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PLENTIFUL ENERGY The Story of the I
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Copyright © 2011 Charles E. Till a
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CONTENTS FOREWORD .................
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CHAPTER 10 APPLICATION OF PYROPROCE
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FOREWORD On a breezy December day i
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CHAPTER 1 ARGONNE NATIONAL LABORATO
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even now is straining the limits of
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with events and time. Till saw the
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it, I saw how a national laboratory
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Figure 1-2. West stands of the Stag
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development of nuclear power for ci
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depended on U.S. ability to maintai
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construction funding kept increasin
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faced a nightmarish combination of
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concept in the next decade.) In sti
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was based on EBR-I experience, but
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Figure 1-9. Experimental Breeder Re
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Figure 1-11. Rendering of the EBR-I
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performance. But the decision had b
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its shakedown in early years it jus
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sense primarily a commercial power
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without electrical generation, the
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Its purpose was to demonstrate the
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of each period, which the managemen
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CHAPTER 2 THE INTEGRAL FAST REACTOR
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A line had been pursued that the re
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The IFR refining process also produ
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director of Argonne a year or two b
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eporting on nuclear power developme
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A few weeks later, the mid-term ele
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2.6 Summary In late 1983, the line
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Argonne would be. My Ph.D. at Imper
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I had worked at the United Kingdom
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hadn‘t bothered us with it. But t
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But I had gone over and over the on
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laboratories.‖ Incidentally, late
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Argonne by this time was one of sev
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3.1.2 Life at the Laboratory in the
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An anecdote: In the cooperative arr
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Cycle Facility‖ went. We pushed i
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(LMFBR), which assumed a very rapid
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the pool was a settled issue; it wa
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During the early stage of the IFR p
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scientific work, not on non-essenti
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e generally held, even as facts inc
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cf per day from Canada via pipeline
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serious, and it is made more seriou
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global economy. The LWR, and the Ad
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supply 11%, and one, the world‘s
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Fatih Birol, has recently been quot
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gas production of little use in the
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expenditures during a decade starti
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thousand tonnes in one large increm
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But the principal line of developme
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Tar sands and oil shale recovery ar
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14. W. H. Ziegler, C. J. Campbell,
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Argonne had been a part of the deve
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Breaches or holes in the fuel cladd
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waste. For efficiency in uranium us
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Further, as a metal, sodium does no
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to the boundaries and many leak fro
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is debatable, it remains our belief
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CHAPTER 6 IFR FUEL CHARACTERISTICS,
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To do this, an extraordinarily simp
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Further cementing the decision was
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the AEC, but the reactor operation
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hands-on access needed to accomplis
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temperature. However, a very substa
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It turned out that the high-plutoni
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In the column ―Pu content % heavy
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40 start-ups and shutdowns 5 15% ov
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During casting, a partial vacuum (1
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is in fact a new fuel. Plutonium-ba
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8. G. L. Hofman and L. C. Walters,
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characteristics necessary for this.
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exchangers, and the steam generator
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experiments, as mentioned; this has
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sufficient to allow radioactive rel
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In the IFR, this loss of the coolin
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Figure7- 2. Reactor outlet temperat
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for thermal expansion of heavy stru
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power to shut down power is basical
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criticality. The debris is in the f
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7.10.2 The EBR-I Partial Meltdown T
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7.11 Licensing Implications What ar
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The sodium flowing into the steam g
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[15] Provisions are also made to co
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disassembly comes, it is with a rea
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CHAPTER 8 THE PYROPROCESS In the ne
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EBR-II purposes, and it established
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valuable fuel constituents, uranium
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and materials and it had been renam
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The first operation is done in the
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into the receiver crucible. The hea
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In the final step, the pins are arr
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Spent Fuel Processed, kg effective
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products, highly radioactive and se
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its own bayonet-style partial inter
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If the bond sodium along with the s
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CHAPTER 9 THE BASIS OF THE ELECTROR
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Whether or not a given reaction can
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9.3 Kinetics of the Reactions Chemi
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The exponential exp((E f -E b )/RT)
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The electrorefining process brings
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cathode operation. Once the solutio
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Table 9-2. Measured data and calcul
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All four measurements show that eve
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The free energy of the reaction of
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2. At an actinide chloride ratio of
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CHAPTER 10 APPLICATION OF PYROPROCE
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10.2 Electrolytic Reduction Step 10
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The pyrochemical process simply sup
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Figure 10-1. Electrolytic reduction
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The distribution of fuel constituen
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an electrorefiner with a 5001,000 k
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aqueous reprocessing plant. The eco
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Li metal at the cathode. Lithium me
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4. D. W. Dees and J. P. Ackerman,
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Our intent for the IFR technology w
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dose to any member of the public mu
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IFR process, as we shall see, does
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Relative Radiological Toxicity uran
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doses from Tc-99 and I-129 equilibr
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Fraction of Initial Actinide, % pro
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long-lived fission products and tra
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to decay to the point where they co
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References 1. ―Nuclear Waste Poli
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12.1 Introduction Assessment of a p
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History provides empirical evidence
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program offered nations help with n
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Other nations are recycling their s
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uranium-233 cycle has been half-hea
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electrorefiner salt. And this, of c
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those concentrations in making the
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chance of ―pre-ignition‖ leadin
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It is now known that the plutonium
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12.8 Monitoring of Processes Always
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[18] In it he shows that with a spo
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Such a system tracks the quantity a
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weapons grade plutonium. Levels of
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12.13 Summary In IFR technology the
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12. T. P. McLaughlin, et al., ―A
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of concentration of uranium chlorid
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agreement with the measured ratio w
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eference 7. The important calculati
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as well. The numbers were obtained
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Run3: Plutonium isn’t, Uranium is
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The final actinide chloride ratios
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values of several of the constants
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HCDA HFEF HM HWR HTR IAEA ICRP IEA
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ABOUT THE AUTHORS Dr. CHARLES E. TI