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PFC/RR-81-26 DOE UC-20 C, D, E AN EVALUATION OF ACCIDENTAL WATER-REACTIONS WITH LITHIUM COMPOUNDS IN FUSION REACTOR BLANKETS P. J. Krane M. S. Kazimi July 1981 Plasma Fusion Center and the Department of Nuclear Engineering Massachusetts Institute of Technology Cambridge, Massachusetts 02139 E.G. & G. Idaho, Inc. and The U.S. Department of Energy Idaho Operations Office under DOE Contract #DE-AP07-79ID00019
Transcript
  • PFC/RR-81-26DOE UC-20 C, D, E

    AN EVALUATION OF

    ACCIDENTAL WATER-REACTIONS WITH LITHIUM

    COMPOUNDS IN FUSION REACTOR BLANKETS

    P. J. KraneM. S. Kazimi

    July 1981

    Plasma Fusion Center

    and the

    Department of Nuclear Engineering

    Massachusetts Institute of TechnologyCambridge, Massachusetts 02139

    E.G. & G. Idaho, Inc.

    and

    The U.S. Department of EnergyIdaho Operations Office

    under

    DOE Contract #DE-AP07-79ID00019

  • PUBLICATIONS UNDER CONTRACT #K-1702ON FUSION SAFETY

    1. M. S. Kazimi et al., "Aspects of Environmental Safety Analysis ofFusion Reactors," MITNE-212, Dept. of Nuclear Engineering, M.I.T.,October 1977.

    2. R. W. Sawdye, J. A. Sefcik, M. S. Kazimi, "Reliability Requirementsfor Admissible Radiological Hazards from Fusion Reactors," Trans.Am. Nucl. Soc. 27, 65-66, November 1977.

    3. D. A. Dube, M. S. Kazimi and L. M. Lidsky, "Thermal Response ofFusion Reactor Containment to Lithium Fire," 3rd Top. Meeting inFusion Reactor Technology, May 1978.

    4. R. W. Sawdye and M. S. Kazimi, "Application of Probabilistic ConsequenceAnalysis to the Assessment of Potential Radiological Hazards of Poten-tial Hazards of Fusion Reactors," MITNE-220, Dept. of Nuclear Engi-neering, M.I.T., July 1978.

    5. D. A. Dube and M. S. Kazimi, "Analysis of Design Strategies forMitigating the Consequences of Lithium Fire within Containment ofControlled Thermonuclear Reactors," MITNE-219, Dept. of NuclearEngineering, M.I.T., July 1978.

    6. R. W. Sawdye and M. S. Kazimi, "Fusion Reactor Reliability RequirementsDetermined by Consideration of Radiological Hazards," Trans. Am. Nucl.Soc. 32, 66, June 1979.

    7. R. W. Green and M. S. Kazimi, "Safety Considerations in the Design ofTokamak Toroidal Magnet Systems," Trans. ANS 32, 69, June 1979.

    8. R. W. Green and M. S. Kazimi, "Aspects of Tokamak Toroidal MagnetProtection," PFC/TR-79-6, Plasma Fusion Center, M.I.T., July 1979.

    9. S. J. Piet and M. S. Kazimi, "Uncertainties in Modeling of Consequencesof Tritium Release from Fusion Reactors," PFC/TR-79-5, Plasma FusionCenter, M.I.T., July 1979.

    10. M. J. Young and S. J. Piet, "Revisions to AIRDOS-II," PFC/TR-79-8,Contract #K-1702, Plasma Fusion Center, M.I.T., August 1979.

    11. S. J. Piet and M. S. Kazimi, "Implications of Uncertainties inModeling of Tritium Releases from Fusion Reactors," Proc. TritiumTechnology in Fission, Fusion and Isotopic Applications, April 1980.

    12. M. S. Tillack and M. S. Kazimi, "Development and Verification of theLITFIRE Code for Predicting the Effects of Lithium Spills in FusionReactor Containments," PFC/RR-80-ll, Plasma Fusion Center, M.I.T.,July 1980.

  • Publications Under Contract #K-1702 (continued)

    13. M. S. Kazimi and R. W. Sawdye, "Radiological Aspects of Fusion ReactorSafety: Risk Constraints in Severe Accidents," J. of Fusion Energy,Vol. 1, No. 1, pp. 87-101, January 1981.

    14. P. J. Krane and M. S. Kazimi, "An Evaluation of Accidental Water-Reactions with Lithium Compounds in Fusion Reactor Blankets,"PFC/RR-81-26, Plasma Fusion Center, M.I.T., July 1981.

    15. D. R. Hanchar and M. S. Kazimi, "Tritium Permeation Modelling of aConceptual Fusion Reactor Design," PFC/RR-81-27, Plasma Fusion Center,M.I.T., July 1981.

  • AN EVALUATION OF ACCIDENTAL WATER-REACTIONS

    WITH LITHIUM COMPOUNDS IN FUSION REACTOR BLANKETS

    ABSTRACT

    Efforts to mitigate potential problems of lithium-based blanketsfor fusion reactors include the use of lithium compounds for breedingpurposes. This report investigates the safety aspects of these alloys -relative to the use of pure lithium in a water-cooled blanket. Includedin the study is a modification of the LITFIRE computer code to predictthe thermal response of an internal blanket breeder-water interaction.

    For the problem analyzed, results indicate that some of thelithium-lead alloys may pose safety problems approximate to thoseassociated with the use of liquid lithium. Li20 is shown to besignificantly safer than liquid lithium, while results using LiAl aresimilar to those of the lithium-lead alloys.

    In addition, the study provides an overview of this safety question,signaling areas that require further development.

  • -3-

    ACKNOWLEDGEMENTS

    Many people helped bring this effort to conclusion. In particular,

    Mark Tillack and Steve Piet, and Rachel Morton provided the needed hints

    to run LITFIRE and locate material properties.

    Gail Jacobson transformed the written notes into a typed manuscript.

    This report is based on a thesis submitted by the first author as

    part of the requirements for the degree of M.S. in Nuclear Engineering.

  • -4-

    TABLE OF CONTENTS

    Abstract .......................................................

    Acknowledgements ...............................................

    List of Figures ................................................

    List of Tables .................................................

    page

    2

    3

    6

    7

    CHAPTER 1.

    CHAPTER 2.

    CHAPTER 3.

    CHAPTER 4.

    INTRODUCTION .......................................

    BLANKET DESIGN BASIS DESCRIPTION ...................

    2.1 Introduction ..................................

    2.2 Breeding Material .............................

    2.2.1 Lithium-Lead Alloys ....................2.2.2 Alternative Breeders ................

    2.3 Coolant .......................................

    2.4 NUWMAK Blanket Design .........................

    2.4.1 Structural Materials....................2.4.2 Mechanical Design ......................2.4.3 Summary of Important Parameters ........

    EQUILIBRIUM Tf CALCULATION .........................

    3.1 Introduction ..................................

    3.2 Assumptions and Methodology ...................

    3.3 Results and Discussion ........................

    DYNAMIC CALCULATIONS USING LITFIRE .................

    4.1 Introduction ..................................

    4.2 LITFIRE Description ...........................

    4.3 Internal Blanket Accident Option ..............

    4.3.1 Assumptions and Structural Model .......

  • -5-

    Table of Contents (continued)

    4.3.2 Heat Transfer Mechanisms ................

    A. Heat of Reaction ....................B. Sensible Heat Addition to Reactants .C. Forced Convective Cooling ...........D. Conduction ..........................E. Free Convection .....................F. Radiation ...........................

    4.3.3 The Numerical Scheme ....................

    4.4 Results and Discussion ........................

    CHAPTER 5.

    References

    Appendix A.

    Appendix B.

    Appendix C.

    Appendix D.

    CONCLUSIONS AND RECOMMENDATIONS .....................

    .....................................................

    Physical Properties Data ...........................

    Complete Listing of LITFIRE ........................

    Sample Input to LITFIRE ............................

    Sample Output of LITFIRE ...........................

    page

    49

    495152535354

    55

    56

    67

    69

    70

    74

    115

    118

  • -6-

    LIST OF FIGURES

    No. page

    1.1 LITFIRE Predictions for Consequences of LithiumSpill in UWMAK III Containment ........................... 10

    2.1 Cross-Sectional View of NUWMAK ........................... 13

    2.2 Top View of NUWMAK ....................................... 14

    2.3 Pb-Li Phase Diagram ...................................... 16

    2.4 Effects of Lithium Concentration in a Lithium-LeadBreeder on Shielding Requirement and Tritium Breeding .... 18

    2.5 Estimated Tritium Inventory in Alternative BreederBlankets for 3000 MWth Reactor ........................... 19

    2.6 Phase Diagram for LiAl System ............................ 23

    2.7 Impact of Structural Material Content (316 StainlessSteel) on Tritium Breeding ............................... 27

    2.8 Cross-sectional View of NUWMAK Blanket ................... 32

    2.9 Schematic of the Blanket and Shield for NUWMAK ........... 34

    3.1 Equilibrium Final Temperature Profiles for VariousBreeders in Static Calculation ........................... 41

    4.1 Internal Blanket Accident Option Heat Flow Diagram ....... 44

    4.2 Internal Blanket Accident Option Node Structure .......... 48

    4.3 Lithium Breeder Thermal Response to Water Interactions ... 57

    4.4 Li7Pb2 Breeder Thermal Response to Water Interactions .... 58

    4.5 LiPb4 Breeder-Thermal Response to Water Interactions ..... 59

    4.6 LiAl Breeder Thermal Response to Water Interactions........60

    4.7 Li2O Breeder Thermal Response to Water Interactions ...... 61

    4.8 Comparison of Reaction Zone Temperature Profilesof the Various Breeders .................................. 64

    4.9 Comparison of First Breeder Element TemperatureProfiles of the Various Breeders ......................... 66

  • -7-

    LIST OF TABLES

    No page

    2.1 Reactions of Li-Pb Alloys and Lithium with Water ....... 20

    2.2 Summary of Favorable and Unfavorable Features ofLithium-Lead Breeders .................................. 22

    2.3 Summary of Favorable and Unfavorable Features ofthe Water-Cooled Blanket Concept ....................... 28

    2.4 Summary of Structural Material Assessment for theWater-Cooled Blanket Concept ........................... 29

    2.5 Physical Properties of Ti-6-4 .......................... 31

    2.6 Major Features of NUWMAK Design ........................ 35

    2.7 Summary of Important Blanket Parameters ................ 36

    4.1 Breeder - Coolant Reactions of Interest ................ 50

  • -8-

    CHAPTER 1. INTRODUCTION

    Advancements in plasma physics research, together with a growing

    concern for the risks of energy production in the public sector, has

    led to an increasing number of detailed fusion safety studies. Topics,

    including routine and accidental releases of tritium, activation of

    structural material by neutron bombardment, and the consequences of

    lithium fires, are currently under various degrees of investigation.

    The findings of these studies are incorporated in subsequent fusion

    reactor designs, answering some questions and creating still more.

    This work is the product of a research program whose objective is

    to minimize the potential problems of a lithium-based blanket for fusion

    reactors. Such a blanket is practically forced upon us by the choice of

    a D-T fuel mixture for first generation fusion power plants [1]. The

    needed tritium is bred via the reactions:

    6Li (n,T) 4He + 4.8 MeV

    7Li (n,n'T) 4He - 2.5 MeV.

    Initially, natural lithium (92.58% 7Li, the rest 6Li), a liquid at

    operating blanket tenperatures, was the primary candidate for blanket

    breeder and/or coolant materials, due to its excellent breeding and heat

    transfer qualities, effectiveness in neutron moderation and relatively

    low pumping power need as compared to other liquid metals [2]. However,

    with time and study, serious disadvantages in the use of liquid lithium

    emerged.

  • -9-

    Pure lithium is highly reactive with air, water and concrete; all

    materials that will be in abundant supply in the reactor environment.

    Experimentation at the Hanford Engineering Development Laboratory (HEDL)

    and computer modelling studies at MIT using the computer code LITFIRE

    (to be discussed in more detail later in this report) indicate that

    temperatures and pressures in the reactor containment area, in the event

    of a sizable lithium spill, can attain critically high values [3].

    Figure 1.1 shows such a possibility. Such an event could provide a pathway

    for release of tritium or structural activation products, providing a

    hazard to plant personnel or the outside world.

    This problem and others, including corrosion, difficulties in tritium

    recovery, and magnetohydrodynamic instabilities [4], have led designers

    to consider alternative materials for fusion blankets. Among such

    considerations are lithium-lead alloys.

    This report will provide a preliminary analysis of lithium-lead

    alloys for use as breeding materials from the safety point of view. While

    it is thought that these materials provide less of a hazard than the use

    of liquid lithium, little has been demonstrated. Thus, there is the need

    to formulate some framework for a comparison.

    Before actual calculations can be made, a basis must be established.

    The NUWMAK reactor design by the University of Wisconsin (1978) was chosen

    for this purpose, due to its use of Li62Pb38 eutectic as the tritium

    breeder. The primary hazard here involves interaction between the lithium-

    lead alloy breeder and the boiling water coolant, inside the blanket.

    Specifics of this design are further discussed in Chapter 2.

  • -10-

    1250-

    1000 Pool

    750-

    CelIGas

    0750

    250

    Stee

    Li .e

    0 2 4 6 8 10 12

    TIME (10 3 sec)

    Figure 1 .1 LITFIRE predictions for consequences of lithiumspill in UWOAK III containment (Reference 3) .

  • -11-

    Using this basis, two separate. studies are performed. The first is

    a static calculation: the breeder and coolant are allowed to interact

    immediately and the subsequent equilibrium final temperature of the blanket

    materials is determined. This is presented in Chapter 3. The second

    study is a dynamic calculation, using LITFIRE, of the temperature

    histories at various points in the blanket, if some accident allows breeder

    and coolant to come into contact. This is presented in Chapter 4. It

    should be stressed that in both studies, the values obtained are not

    sufficient evidence in themselves. Rather, these values must be compared

    with similar calculations employing the use of pure lithium. In this

    way, a measure of the relative hazards of the alternate breeders can be

    assessed.

  • -12-

    CHAPTER 2. BLANKET DESIGN BASIS DESCRIPTION

    2.1 Introduction

    NUWMAK, a conceptual thermonuclear reactor designed by the Fusion

    Engineering Program of the University of Wisconsin in March 1979, is one

    of a number of second generation studies aimed at maximizing the strengths

    of fusion while minimizing the weaknesses. This work builds upon the

    findings of a number of first generation designs aimed at identifying

    the important problems of fusion power.

    The design philosophy of this study was to search for an "end

    product that has the potential to be reliable, maintainable, environmentally

    acceptable, and reasonably economic [4]." To do this, a number of changes

    were made to the preceeding reactor concept, UWMAK III, including: an

    increase in the magnetic field to increase power density, a simplification

    of design to facilitate maintainence (as well as eliminate large cost

    items), the selection of structural materials to minimize resource

    requirements and costs, and a change in blanket breeder and coolant

    materials to reduce thermal fatigue and thereby increase reliability.

    The resulting structure is shown in Figures 2.1 and 2.2

    The new elements in blanket breeder and coolant materials are of

    particular interest to those concerned with fusion safety studies.

    Utilized in NUWMAK are: (a) Li62Pb38 eutectic for the breeding material,

    used because its melting point is very near the blanket operational

    temperature and thus, the latent heat of melting can provide energy

    storage, and (b) boiling water for the coolant, the "perfect choice,"

    discarded previously with the presence of pure lithium as the breeder.

  • -13-

    I-

    U,0:

    _jCL L)

    'TC ..

    U)IL

    a.

    m0j

    Ix ..... .

    00J

  • -14-

    TOP VIEW OF NUWMAK

    INNER SUPERCONDUCTIVEBLANKET OH COILS

    TUNGSTEN

    EDDY ZONECURRENTSHIELD

    - NORMAL COPPEROUTER .TF TRIMMING COILSBLANKET

    CENTRALSTRUCTURALCYLINDER -.RF CAVITY

    -L GRAPHITE- -REFLECTOR

    - / FIXED SHIELD

    VACUUM-

    REMOVABLE SHIELD

    SUPERCONDUCTIVE D MOU- TABL CRYOGENICTF COILS

    Figure 2(Reference 4 )

  • -15-

    A preliminary survey of the hazards of lithium-lead alloys indicates

    that interaction with water is by far the more severe problem, as these

    materials are relatively inert in air. NUWMAK, in addition to its use

    of Li62Pb38, provides an opportunity for the breeder and coolant to come

    into contact, specifically a breach in the cooling system inside the

    blanket. Thus, NUWMAK is the logical first choice for a basis for an

    investigation of the relative safety of the lithium-lead alloys.

    2.2 Breeding Materials

    2.2.1 Lithium-lead alloys

    The lithium compound selected as the tritium breeding material must

    satisfy many requirements. It must have desirable neutronic and irradia-

    tion characteristics, chemical stability at blanket operating temperatures,

    and be compatible with other blanket materials. More importantly, the

    compound must breed and release tritium at sufficient rates to fuel the

    reactor, yet limit the tritium inventory in the blanket to reasonable

    1 'vels.

    Lithium-lead compounds are interesting materials. Figure 2.3 shows

    the phase diagram of a Li-Pb two component mixture. However, beyond Li7Pb2'considered the most attractive lithium-lead alloy for breeding purposes,

    little else on the subject of Li-Pb physical properties is certain.- -An

    accumulation of data relevant to this study through a literature search

    and "data synthesis" is presented in Appendix A.

    Two neutronic characteristics of the lithium-leads, breeding cabability

    and long-lived activation products, have been studied. In the latter only205 Pb presents any problem in the long term unless significant amounts of

    impurities exist. This is not expected to be serious [4]. Breeding

  • -16-

    IU Pb2

    7260C IG

    LiPb

    48 2 C C 4

    - - 177 0 C

    -IF

    20 40ATOM

    PHASE

    60-% Li

    80

    K

    100

    DIAGRAM

    Figure 2.3

    (Reference 4)

    800

    700

    C.)

    2

    LLII"

    60c

    50C

    40C

    300

    200

    l000

    Pb - Li

    I i I

  • -17-

    capability depends on the amount of lead present.

    Li7Pb2 has been examined in detail and exhibits an excellent breeding

    property. This is due to the presence of lead, which acts as a neutron

    multiplier. Figure 2.4 shows the effect of lithium concentration in the

    lithium-lead breeder on the total breeding ratio. The total bulk shield

    thickness required to protect toroidal field coils is shown for reference.

    It is evident that a reduction of the lithium concentration will cause a

    substantial loss of fuel multiplication. However, the reduction of lithium

    also tends to enhance magnet protection by virtue of more effective nuclear

    radiation shielding by the added lead [5].

    A diffusion study by Wiswall [6] shows that the soluability of tritium

    in Li-Pb is much lower than that in pure lithium, as the activity of lithium

    is very low due to the presence of lead. Thus, the tritium inventories can

    be much smaller, tritium diffusivities relatively higher, and tritium

    recovery much easier. Specifically, Fig. 2.5 shows that Li7Pb2 has the

    lowest inventory of any of a number of proposed breeders. A problem here

    could be the fact that Li7Pb2 becomes a "chunk" at high temperature. This

    would increase the diffusion path of tritium and make recovery difficult [4].

    A more serious problem of the lithium-leads involves their compati-

    bility with the blanket environment. All react to some extent with water.

    Table 2.1 shows the results of experimentation to investigate this at

    Argonne National Laboratory. It can be seen that Li-Pb alloys can react

    vigorously with water, more so at elevated temperatures. However, a

    significant result is that Li17Pb83 exhibited only moderate reaction with

    water. Also, insufficient hydrogen was evolved by the alloy reactions

    to attain ignition conditions, unlike the case with liquid lithium.

  • -18-

    S1M1 3

    0 1-- 0 i

    '10) j) 0)09 6103a 05

    04

    03

    02

    Of

    00 10 20 30 40 so 60 70 60 10 1O

    L:ITMIU CONCENTIOATI0,. %

    Figure 2.4 Effects of lithium concentration in a lithium-lead breeder on shielding requirement andtritium breeding (Reference 5).

    I

    U

    2

    p

    ft

    U

  • -19-

    650 600 550

    TEM. *C

    500 450 4003.5

    3.01

    0 2.5F-

    wz- 2.0

    CD1.5

    0

    1.0

    0.5I.C

    I 1 .1 I I

    -

    ~~~~1

    0

    0Li20 LI.Pb2

    L.At

    0

    C

    1.1 1.2 1.3 1.4 1.5 1.6

    10 K/T

    Figure 2.5 Estimated tritium inventory in alternativebreeder blankets for a 3000 1lth reactor(Reference 9).

    300I I

  • -20-

    TABLE 2.1

    Reactions of Li-Pb Alloys and Lithium

    with Water

    (Reference 7)a Injected under water

    Sample

    WaterCase Composition State Temp/*K Ter-p/*K Reaction

    1 Li7fpb2 s 773 298 Modest

    2 Li7Pb2 s 773 369 Vigorous

    3 Li7Pb2 s 873 368 Vigorous

    4 Li7Pb2 L 1103 36S Very Vigorous

    5 Lio. 62 Pbo. 3 8 L 773 368 Vigorous

    6 Li0 .17Pb0 .8 3 z 773 368 Very modest

    7 Li z 773 368 H2 Detonation

    8 Lia Z 773 368 Detonation

  • -21-

    In all reactions, LiOH (melting point at 470 'C) is formed. Liquid

    LiOH is an extremely corrosive substance and would degrade the integrity

    of the activated structural materials [7]. Fortunately, Li-Pb is relatively

    inert in air. It was reported [8] that "LiPb (50-50 mixture) resembles Pb

    in every respect except density. LiPb would not ignite, even when exposed

    to the flame of a gas-air torch." Therefore, though a Li-Pb - H20. reaction

    could be very serious, it is not expected to be as severe as an accident

    involving pure lithium. Table 2.2 provides a summary of the advantages

    and disadvantages of the lithium-lead alloys.

    2.2.2 Alternative Breeders

    For completeness, LiAl and Li20, also candidates for the tritium

    breeding material, will be analyzed with regard to safety in this study.

    Other strong candidates, specifically Li2SiO 3 and LiAl0 2, have been ignored

    in this study since they have no appreciable reaction with water.

    LiAl is in many ways akin to Li7Pb2, such as a similarity in reactivity

    with water. However, the latter material is preferred by designers due

    to a superior tritium breeding capability. This is because there is a

    lower lithium-atom density in LiAl and no neutron multiplier, with the

    absence of Pb. Tritium extraction characteristics are also poorer than

    that of Li7Pb2 [9]. The primary activation product is 26Al, more of a

    problem than 205Pb. Physical properties of this breeder are also

    unexplored and are discussed in Appendix A. The phase diagram is shown

    in Fig. 2.6.

    Li20 has a marked advantage over the lithium-lead alloys in the matter

    of reaction with water. Because it is in oxide form, this compound does

    not evolve hydrogen upon reaction and produces less heat [9]. It is

  • -22-

    TABLE 2.2

    Summary of Favorable and Unfavorable Features of

    Lithium-Lead Breeders

    Lithium-Lead Alloys

    Advantages

    1. High breeding ratioattainable

    2. Probably less reactivewith water than liquid Li

    3. Tritium recovery appearsfeasible with low-pressurehelium

    4. Lead helps shield magnets

    Disadvantages

    1. Poor technology base:high degree of uncertaintyin properties

    2. Reactive with water coolant

    3. High blanket weight

    4. Uncertain radiation damageeffects

    5. Uncertain tritium releasemechanism

    6. Requires blanket changeoutduring reactor life

    7. Activation product: 205Pb

  • -23-

    800

    700

    600

    So-So

    400

    300

    S2} 456 8

    - S

    0. or (At

    7/

    I

    ---

    .17 _1001____ ___

    0At.

    .0 20

    WEIGHT PER CENT LITHIUU1', 2A 25 30 40 5 0 7D BO 90

    * REF 5

    o*Y. *

    601

    t

    3D 40 50 60 70 SO s 10D30 iC PE E5 H0 __:_ss_____s

    ATOMIC PER CENT LITHIUM L.

    Figure 2.6 Phase Diagram for LiAl System.(Reference 9)

    2

  • -24-

    therefore expected that the use of this breeder will not pose a major safety

    problem. However, Li20 has fallen into disfavor because it has a high

    lithium-atom density. This, combined with a poor diffusion rate, leads to

    excessive tritium inventories. Physical properties of this breeder are

    also discussed in Appendix A.

    2.3 Coolant

    Many -factors affect the choice of coolant. Unique in power production

    to fusion is the interrupted burn cycle of the plasma. This produces

    the problem of thermal fatigue in the first wall and blanket, caused by the

    fluctuating temperature of these structures with the plasma burn cycle.

    The temperature change is a combination of three effects:

    1. Coolant temperatures rise, Tcout-Tcin

    2. Film temperature drop, Twall - Tc (=Q/h)

    3. Temperature difference across the first wall, AT= Q X/k [4].

    While the third effect depends on structural materials, the first two can

    be greatly reduced by choice of the proper coolant, one which has a small

    coolant temperature rise that simultaneously provides a large heat transfer

    coefficient. This describes a boiling liquid and the first logical

    choice is boiling water.

    A considerable technology has been developed through the years for

    the use of water as a coolant in energy production. There exist many

    advantages. Water is an excellent heat-transfer fluid, costs little and

    is readily available. It is easy to pump and is non-corrosive with

    conventional structural materials.

  • -25-

    It is interesting to note, however, that up to this point, few

    designers have considered water for the primary coolant. There exist a

    number of concerns and questions including neutronics, tritium, and safety

    considerations. In addition, the use of a boiling water or steam coolant

    will require high pressure containment. The NUWMAK design calls for

    cooling water at 300 *C and 8.6 MPa (1250 psi). This poses additional

    design and safety problems.

    The safety concerns of a water-cooled blanket have been discussed.

    It should be noted that this problem effectively prohibited the use of

    water as a coolant until alternative breeders to lithium were suggested.

    Even so, current designs using water stress the use of strong cladding

    materials for coolant channels.

    High-integrity cladding is also the prescription to minimize

    tritium diffusion into the cooling water. Tritiated water is a safety

    hazard and recovery of the tritium is difficult and expensive. However,

    recent studies using permeation rates for stainless steel cooling tubes

    show tritium losses could be less and 1 Ci/day, assuming the formation of

    oxide films inside the tubes [9]. Irregardless, it is obvious that the

    coolant loop cannot be used for tritium recovery, necessitating some

    recirculation of the breeder.

    The necessity of avoiding contact between breeding materials and

    coolant tends inherently, to increase structural material content in the

    blanket. From a neutronics point of view, this increase tends to degrade

    the tritium breeding ability, due to increased parasitic neutron

    absorption. However, the strong neutron slowing-down power of water

    improves breeding performance by increasing the 6Li (n,T) 4He reaction

    rate for low energy neutrons. This decreases parasitic absorption by

  • -26-

    the structural materials [5]. Therefore, proper design and choice of

    materials can leave the tritium breeding capability of a water-cooled

    blanket virtually unchanged.

    Figure 2.7 shows this phenomenon for various breeders, with 316

    stainless steel used as structural material. It is important to note

    that the addition of water significantly improves the breeding ratio in

    the Li7Pb2 , more so than the other breeders. This is due to reduced

    parasitic absorption in lead as well as the stainless steel.

    Table 2.3 summarizes the advantages and disadvantages of the

    water-cooled blanket concept. Chief among the assets is the use of

    available technology in its construction. The major liabilities appear

    to be the safety problem and limited choices in compatible breeding and

    structural materials. Further study in both areas is necessary before

    a final decision can be made.

    2.4 NUWMAK Blanket Design

    2.4.1 Structural Materials

    Many structural materials have been considered for a water-cooled

    blanket design, including: austenitic stainless steel, high nickel alloys

    and selected titanium, vanadium and niobium alloys [9]. Table 2.4

    summarizes an assessment of these candidates with regard to properties

    associated with the blanket environment.

    One of the liabilities of the water-cooled design is apparent. The

    vanadium and niobium materials, which respond well to neutron bombardment,

    are eliminated due to water corrosion problems. Also noted is a general

    lack of data regarding the compatibility of these structural materials

    with the lithium-lead alloys. Since decomposition of these alloys is not

  • -27-

    1.8

    1.7 - WITHOUT W.TER15 v/a Hs IN LI Pb2 a LizO

    LIP ---- WITH WATER (10-15 v/o)1.6 0-5 v/o He IN LiTpz IN

    BREEDER BLANKz-T: 0.8 m1.1 50 %SS+- 50 % SC SHIEL.D: 0.2

    .0 1.0 to5 15 20

    STAINLESS-STEEL VOLUME. %

    Figure 2.7 Impact of Structural Material Content C316 SS)on Tritium Breeding (Reference 6).

  • -28-

    TABLE

    Summary of Favorable and

    the Water-Cooled

    2.3

    Unfavorable Features of

    Blanket Concept

    Water Coolant

    Advantages

    Excellent heat-transferfluid

    Well-developed technologybase

    Low cost and readilyavailable

    Relatively low temperature(-.320 *C) operation

    Compatible with conventionalstructural materials

    Low pumping power need

    Enha'nces tritium production

    Liquid at room temperature

    1.

    2.

    3.

    4.

    5.

    6.

    7.

    Disadvantages

    Highly reactive with candidatebreeding materials

    Reaction product (LiOH) is verycorrosive

    Requires high-pressurecontainment

    Cannot be used for tritiumrecovery

    Expensive to remove tritium fromH20 (safety)

    Water tends to be a sink fortritium

    Nb and V, candidate structurematerials are incompatable

    1.

    2.

    3.

    4.

    5.

    6.

    7.

    8.

  • -29-

    TABLE 2.4

    Summary of Structural Material Assessment for the

    Water-Cooled Blanket Concept

    Rating numbers defined as follows:

    Compares favorably with other candidate structural materials.

    Limits operating life but probably acceptable under certainconditions. -

    Little data available but may be a libit4in factor.

    Probably not viable for conditions of interest.

    Rat ing

    Property Requirement Fe Ni Ti V Nb

    Bulk Radiation Effects 2 2 ? 1 1

    Compatibility with H20 1 1 1 4 4

    Compatibility with Liquid Li 3 5 3 1 1

    Compatibility with SolidLi20 and Li 7Pb2 3 3 3 3 3

    Compatibility with H(DT)Environment 1 1 3 -1 .1

    *

    1.

    2.

    3.

    4.

    I

  • -30-

    desirable, this question should be studied.

    The NUWMAK design utilizes Ti-6Al-4V alloy for the first wall and

    coolant tube material due to its high strength-to-weight-ratio, good

    fatigue resistance, fabricaility, low long term residual activity and

    well established industry [4]. Physical properties of this alloy are

    shown in Table 2.5. The NUWMAK shield is more conventional, primarily

    B4C.

    2.4.2 Mechanical Design

    The blanket of NUWMAK is shown in Fig. 2.8. The blanket structure

    is Ti-4A1-4V which operates at a temperature of approximately 350 *C.

    The coolant is boiling water at 300 *C.and 1250 psi. The breeder is

    Li62Pb38 eutectic, operating at approximately 400 *C. The design life

    for each blanket module is two years.

    The blanket is divided into eight modules in the reactor. Each

    module is fed and discharged coolant and breeding materials separately.

    There are two blanket units- in each module; the inner blanket near the

    machine axis and the outer blanket, as seen in Fig. 2.8. These two units

    are completely separate from each other.

    The first wall consists of a continuous bank of tubes running in the

    vertical direction. Beyond this, the blanket is cooled with rows of

    vertical tubes on a triangular pitch. The spacing between rows of tubes

    is progressively increased towards the back of the blanket to account for

    the radially decreasing nuclear heating [4]. Radial struts are spaced at

    20 cm intervals, reinforcing the first wall against the hydrostatic

    pressure of the breeding material, which fills the space between the

    coolant tubes.

  • -31-

    TABLE 2.5

    Physical Properties of Ti-6-4

    Atomic Weight

    Melting Point

    Mass Density

    Yield Strength

    Modulus of Elasticity

    Yield-to Weight Ratio

    Thermal Condcutivity

    Coefficient of Thermal Expansion

    Heat Capacity

    45.9

    1668 *C

    4.4 g/cm3

    530 MPa

    85 GPa

    120 N-m/g

    .12 W/cm-K

    10 x 10-6/OC668.8 J/kg-K

  • T BREEDING MINLET

    Al

    NNERBLANKE

    BREEDINGMATERIALOUTLET COOLANT

    OUTLET

    T

    ,---FIRST WALLCOOLING TUBES

    0

    Figure 2.8 Cross-Sectional Viewi of Blanket (Reference 4) .

    -32-

    COOLANINLET TERIAL

    OUTERBLANKET

    3 meters2

    i

  • -33-

    At the blanket's edge is a thin graphite reflector. Beyond this is

    a shield to protect the cryogenic magnet coils. The shield is primarily

    B4GC, operating at approximately 150 *C. Figure 2.9 shows a schematic

    diagram of this system.

    2.4.3 Summary of Important Parameters

    The major features of the NUWMAK design are given in Table 2.6. In

    addition, important blanket parameters pertinent to this study are given

    in Table 2.7. These values are used where appropriate in subsequent

    calculations.

  • -34-

    SCHEMATIC OF THE BLANKET ANDFOR NUWMAK

    SHIELD

    SHIELD

    -JBREEDG

    D .A IG

    2 1 13.75 5 9 102.9 3.35 3.95 6.4 6.9 7.95

    COLD HOT BREEDING GRAPHITESHIELD SHIELD ZONE REFLECTOR SHI

    3.5%Ti alloy 4%Ti alloy 5.7%Ti alloy 3.5%Ti.alloy 3.5%

    95.25% B4C 93% W 89.4% Pb Li 95.25% C 95.250%

    1% H 2 0 2% H20 3.7% H20 1% H2 0 1%

    0.25% Pb I % Pb 1.2% Pb 0.25% Pb 0.25%

    meters

    ELD

    ri alloyB4C

    Pb

    Figure 2.9(Reference 4)

    6k-

    41-

    2k

    I I

  • -35-

    TABLE 2.6

    Major Features of NUWMAK Design

    Power

    Total Thermal PowerNet Electric Power

    Plasma

    Major RadiusMinor RadiusPlasma Height to Width Ratio (b/a)Plasma CurrentToroidal Beta

    neTE

    q(a)

    2283 MWth660 MWe

    5.13 m1.13 m1.647.2 MA6%

    2 x 101 4 cm- 3-sec

    2.64

    Magnet

    On-Axis Toroidal FieldToroidal Field at NbTi ConductorStabilizerNumber of Toroidal Field CoilsNumber of Cu Trim Coils

    6.05 Tesla11.5 TeslaAl uminum816

    Blanket

    Structural MaterialCoolantBreeding Material

    Average Neutron Wall Loading

    Titanium AlloyBoiling WaterLi62Pb384.34 MW/m2

  • -36-

    TABLE 2.7

    Summary of Important Blanket Parameters

    Plasma Burn TimePlasma Down Time

    225 sec20 sec

    Coolant TemperatureCoolant PressureTotal Coolant Flow RateTotal Coolant Tube

    Surface Area

    Heat Transfer Coefficientof Boiling Water

    Coolant Tube ODCoolant Tube IDN. Tubes in Outer BlanketModule

    Pitch Length

    Space for Breeder inOutside Blanket Module

    Breeder TemperatureShield Temperature

    300 *C8.6 MPa1500 kg/sec

    4350 m2

    20000 Btu/hr-ft2- OF

    1.3 cm1.0 cm

    475

    12 cm

    17.72 m3

    400 *C150 *C

  • -37-

    CHAPTER 3. EQUILIBRIUM Tf CALCULATION

    3.1 Introduction

    Lithium-lead alloys are considered less of a safety hazard due to

    the presence of lead, which is thought to slow down the water reaction,

    decrease the heat of reaction and help absorb what heat is released.

    However, a number of physical properties are altered with the addition

    of lead. Since most of these properties have direct bearing on an

    interaction with water, the consequences of such an interaction are not

    directly predictable.

    For this reason, a preliminary analysis of the Li-Pb - H20 reaction is

    performed using a static calculation. In this case, the breeder inside

    one blanket module is allowed to interact completely with varying amounts

    of the water available to that module. Assuming the heat of reaction is

    contained within the blanket, the equilibrium temperature of the reaction

    products, unreacted breeder and blanket structural materials is then

    determined.

    Such a scenario is unrealistic, but this calculation is important

    for two reasons. First, it serves as a reference for further study.

    Second, with its assumptions, such a calculation may indicate the

    maximum attainable bianket temperature in a particular module in the case

    of an internal blanket water interaction.

    3.2 Assumptions and Methodology

    The outer blanket section of an individual module is chosen for

    consideration. The inner blanket section contains only a nominal amount

    of breeder and the consequences of an accident in that section do not

  • -38-

    appear as severe. Data from the NUWMAK design (Table 7.H.2) indicates

    that an outer blanket module contains 38.4 tonnes of titanium structural

    material, 106.0 tonnes of graphite and 17.7 m3 of space to contain the

    breeder. Therefore, the amount of breeder present can be determined with

    knowledge of the density.

    The initial temperature of breeder and graphite is 400 *C. The

    structural materials are at a temperature of 350 *C and the coolant is

    at 300 *C and 1250 psi. The reaction between breeder and coolant is

    assumed to be immediate and complete at 400 *C, the heat of reaction

    helping to raise the water temperature to that point. The heat of reaction

    can be determined using:

    AHr = AH 5 + ZAHprod - EAHreact, cal/g breeder (3.1)

    where AH2 5 is the standard heat of hydrolysis at 25 'C and AHprod and

    AHreact are the enthalpy changes of reaction products and reactants,

    respectively, as they are heated from 25 *C to 400 *C.

    The amount of coolant water available to the outer blanket module

    can be determined by analysis of NUWMAK's steam generating unit. In this

    respect, NUWMAK is very much like a fission boiling water reactor [4].

    Examination of the Dresden BWR reveals that the total coolant volume in

    the 3411 MW th plant's cooling system is 11,695 ft3 [10]. Scaling this

    down to NUWMAK's 2283 MWth output and assuming the average density of

    water in the coolant loop to be 62.37 lb/ft 3 (an overestimate), it can be

    shown that approximately 15,260 pounds of water are available to

    interact with the breeder in one module.

    ---------- -

  • -39-

    It is assumed that a fixed percentage of this -cooling water interacts

    with the breeder. Thereafter, no loss of heat is allowed from the

    blanket. The resulting final equilibrium temperature can be calculated

    using the expression

    T f= T 0 + R (3.2)(Ms~s + Mb'b + ZMRi Ri

    where Tf = final equilibrium blanket temperature

    T = initial blanket temperature

    QR = reduced heat of reaction

    Ms = structural mass

    Mb = remaining breeder mass after reaction

    MR = reaction product mass after reaction

    C = mean specific heat for each component

    Reaction products include hydrogen gas, LiOH and the alloy element.

    A proper evaluation of the M C. terms in the above equation varies

    with each component. For example, LiOH is evaluated above its melting

    point as

    M LiOH [s(T mel t- To)+ AHmel t L(Tf-Tmelt) (MLiOH LiOH T T (3.3)

    where Cs = mean solid specific heat of LiOH

    CL = mean liquid specific heat of LiOH at 470 *C

    AHmelt = heat of melting for LiOH at 470 'C

    Tmelt = melting point of LiOH (470 *C)

  • -40-

    Similar expressions can be written for the other components.

    The reduced heat of reaction can be written as

    QR = xMc [ao AHR ~c (T - T )] - MTi CTi (To - T i), (3.4)

    where Mc = mass of total available- coolant

    M = mass of titanium structural material

    Cc = mean specific heat of coolant

    CTi mean specific heat of titanium structural material

    Tc = coolant temperature

    TTi = titanium structural material temperature

    x = fraction of available coolant reacting

    ao = reaction stoichiometric combination constant

    This is done to raise the coolant and titanium alloy structure to the

    initial blanket temperature of 400 *C.

    3.3 Results and Discussion

    Figure 3.1 shows the resulting equilibrium blanket temperatures for

    the various breeders under consideration, plotted against the reacting

    percentage of available water. A number of interesting results are noted.

    First, as expected, the pure lithium breeding blanket reached the

    highest temperature upon reaction with water. The dotted line signifies

    that with a high percentage of available water reacting, some of the

    unreacted lithium will begin to vaporize at a temperature also close to

    the melting point of steel. This indicates a potential for further

    problems if a steel blanket liner is used.

  • -41-

    TEMPERA

    URE

    C

    ±1450

    1300

    1±50

    1000

    700

    550

    400

    0.25 0.50 0.75 1.00

    PERCENTAGE OF AVAILABLE H20 .REACTING

    Figure 3.1 Equilibrium Final Temperature Profiles forVarious Breeders in the Static Calculation.

    Li

    LiAl

    Li Pb

    -.- - Li2

    - -

  • -42-

    Li7Pb2 and LiAl are very much alike. Though lower equilibrium

    temperatures are exhibited than those of the pure lithium breeder, the

    difference is not very large to be significant. At low percentages of

    reacting available water, there is no difference.

    Li20 and LiPb4, on the other hand, appear to be significantly "cooler"

    than the pure lithium case. In the case of Li20, the key difference is a

    very low heat of reaction with water. LiPb4 , with a relatively high

    density, is the only case in which there exists more available water

    than breeder. Thus, a limited heat of reaction and large residue of

    lead leads to reduced equilibrium temperatures.

    I- -I

  • -43-

    CHAPTER 4. DYNAMIC CALCULATION USING LITFIRE

    4.1 Introduction

    Though valuable as a reference, the calculations of Chapter 3 have

    little to do with a plausible internal blanket breeder-coolant interaction.

    It is incorrect to assume that these materials will react instantly at a

    constant temperature; it is imprudent to declare that the flow of cooling

    water will cease and that all heat will be retained within the blanket

    perimeter. Clearly, a dynamic formulation is needed.

    To this end, the LITFIRE computer code is modified to estimate the

    thermal response of the NUWMAK blanket to possible accidents. In this

    modification, called the internal blanket accident option, the breeder and

    water react in a zone located in the middle of the breeder mass. The

    leakage of water into this "reaction zone" is determined by the number of

    broken coolant tubes, set small enough to justify the assumption that

    this is the limiting effect on the reaction rate. The heat of reaction

    is transferred to the breeder mass by conduction and free convection, to

    the blanket liner and shield by further conduction, and out of the

    blanket via forced convective cooling by unbroken coolant tubes. Figure

    4.1 shows the heat flow diagram for this system.

    It is hoped this model presents a truer picture of what will happen

    within the blanket in the event of a cooling system leak. Again, due to

    uncertainties concerning data and some assumptions, this study can only

    provide a measure of relativt safety, compared with the trials

    utilizing liquid lithium.

  • -44-

    7Heatof REACTION ZONE ;G4onvec ve

    Reaction Cooling

    Free Convection Conduction

    FIRST BREEDER ELEMENT CoolingCooling

    - Conduction

    BREEDER SECOND BREEDER ELEMENT ) ConvectiveZONE C Cooling

    4'Conduction

    FINAL BREEDER ELEMENT ConvectiveCooling

    Conduction

    LINER

    Conduction

    SHIELD

    Figure 4.1 Internal Blanket Accident Option Heat FlowDiagram.

  • -45-

    4.2 LITFIRE Description

    LITFIRE is a computer code developed at MIT [11] to predict the

    consequences of a hypothetical lithium spill in a fusion reactor

    containment. It was first written in 1977 as a mofidication of the

    Argonne National Laboratory code SPOOLFIRE, used to model the conse-

    quences of sodium fires. LITFIRE was later modified and improved in

    1980 [3], utilizing the experimental results of small-scale lithium

    spill tests performed at the Hanford Engineering Development Laboratory.

    In this code, the flow of heat is traced from the lithium reaction

    zone source to reactor containment components, and eventually out to

    the ambient. This system is simulated by a nodal network in which

    each node has a heat capacity and temperature equal to that of its

    physical counterpart. Heat flows between nodes are calculated using

    standard heat transfer correlations.

    To provide the reactor containment thermal and pressure response,

    LITFIRE solves a set of coupled heat and mass transfer equations.

    This is done by using the method of finite differences for the spacial

    dimensions, and either Simpson's rule or a Runge-Kutta method in the

    time domain [3]. Properties are computed at each time step from the

    integral equation

    t

    Y(t) = Y(t0 ) + dt' dY/dt',

    where the rates of change dY/dt are given for each node by finite

    difference solution of the heat transfer relations.

  • -46-

    4.3 Internal Blanket Accident Option

    4.3.1 Assumptions and Structural Model

    The internal blanket accident option models an accidental inter-

    action of coolant water and lithium-based breeder in the center of an

    outside blanket module. This interaction is caused by a breach of

    several neighboring coolant tubes, while the reactor as a whole undergoes

    normal operation.

    It is assumed that this event is undetected, thus assuring

    continuance of the plasma burn and coolant recirculation. It is felt

    that the three monitored parameters relevant to an accident of this

    type, namely bulk breeding material temperature, coolant temperature,

    and coolant flow rate, will not change appreciably until later stages

    of the accident.

    The reaction rate is immediate and limited by the leakage of water

    into the breeding material. The leakage rate, dictated by the number of

    broken coolant tubes, is set very low, 0.6 kg/sec (three broken tubes),

    to make this assumption reasonable. Although there is a suspicion

    that the water reaction rate of the lithium-lead alloys is slow at low

    temperatures, no data exists. It is also assumed that the reaction

    zone pressure at high temperatures does not significantly retard the

    leakage rate of water into the zone.

    The reaction zone is very difficult to characterize. However,

    certain assumptions can be made. First, the zone can be considered

    spherical, as boiling water at 8.6 MPa will disperse equally in all

    directions upon tube rupture. The reaction zone must be large enough

    to accomodate the influx of breeder and coolant, thus the zone radius

  • -47-

    should be large compared to the coolant tube pitch length. However, to

    accomodate the assumption that the water reiction is instantaneous, the

    reaction zone volume should be small, compared to that of the blanket

    module.

    The initial radius of the reaction zone for three ruptured coolant

    tubes is set at one foot. This is over six times the characteristic

    distance separating the three coolant tubes in question. The volume

    of this zone is less than 2% of the total blanket volume. This seems

    reasonable for the small leakage rate. Further research in this area

    would aid the accuracy of the model.

    The reaction products (LiOH and alloy element, if any) remain in the

    reaction zone, thus increasing the radius of this zone with time. The

    heat capacity of this expanded zone is calculated summing the products

    of the individual heat capacity of each component multiplied by the

    weight percent.

    The nodal structure of this system is shown in Figure 4.2. It can

    be seen that the reaction zone and breeder mass a.re broken into a number

    of sections. This is to more accurately account for heat transfer by

    conduction. The number of sections in each zone is selected so as to

    keep the element widths to approximately 6 inches. These elements

    increase and decrease in width with time in the reaction zone and

    breeder zone, respectively, as the reaction zone expands.

    The blanket elements are spherical, like the reaction zone, to

    facilitate computation. The outer element is therefore irregularly

    shaped to account for the NUWMAK geometry. This is not expected to

    create any difficulty, as it is doubtful that much heat will be

  • -48-

    -a--.

    N

    "S

    N'

    REACTIONa *

    ZONE L-' ,i1

    'S

    -'p..

    7,

    '5-

    N, *.

    '.5' *\'S .5

    \ 5.

    '~ *\~) . . . 0 0I

    / i/

    I /5, I

    5/ . S

    //

    5-

    //

    /

    I

    7/'

    BREEDER ZONE

    SHIELD

    ,L IN ER

    Figure 4.2 Internal Blanket Accident OptionNode Structure.

  • -49-

    transferred to this region. For completeness, the steel liner and

    B4C shield are also monitored in the code. The conduction of heat is

    assumed to stop at the far edge of the shield.

    The heat of reaction is distributed evenly throughout the reaction

    zone, heating the reactants and reaction products. Heat is removed by

    conduction and free convection to the breeder zone, and via forced

    convection by unbroken coolant tubes as shown in Fig. 4.1. The surface

    area of cooling tubes in each element is calculated as a volume

    percentage of the total.

    Finally, it should be noted that the densities and thermal

    conductivities of the lithium-lead alloys and other alternate breeders

    are held constant with temperature in this analysis. As discussed in

    the appendix, this data has only been determined at one temperature.

    Rather than increase uncertainties with various correlations, the values

    are unaltered.

    4.3.2 Heat Transfer Mechanisms

    A. Heat of Reaction

    All of the alternate breeders considered in this study react to

    some extent with water. Table 4.1 shows the reactions of interest.

    Other reactions also take place, such as the production of Li202, but

    are discarded as they play a very minor role. For exampl.e, the peroxide

    is unstable above 250 'C [11] and is not produced above that temperature.

    Reaction occurs at the reaction zone temperature Tcz' The heat

    of reaction can be calculated using

    AHR H25 + AHrod - EAHreact ,e Btu/lb breeder (4.1)

  • -50-

    TABLE 4.1

    Breeder-Coolant Reactions of Interest

    AHhyd

    (kJ/g-atom of Li)

    Li + H20 - LiOH + 1/2 H2 205

    1/7 Li7Pb2+ H20 + LiOH+ 1/2 H2 + 2/7 Pb 200

    LiPb4 + H20 + LiOH + 1/2 H2 + 4Pb 170

    LiAl + H20 LiOH +1/2 H2 + Al 200

    Li20 + H20 + 2LiOH 64

  • -51-

    where HO5 is the standard heat of hydrolysis at 25 C and AHprod and

    AHreact are the enthalpy changes of the reaction products and reactants,

    respectively, as they are heated from 25 *C to Tcz'

    Since the reaction is immediate, limited by the leakage of water

    into the reaction zone, the reaction rate is the leakage rate. This

    can be written as

    R = NT lb H20/sec (4.2)

    where m is the mass flow rate of water through one tube and NT is the

    number of ruptured tubes. Thus, the total heat generation rate inside

    the reaction zone can be given by

    Q = a0 AHR m NT BTU/sec (4.3)

    where a is the stoichiometric combination constant for the breeder

    and water in the given reaction.

    B. Sensible Heat Addition to Reactants in the Reaction Zone

    A portion of the heat of reaction is used to heat the inflowing

    coolant water and breeder to the reaction zone temperature. This can

    be written as

    Qs =NTi w cw (Tcz- Tc) + rb cb (Tcz- T ) BTU/sec (4.4)

    where m w is the mass flow rate of water in a coolant tube

    c w is the mean specific heat of the coolant

  • -52-

    m b is the mass influx of breeder to the reaction zone

    Cb is the mean specific heat of the breeder

    Tc is the coolant temperature

    TL is the bulk breeder temperature.

    In this case. the influx of breeder into the reaction zone is

    considered equal to the leakage rate of the coolant into the zone, as

    reaction is immediate . This mass transfer is further discussed in

    the free convection section.

    C. Forced Convective Cooling

    Forced convection, due to the continued coolant recirculation

    through undamaged tubes, is an important heat transfer mechanism.

    Because only a small number of the 475 coolant tubes in an outside

    blanket module are damaged, cooling will take place in both the

    breeding and reaction zones. The cooling tube surface area in each

    element can be determined as a volume percentage of the blanket as

    a whole. For example, the initial reaction zone, approximately 2%

    of the blanket by volume, comes into contact with roughly 2% of the

    total cooling tube surface area. This total area can be determined

    using the information in Table 2.7.

    This total heat flow can be computed for each element using

    Qc + (T - Tc) BTU/sec (4.5)k TiAso hA J

    where 6 is the coolant tube thickness

    kTi is the thermal conductivity of the titanium alloy

  • -53-

    A s is the outer coolant tube surface area

    AsI is the inner coolant tube surface area

    h is the boiling water heat transfer coefficient

    T. is the bulk temperature of the element in question.

    D. Conduction

    Conduction plays a major role in the transfer of heat from the

    reaction zone to the breeder mass. The heat conduction term between

    two elements can be expressed'as

    Qcondij = Ai (Ti - Tj)/d 1 j BTU/sec (4.6)

    where A is the inner element surface area

    k is the inner element thermal conductivity

    k is the outer element thermal conductivity

    T is the inner element bulk temperature

    T is the outer element bulk temperature

    di. is the separation distance between the elements.

    The surface area assigned to each element is at its outer

    perimeter. In the above expression, it is assumed that the inner

    element is at a higFier temperature, as is the case at all times in

    the LITFIRE option.

    E. Free Convection

    A preliminary order of magnitude analysis indicates that the

    free convective enhancement to conduction is Pr Gr 1 /2, where Pr and

    Gr are the Prandl and Grashof numbers. For a 400 'C temperature

  • -54-

    difference between the reaction and breeder zones in the lithium case,

    this enhancement is better than a factor of ten. Thus, free convection

    is an important mode of heat transfer in the model.

    As mentioned before, there will be mass transfer in the breeding

    zone due to the influx of this material into the reaction zone. It is

    this movement that allows convective cooling of the reaction zone by

    the first breeder zone element.

    Given the spherical shape of the reaction zone, the semi-empiracle

    relation

    Fi = 2.0 + 0.60 Gr1/4 Pr1/3 (4.7)

    is useful to find the average heat transfer coefficient for Grl/2

    Prl/ 3 < 200. NIII is the average Nusselt number and is related to theaverage heat transfer coefficient him by

    Nu =h m L/k (4.8)

    where L, the characteristic distance, is in this case the reaction zone

    diameter.

    Thus, the heat flow due to free convection can be described by

    Q'c AczDkb (2.0 + 0.60 Gr1/4 PrT/3 )( T 4.9)D cz- L sec

    where Acz is the reaction zone surface area and kb is the bulk breeder

    thermal conductivity. Gr = D3p2gaAT and Pr - C2 k are applicable to

  • -55-

    the fluid breeders.

    F. Radiation

    Using an order of magnitude analysis, the radiative heat flow is

    related to the conductive heat flow by

    grad T3L Q (4.10)

    where a is the Stefan-Boltzmann constant. At 1500 OF, this radiative

    heat flow is a factor of ten less than that of conduction in a lithium

    breeder. Therefore, radiation is neglected in the model.

    4.3.3 The Numerical Scheme

    The temperature of a thermal element may be found from the solution

    to

    mc t = q+ + q3 + ... , T = T0 at t = to, (4.11)

    where mc is the element's heat capacity and ql, q2' q3 ... are heat

    flows into the element, shown in Fig. 4.1. This may also be expressed

    as

    T ( +q 2 + q 3 + ... ) dt +T. (4.12)

    t0

    In LITFIRE, this is expressed as

    T = INTGRL (T , dt/dt). (4.13)

  • -56-

    A set of sub-routines is used to perform the integrutions using

    either Simpson's Rule or a Runge-Kutta method.

    For example, heat flows into the reaction zone are the heat of

    reaction, sensible heat addition to the reactants, conduction, free

    convection and forced convective cooling. Therefore, the temperature

    of the reaction zone at time t can be determined in LITFIRE by using

    Eq. (4.13) and

    dT lQQ Q- Q1 (4.14)dtQ - Qs ~ QcR ~ condRL

    where the subscript R'denotes the reaction zone and Li denotes the

    first breeder element. Q, Qs' QcR' QcondRL1, and Q can be determined

    using Equations (4.3), (4.4), (4.5), (4.6), and (4.9), respectively.

    Similar equations can be written for each thermal element in the model.

    4.4. Results and Discussion

    Figure 4.3 shows the thermal response of the reaction zone (TCZ),

    first breeder element (TLIl) and middle breeder element (TLI4) over the

    first 1000 seconds for a lithium breeder accident, as described earlier

    in this chapter. Similar graphs are plotted in Figures 4.4 through 4.7

    for Li7Pb2, LiPb 4, LiAl and Li20 breeders, respectively. A number of

    interesting points are noted.

    First, the general shapes of the curves in each case are similar,

    although different maximum temperatures are attained. A change of time

    step shows no appreciable difference. The reaction zone ri.ses rapidly,

    reaching a maximum value within the first two minutes of the coolant

    tube breaks. Thereafter, the temperature decreases monotonically,

  • -57-

    TCZ

    - T L I4

    100 200 300 400 SO 6ee 7ee see goo e0eTIME (SECONDS)

    Figure 4.3 Lithium Breeder Thermal Response to WaterInteraction.

    aiee

    1900

    1700TEM IseePER 1300ATU 1.±00R

    E 00

    700

    see

    300

  • -58-

    19ee

    1700

    T 1500EMP 1300ERAT 1100URE 900

    F

    700

    500

    300

    T C Z ~

    T L 11TL14

    100 200 300 400 500 600 700 800 900 1000

    TIME (SECONDS)

    Figure 4.4 Li Pb Breeder Thermal Response to HaterInter ction.

    I

  • -59-

    TEMPERATURE

    1700

    1500

    1300

    1100

    900

    '- 700

    see

    300

    100 200 300 400 500 600 700 800 90 1000

    TIME (SECONDS)

    Figure 4.5 LiPb4 Breeder Thermal Response to L'aterInteraction.

    TCZ

    TLIl

    - TL14

    I

  • -60-

    1700 - -

    Ti'ee

    EMP 1300 TCZER

    1100

    URE 90 ___ TITLIl

    700 - L14

    see --

    300

    100 200 300 400 500 600 700 800 900 1000

    TIME (SECONDS)

    Figure 4.6 Li,'.1 Breeder Thermal Response to VaterInteraction.

  • -61-

    1300

    T.E 1100MPERA goo

    URE 700

    500

    300

    100 200 300 400 500 600 700 800 900 1000

    TIME (SECONDS)

    Figure 4.7 Li C Breeder Thermal !esponse to UaterInteraction.

    TCZ

    TL14- TLI4 -

    - -I I I I I I I I

  • -62-

    more gradually as time progresses. The first blanket element exhibits

    similar behavior, but at lower temperatures and lagging over a minute

    behind. The middle blanket element is relatively unchanged, slowly

    increasing 50 OF in the lithium case and nearly constant in the

    alternate breeders.

    This behavior may be due to different characteristic times for the

    various heat transfer processes. The heat of reaction in the reaction

    zone is instantaneous and relatively large compared to the conductive

    and convective flows, thus a rapid initial rise. Eventually, as the

    temperature difference between the reaction zone and first breeder

    element increases, so do the conductive and convective flows and the

    temperature profile flattens and decreases. Thereafter, as this

    temperature difference decreases, the reaction zone temperature decreases

    more gradually. This continues until the breeder (or water, in the LiPb 4case) is depleted, eliminating the heat of reaction. Thereafter, all

    zones are eventually recooled to 752 *F. The first 1000 seconds are

    shown as the entire process takes upwards to 11 hours (4 x 104 seconds).

    The relatively small volume of the reaction zone (less than 2% of

    the blanket module volume) may account for both the high temperatures

    attained in the reaction zone and the large temperature difference

    between this zone and the first breeder element (approximately 1000 *F

    in the lithium run). A small volume implies a small mass and surface

    area. The small mass is very sensitive to the heat of reaction and the

    small surface area impedes conductive and convective flows out. As

    the reaction zone expands, this effect is diminished.

  • -63-

    The blanket liner, shield and other breeder elements were also

    monitored. All zones outside of the fourth breeder element showed

    no significant change. Thus, the accident appears to be effectively

    localized. The second and third breeder elements showed similar

    behavior as the first, with progressively shorter time lags.

    Figure 4.8 presents a comparison of the reaction zone temperature

    profiles for the various breeders. As expected, the liquid lithium

    breeder produces the highest temperatures. Also expected, using the

    results of Chapter 3 as reference, is that the Li20 breeder temperatures

    are significantly less. This breeder has a definite safety advantage

    compared to pure lithium.

    The same can not be said, however, of the lithium-lead breeders

    and LiAl. Though less, the resulting temperatures are well within the

    range of the lithium case, as close as 70 OF (Li 7Pb 2 ) and not further

    apart than 250 OF (LiPb4). These differences are insignificant at a

    base temperature of 1950 *F.

    This result was surprising in the case of LiPb 4. Equation (4.14)

    indicates that the temperature rate of change in the reaction zone is

    inversely proportional to the reaction zone mass. Since the reaction

    zone volume is initially fixed and there is a factor of 20 increase

    in the density of LiPb4 over that of Li (at 400 *C, the density of Li

    3 3is 0.51 g/cm ; the density of LiPb 4 is 9.9 g/cm ), it was felt that the

    temperature rise would be proportionally decreased.

    However, a closer look at Eq. (4.14) indicates that the temperature

    rate of change is also inversely proportional to the reaction zone

    specific heat. In this case, the specific heat of LiPb4 , approximately

  • -64-

    200 300

    TIME (SECONDS)

    400 500

    Figure 4.8 Comparison of Rleactor Zone Temperature Profilesof the Various Breeders

    21ee

    iee

    1700

    Isee

    1300

    1100

    TEMPERATURE

    F

    Li

    -LiAl Li Ph 2

    Li 0

    -. I

    900

    700

  • -65-

    that of Pb, i-s nearly a factor of 20 less than that of pure lithium

    (at 400 *C, the specific heat of lithium is 1.01 cal/g- *F; that of

    LiPb4 is 0.041 cal/g - 'F). Thus, the terms in the denominator of

    Eq. (4.14) effectively cancel each other out and the slightly different

    reaction zone temperature profiles of Li and LiPb4 are simply a

    reflection of the slightly different heats of reaction of the two

    breeders with water.

    A comparison of the thermal responses of the first breeder elements

    for the various breeders, shown in Fig. 4.9, is also interesting.

    Again, the lithium case produces the highest temperatures and the Li2O

    case produces the lowest. The lithium-lead alloy and LiAl results are

    again similar. Here the Li7Pb2 element is cooler overall due to a very

    low thermal conductivity, experienced in the lithium-lead system at

    a 20% lithium atom percentage [13]. However, in this comparison, the

    differences between these alloys and the lithium case are more pronounced.

    This indicates that the use of liquid lithium.will produce more wide-

    spread accidental consequences.

  • -66-

    1109

    ieeeTEMPER SeeATURE

    F 800

    700

    100 200 300 400 500 600 700 800 s00 1000

    TIME (SECONDS)

    Figure 4.9 Comparison of First Breeder Element TemperatureProfiles of the '!arious Breeders.

    Li 2

    I I I * I I I

  • -67-

    CHAPTER 5. CONCLUSIONS AND RECOMMENDATIONS

    Results indicate that the lithium-lead alloys may not be signifi-

    cantly safer than pure lithium as a fusion reactor breeding material,

    utilizing the NUWMAK geometry. In both calculations, short term

    temperatures resulting from interaction of Li7Pb2 and LiPb4 with water,

    though lower, are within a few hundred degrees of those associated with

    the use of liquid lithium.

    However, a proper conclusion to this study is that a conclusion

    cannot yet be made. The calculations of Chapters 3 and 4 provide an

    overview of the safety question, raising some interesting observations

    and determining areas that need to be explored in more detail.

    First, the lithium-lead alloys and LiAl can pose safety problems

    approximate to those of liquid lithium, as noted above. This can be

    quite serious, as shown in Chapter 3, with temperatures reaching to

    the melting point of steel in a water-cooled blanket. For this reason

    alone, further study of these alternate breeders is required.

    Results of. Chapter 4 indicate that such an interaction could go

    undetected, as a continuance in coolant recirculation may keep the

    consequences localized. Measurable quantities, like bulk breeder

    temperature and coolant temperature and flow rate a're practically

    unperturbed. Thus, further design work might include features to

    mitigate this problem.

    Uncertainties in characterizing the reaction zone in the dynamic

    model render the resulting temperature profiles less meaningful. Further

    work in this area, perhaps experimental, would make the model more

    accurate.

  • -68-

    Finally, better physical properties data on the alternate breeders

    is required. In particular, an understanding of the water reaction

    rates is central to the study of these materials. If it can be proved,

    as surmized, that these rates are significantly lower than those of

    liquid lithium, a significant reduction in safety hazards may be

    assured.

  • -69-

    REFERENCES

    1. A. J. Impink, Jr. and W. G. Homeyer, "Tritium Regeneration inProposed Fusion Power Reactors," Transactions of the AmericanNuclear Society, S(l): 100, June 1962.

    2. J. L. Ballif, et al., "Lithium Literature Review: Lithium'sProperties and Interactions," HEDL report TC-1000, January, 1978.

    3. Mark S. Tillack, "Development and Verification of the LITFIRE Modelfor Predicting the Effects of Lithium Spills in Fusion ReactorContainments," Master's Thesis, MIT, June 1980.

    4. B. Badger, et al., "NUWMAK", University of Wisconsin, UWFDM-330,March 1979.

    5. "Special Purpose Materials - Annual Progress Report," DOE/ET-0095,May 1979.

    6. R. H. Wiswall and E. Wirsing, "Tritium Recovery from Fusion BlanketsUsing Solid Lithium Compounds," Radiation Effects and TritiumTechnology for Fusion Reactors Conference, Gatlinburg, Tenn., 1975.

    7. R. G. Clemmer, et al., "Assessment of Solid Breeding Blanket Ophonsfor Commercial Tokamak Reactors," ANL-CEN/205, 1980.

    8. N. A. Frigerio and L. L. LaVoy, "The Preparation and Properties ofLiPb, A Novel Material for Shields and Collimators," NuclearTechnology, 10, 322, 1971.

    9. D. L. Smith, et al., "Fusion Reactor Blanket/Shield Design Study,"ANL/FPP-79-1, July 1979.

    10. "Dresden Nuclear Power Station Units 2 and 3, Safety Analysis Report,"Commonwealth Edison Company, 1968.

    11. D. A. Dube and M. S. Kazimi, "Analysis of Design Strategies forMitigating the Consequences of Lithium Fire within Containment ofControlled Thermonuclear Reactors," MITNE-219, July 1978.

    12. R. Bird, W. Stewart and E. Lightfoot, Transport Phenomenon, JohnWiley & Sons, Inc., 1960.

    13. Marie-Louis Sabourgi, et al., "Thermodynamic Properties of aQuasi-ionic Alloy from Electromotive Force Measurements: The Li-PbSystem," The Journal of Chemical Physics, 68, 4, February 15, 1978.

    14. John H. Perry, et al., Chemical Engineers' Handbook, McGraw-HillBook Company, Inc., 1963.

  • -70-

    APPENDIX A

    Physical Property Data

  • -71-

    Table A.1 summarizes the important physical property data of the

    various alternate breeders analyzed in this report. Except as indicated,

    all of these values are gathered from the previously identified

    references. It is important to realize that, aside from the lithium

    and melting point data, all numbers are estimates at best.

    For reasons detailed earlier, only the physical properties of the

    lithium breeder are allowed to vary with temperature in calculations

    of Chapters 3 and 4. The correlations used are:

    p = 0.5368 - 1.0208 x 10~ 4T (g/cm3 )k = 10.48 + 4.98 x 10- 3 (T- 180.6) -0.58x10- 6 (T-180.6) 2

    (cal/sec-m-*C)

    c = 1.0037 - 0.01063x + 0.00564x2 - 0.001279x3 (cal/g *C)

    where x = .004938T - 6.20741

    Here, p = density of lithium

    k = thermal conductivity of lithium

    cp = specific heat of lithium

    T = lithium temperature in *C

    The latent heats of melting for the alloy breeders are determined

    using the correlation

    Hmelt/Tmel t " 2.2

    This is an average value for metallic alloys [14].

  • -72-

    The thermal conductivity of LiPb4 is estimated with the correlation

    km = k1w1 + k2w2 - 0.72(k 2 - k1)(w w2)

    This is appropriate for a binary liquid mixture. Here, the weight

    fraction w2 refers to the component having the larger value of k [14].

    The specific heat data of the alloy breeders is determined using

    the relation

    C, Xi c +XcACalloy Li CLi + XA CPA

    where XLi = weight fraction of lithium

    XA = weight fraction of the alloy element

    cpA = specific heat of the alloy element

    c =Li specific heat of lithium

    The specific heat values for the alloy elements, lead and aluminum,

    can be found in the literature.

  • -73-

    TABLE A.1

    Summary of Physical Properties of Candidate

    Breeding Materials at Standard Conditions

    Lithium Li7Pb2LiPb 4 LiAl Li20

    Properties

    Melting Point, *K

    AHmelt, cal/g mole

    Density, g/cm 3

    Li atom density, g/cm3

    Thermal conductivityw/m-k

    Specific Heat cal/g OK

    Heat of Reactionwith Water

    g-atom Li

    Atomic weight

    453

    722.4

    0.51

    0.51

    50

    1.01

    245

    7

    999

    2200 a

    4.59

    0.49

    \20

    0.14b

    200

    463

    508

    1120a

    9.9

    0.08

    ,'35 a

    973

    2140 a

    1.76

    0.37

    30

    0. 04 1b 0.44b

    170c

    835

    200

    1970

    2.01

    0.93

    1.73

    0.35

    64

    34 30

    correlation

    interpolated value

    ~estimated

    a.

    b.

    c.

  • -74-

    APPENDIX B

    Complete.Listing of LITFIRE

  • -75-

    00w

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  • -76-

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  • -77-

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  • -78-

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  • -79-

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  • -80-

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