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ORNL-2106 - the Molten Salt Energy Technologies Web Site

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2.5. COMPATIBILITY OF MATERIALS AT HIGH TEMPERATURES<br />

PENETRATION OF GRAPHITE<br />

BY MOLTEN FLUORIDES<br />

H. J. Buttram G. F. Schenck'<br />

It appears very likely that graphite is <strong>the</strong> only<br />

reasonably effective reactor moderator material that<br />

will remain chemically stable upon direct exposure<br />

to molten fluoride fuel mixtures. The use of graph-<br />

ite to contain such fuel mixtures has been known<br />

fora long time to be practical for simple laboratory-<br />

scale experimental equipment. The graphite most<br />

commonly used for this purpose has <strong>the</strong> commercial<br />

designation C-18. However, little information is<br />

available concerning <strong>the</strong> rate of penetration of<br />

reactor-grade graphite by molten fluoride fuel mix-<br />

tures, and accordingly an investigation of this phe-<br />

nomenon has been initiated.<br />

Specimens of APC' graphite 1/4 x $ x \ in. were<br />

soaked at 6OOoc for various periods in sealed cap-<br />

sules of lnconel containing molten NaF-ZrF, or<br />

NaF-ZrF,-UF, mixtures under helium atmospheres.<br />

The specimens were <strong>the</strong>n sectioned and examined<br />

under <strong>the</strong> petrographic microscope. Prel iminary<br />

observations indicate that <strong>the</strong> APC graphite was<br />

completely penetrated by NaF-ZrF, (53-47 mole ?4)<br />

in 1 hr at 6OOOC but that NaF-ZrF,-UF, (53.5-40.0-<br />

6.5 mole 72) had not detectably penetrated <strong>the</strong><br />

graphite in 10 hr at 60Ooc. The rapid penetration<br />

of <strong>the</strong> graphite by <strong>the</strong> NaF-ZrF, melt is considered<br />

to be surprising, since such penetration is in con-<br />

trast to <strong>the</strong> stability of C-18 graphite in this and<br />

similar fluoride mixtures. O<strong>the</strong>r graphite5 of higher<br />

densitywjll be examined in <strong>the</strong>se and o<strong>the</strong>r fluoride<br />

mixtures. If necessary, attempts will be made to<br />

prevent penetration of <strong>the</strong> graphite by prior impreg-<br />

nation with high-melting-point materials such as<br />

NaF or CaF,.<br />

EFFECT OF ATMOSPHERE ON ANODIC<br />

DISSOLUTION OF NICKEL IN<br />

MOLTEN NaOH<br />

F. A. Knox<br />

An attempt has been made to study <strong>the</strong> efficiency<br />

of anodic dissolution of nickel in NaOH under<br />

various atmospheres and various conditions of cur-<br />

'On l assi nment from Pratt & Whitney Aircraft.<br />

Nationas Carbon Co. code designation.<br />

F. Kertesz<br />

PERIOD ENDING JUNE 10, 1956<br />

rent density and temperature. The apparatus con-<br />

sisted of a crucible of Morganite (recrystallized<br />

alumina) containing molten sodium hydroxide into<br />

which a nickel anode and a cathode, as well as a<br />

nickel <strong>the</strong>rmocouple well, were inserted. This<br />

electrolytic cell and its furnace were placed in a<br />

large chamber which could be evacuated or filled<br />

with <strong>the</strong> desired atmosphere. A lead storage bat-<br />

tery served as <strong>the</strong> power supply; <strong>the</strong> circuit also<br />

contained a voltmeter, ammeter, and ampere-hour<br />

meter, as well as rheostats to control <strong>the</strong> current<br />

density applied.<br />

When <strong>the</strong> assembled electrolytic cell was main-<br />

tainedat <strong>the</strong> desired temperature without an applied<br />

voltage, attack on <strong>the</strong> electrodes was negligible.<br />

Passage of current resulted in erosion of <strong>the</strong> anode<br />

and subsequent deposition of crystalline nickel on<br />

<strong>the</strong> cathode. The weight gain of <strong>the</strong> cathode did<br />

not correspond precisely to <strong>the</strong> weight loss of <strong>the</strong><br />

anode, since <strong>the</strong> crystalline deposit was not per-<br />

fectly adherent; in addition some sodium alumi-<br />

nate, formed by <strong>the</strong> reaction of NaOH with <strong>the</strong><br />

AI'O, of <strong>the</strong> crucible, apparently contaminated <strong>the</strong><br />

cathode deposit. Loss in 'weight of <strong>the</strong> anode was<br />

accordingly used to evaluate <strong>the</strong> efficiency of <strong>the</strong><br />

cell.<br />

The data shown in Table 2.5.1 were obtained at<br />

a current density of 2 amp/cm2. At this current<br />

density <strong>the</strong> cell efficiency is very poor under all<br />

conditions. The dissolution efficiency is decreased<br />

slightly by substituting hydrogen for helium as <strong>the</strong><br />

static cover gas and is reduced considerably by<br />

bubbling hydrogen through <strong>the</strong> molten electrolyte.<br />

TABLE 25.1. EFFICIENCY OF ANODIC<br />

- SOLUTIONS OF NICKEL IN NaOH<br />

Current density: 2 amp/cm<br />

600 0.65 0.42<br />

800 2.77 2.12 0.66<br />

125

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