ORNL-2106 - the Molten Salt Energy Technologies Web Site
ORNL-2106 - the Molten Salt Energy Technologies Web Site
ORNL-2106 - the Molten Salt Energy Technologies Web Site
Create successful ePaper yourself
Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.
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