05.08.2013 Views

ORNL-4191 - the Molten Salt Energy Technologies Web Site

ORNL-4191 - the Molten Salt Energy Technologies Web Site

ORNL-4191 - the Molten Salt Energy Technologies Web Site

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

14.1 DETERMINAT1ON OF OXIDE<br />

IN MSRE SALTS<br />

R. F. Apple J. M. Dale<br />

A. S. Meyer<br />

During <strong>the</strong> last week of December <strong>the</strong> moisture-<br />

monitor cell in <strong>the</strong> oxide apparatus became inop-<br />

erative. Because of o<strong>the</strong>r experiments being<br />

performed in <strong>the</strong> same hot cell, <strong>the</strong> moisture-<br />

monitor cell was not replaced until March. The<br />

insensitive cell showed sortie superficial evidence<br />

of radiation damage in that <strong>the</strong> potting compound<br />

(an KTV preparation which is used to seal <strong>the</strong> tube<br />

containing <strong>the</strong> spiral electrodes in a stainless<br />

steel housing) had shrunk and cracked. Flow<br />

checks revealed that substantially all <strong>the</strong> flow was<br />

still passing through <strong>the</strong> electrolysis tube, so that<br />

<strong>the</strong> damage to <strong>the</strong> potting compound could not have<br />

been responsible for <strong>the</strong> cell failure. Resistance<br />

measurements indicated that <strong>the</strong> failure was<br />

caused by ei<strong>the</strong>r removal of or some alteration to<br />

<strong>the</strong> P,05 electrolyte film.<br />

The analyses of oxide in radioactive salt samples<br />

from <strong>the</strong> MSRE for this period are summarized in<br />

Table 14.1.<br />

Two samples of radioactive fuel (IPSL-19 and<br />

IPSL-24), submitted from <strong>the</strong> In-Pile <strong>Salt</strong> Loop 2,<br />

were found to contain 265 and 240 ppm of oxide<br />

respectively. Sample IPSL-24 was stored under<br />

helium at 200°C for a period of about six mont.hs<br />

from <strong>the</strong> time of sampling until <strong>the</strong> analysis was<br />

made.<br />

14.2 DETERMINATION OF U3'<br />

IN RADIOACTlVE FUEL BY A HYDROGEN<br />

REDUCTION METHOD<br />

J. RI. Dale R. F. Apple<br />

A. S. Meyer<br />

A transpiration method is currently being used<br />

to determine thc + 0 concentration in molten<br />

radioactive MSRE fuel. The molten fuel is sparged<br />

with hydrogen to reduce oxidized species according<br />

to fie reaction<br />

MFrl + --<br />

n in<br />

- H, -+ MF, + (n - RZ)IIF ,<br />

2<br />

167<br />

Table 14.1. Oxide Concentrations of MSRE <strong>Salt</strong> Somples<br />

Sample<br />

Dattt Received Oxide Concentration<br />

(PPd<br />

FP-11-28 (fuel) 3-2 1-67 58<br />

FP-12-4 (flush) 6-17-57 11<br />

FP-12-18 (fuel) 7-1 1-67 57<br />

The rate of production of HF is a function of <strong>the</strong><br />

ratio of oxidized to reduced species in <strong>the</strong> melt.<br />

The <strong>the</strong>ory of <strong>the</strong> method has been described pre-<br />

viously.<br />

The computer program which was under develop-<br />

ment has been completed and permits <strong>the</strong> calcula-<br />

tion of expected IIF yields for any preselected<br />

reduction steps on any melt composition. Using<br />

<strong>the</strong> present fuel composition and <strong>the</strong> experimental<br />

conditions of <strong>the</strong> transpirat ion experiment as input<br />

data to <strong>the</strong> program, €IF yields were calculated for<br />

varying initial concentrations of 1J3 '. Sample<br />

concentrations of U3' were determined from <strong>the</strong><br />

comparison of <strong>the</strong> experimental and calculated WF<br />

yields. Table 14.2 shows <strong>the</strong> U3+ results obtained<br />

from <strong>the</strong> [IF' yields of <strong>the</strong> third and fourth reduction<br />

steps of <strong>the</strong> analyses and compares <strong>the</strong>m with ex-<br />

pected values calculated by W. R. Grimes.<br />

The calculated results assume that 0.16% of <strong>the</strong><br />

uranium in <strong>the</strong> fuel was origiiially present as U3 ',<br />

that <strong>the</strong> chromium concentration increase from 38<br />

to 65 ppm which occurred before <strong>the</strong> first sample<br />

was taken resulted in <strong>the</strong> reduction of U4' to<br />

U3 ', that each fission event results in <strong>the</strong> oxida-<br />

tion of 0.8 atom of U3', and that <strong>the</strong>re have been no<br />

o<strong>the</strong>r losses of u3 '.<br />

It will be noted that no analysis results are<br />

listed for samples FP-11-38 and FP-11-49. Although<br />

<strong>the</strong>se samples were run in <strong>the</strong> normal manner, a<br />

total of over 2000 micromoles of HF was evolved<br />

for <strong>the</strong> four hydrogen reduction steps fox each<br />

sample as compared with about SS micromoles for<br />

<strong>the</strong> previous runs. Since this increased HF yield<br />

coincided with an increase in activity in <strong>the</strong> traps<br />

used to collect <strong>the</strong> HF, it appeared likely that <strong>the</strong><br />

buildup in sample activity during <strong>the</strong> extended<br />

period of reactor operation might be responsible.<br />

which 'J. M. Dale, K. 17. Apple, and A. S. Meyer, MSR<br />

"n may be UF,, NiF2' FeF2' CrF2y<br />

Proprarn Sernrmn. Pro&. Rrpf. f'cb. 28, 1967, C>&jL-<br />

UF4 in order of <strong>the</strong>ir observed reduction potentials. 4119, p. 158,

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!