum TF current density ranges from 8.0 MA/m in the OFHC copper outer legs to 30.7 MA/m the BeCu nose region. Assuming active cooling effectiveness in maintaining average conductor temperature at 77 K, Figure predicts average resistivities of nω -m and

0 nω-m, respectively. Heat dissipation without removing any conductor for cooling channels is then P =0.65 MW/m 3 in the OFHC copper outer legs, but P =9.44 MW/m 3 in the BeCu inner leg nose region. Half-turn cooling with flow path lengths near L=5 meters could be used for the OFHC copper outer legs. For P =0.65 MW/m 3, Figures 6-9 optimally recommend removing 4 percent of the conductor volume to form D= centimeter hydraulic diameter coolant channels through which subcooled liquid nitrogen flows at 0 m/s coolant velocity. Total steady power for electrical dissipation plus pumping increases only about 4 % above the power initially required at the start of a pulse without active cooling. On the other hand, L=5 meter half-turn cooling of the BeCu inner legs does not appear attractive. With P =9.44 MW/m 3, Figures 6 through 9 optimally recommend removing 7 percent of the conductor to make room for coolant channels through which liquid nitrogen flows at 4 m/s, or removing 8 percent of the conductor material for liquid nitrogen flow constrained to m/s. Either way, stresses would rise substantially. But there is another flow path geometry possible for the BPX-AT TF coil. Liquid nitrogen flow can be radial, from the TF coil s inside which faces the plasma to its outside.because the BPX-AT uses a wedged design, it is structurally possible to provide coolant supply and return manifolds on both inside and outside of the coil turns. With this geometry the coolant channel length in the nose region is about L= 0.5 meter. For P =9.44 MW/m 3, Figures 6-9 then optimally recommend removing 3.4% of the BeCu conductor to construct flow passages with hydraulic diameter D=.5 millimeters and through which liquid nitrogen flows at 9.6 m/s. The total steady power for BeCu dissipation and cooling is then about 5 percent higher than the initial dissipation for the adiabatic design. BeCu.5 mm X.5 mm. surface cooling channels Figure : Cooling ChannelsView From Plasma Figure depicts surface locations on one TF turn for these radial flow channels. Although this channel placement is simple and removes only 3.4 percent of the conductor volume, it eliminates 3 % of the area effective for wedging support of radial loads. This reduction in wedging area will directly increase the peak conductor stresses. On the other hand, active cooling reduces stresses caused by thermal gradients; in particular the significant thermal stress which develops in the adiabatic design at the junction between BeCu and OFHC copper conductors is almost completely eliminated in the actively cooled design. V. CONCLUSION Intermittent, low duty cycle, long pulse fusion experiments with self-heated DT plasmas can be implemented using cheap, robust, conventional, high magnetic field copper electromagnets designed for thermally steady active cooling with subcooled liquid nitrogen. Such magnet designs avoid many of the problems associated with delicate and costly superconductors, and could permit substantially lower costs and shorter times for magnet technology development, for device construction, and for operations overhead. With today s tight fusion budget pressures and receding fusion development schedules, the author believes it prudent to adopt actively cooled copper magnet technology instead of superconductors for fusion s major next step experiments. REFERENCES. L.Bromberg, et al, A Long-Pulse Ignited Test Experiment- (LITE), Nuclear Technology/Fusion V4; 9 (983). A. TANGA et al, A High Performance and Long Pulse Tokamak, EURATOM-ENEA, CentroRicercheEnergia, CP6500044 Frascati, Rome, Italy (99) 3. E.A.Chaniotakis, et al, Possibilities for Long Pulse Ignited Tokamak Experiments using Resistive Magnets, M.I.T.PlasmaFusionCenter, Cambridge,MA039, (99) 4. R.Woolley, Design Study of Copper Toroidal Field Coils with Bow Shaping, Demountable Sliding Joints, and Active Liquid- Cooling, Proc. ANS Annual Meeting, June996 (Reno) 5. T.Adair et al, High Field Solenoid Magnet with Liquid Cooling, Rev.Sci.Instr. 3 No.4 (960),p46-48 6. J.Gerhold, Dielectric breakdown of cryogenic gases and liquids, CRYOGENICS, October 979, p57-584 7. R.E. Kronauer, Optimal Design Of Fluid-Cooled Electromagnets, High Magnetic Fields, Proc.Intl.Conf.on High Magnetic Fields Nov.96, ed.h.kolm,p6-38,mitpress/jwiley&sonsinc,96 8. R. Fox, Introduction to Fluid Mechanics, Ch8, John Wiley & Sons Inc, New York, 985 9. E. Eckert & R. Drake, Heat and Mass Transfer, Ch8, McGraw-Hill Book Company, New York, 959 0. R. Scott, Cryogenic Engineering, p77-83,d.van Nostrand Company,Inc., Princeton New Jersey, 959. R. Barron, Cryogenic Systems, p474, Oxford University Press, New Yourk, 985. D. Meade, W. Reiersen et al, BPX-AT Executive Summary, Internal PPPL Report, March 99