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ORNL-TM-2180.txt
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< 'rj
-y
AT
l'l( *}
OAK RIDGE NATIONAL LABORATORY
operated by
UNION CARBIDE CORPORATION w
NUCLEAR DIVISION
for the
U.S. ATOMIC ENERGY COMMISSION
ORNL- TM-2180
DATE -March 26, 1968
ELECTRICAL CONDUCTIVITY OF MOLTEN FLUORIDES.
A REVIEW.
G. D. Robbins
NOTICE This document contains information of a preliminary nature
ond was prepared primarily for internal use ot the Oak Ridge National
Laboratory. It is subject to revision or correction and therefore does
not represent a final report.
ISTRECTON OF THIS GOUMET & UNKIMITER
LEGAL NOTICE —
This report was prepared as an account of Government sponsored work. Neither the United States,
nor the Commission, nor any person acting on behalf of the Commission:
A. Mokas any warranty or representotion, expressed or implied, with respect to the accuracy,
completeness, or usefulness of the information contecined in this report, or that the use of
any information, apporatus, method, or process disclosed in this report may not infringe
privately owned rights; or
B. Assumes any liabilities with respect to the use of, or for damages resulting from the use of
any information, apparaotus, method, or process disclosed in this report.
As used in the cbove, ‘‘person acting on bshalf of the Commission’' includes any employee or
centractor of the Commission, or employee of such contractor, to the extent that such employes
ot contrector of the Commission, or employee of such contractor prepares, disseminates, or
provides access to, any information pursuant to his employment or contract with the Commission,
or his empioyment with such contractor.
iii
ELECTRICAL CONDUCTIVITY OF MOLTEN FLUORIDES.
A REVIEW
G. D. Robbins
Reactor Chemistry Division
Oak Ridge National Laboratory
Oak Ridge, Tennessee
ABSTRACT/SUMMARY
A review of electrical conductivity measurements
in molten fluoride systems covering the period 1927 t?
1967 has been made, with particular emphasis on experi-
mental approach. It is pointed out that the common
practice of measuring resistance with a Wheatétone
bridge having a parallel resistance and capa01tanc?,
R_ and C_, in the balancing arm can result in cons;def-
agle error if the relation Rp = Rs[l + szcpz(znf) ] is
not employed in determing the solution resistance, Rs'
The frequency dependence of the measured resistance and
the practice of extrapolating measured resiétances to
infinite frequency versus 1/Nf is examined in térms of
electrode process concepts. A summary of experimental
approaches and results for 56 molten fluoride systems
is presented.
LEGAL NOTICE
Thia report was prepared as an account of Government sponsured work, Neither the United
States, nor the Commiagion, nor any person acting on behalf of the Commigsion:
racy, 1 ful
Privately owned rights; or
B. Assumes any liabilities with veapect to the use of, or for damages regulting from the
uge of any information, apparatus, method, or procesa disclosed in this report,
Ag uded in the above, ‘'person acting on behalf of the Commiaaton” includes any em-
ployee or contractor of the Commission, or emplovee of such contractor, to the extent thet
such employee or contractor of the Commisaion, or emplayee of suck contractor
disseminates, or provides access te, any information pursusnt to hig employment or contract
with the Commisalon, ar his employment with such contractoer.
A. Makes any warranty or Tepresentation, expresaed or implied, with respect to the acou-
or £ ot
of the ed ir this report, or that the yse
of any faformation, appargtus, method, or prucess disciosed {n this report may not infringe
Prepares,
ELECTRICAL CONDUCTIVITY OF MOLTEN FLUORIDES.
%*
A REVIEW
Introduction
Invesitgation of the electrical conductivity of molten
salt systems has been an area of lively research in recent
years, and a number of reviews have appeared which deal with
this aspect of transport phenomena.(1_3)
It will be the
intent of this review to limit itself to the subject of
conductance measurements in molten fluorides. The containment
problems encountered with these materials set them apart from
the other molten halides with respect to experimental diffi-
culties and the consequent precision of measurement which can
be expected. By limiting this review to fused fluorides, it
is hoped that sufficient details may be presented to permit
workers in the field to obtain a comprehensive survey covering
the period 1927 to 1967. To our knowledge, no such review
exists which addresses itself to the questions which we pose
below.
Many investigations in the past have been concerned with
cryolite-containing melts because of their relevance to the
aluminum inaustry, and a review of these systems has been given
(4)
by Grjotheim and Matiasovsky. Renewed interest in the trans-
port properties of fused fluorides in general has resulted from
their use as fuel, blanket, and coolant materials in molten
(5)
salt reactors.
*
Research sponsored by the U.S. Atomic Energy Commission
under contract with the Union Carbide Corporation.
Because of the high specific conductance of most molten
salts (1-6 Q71 cm_l),(é) experimental approaches have tended
(1),
to fall into two groups (1) use of capillary-containing
cells, which results in a cell constant of several hundred
cm !, the capillaries being constructed from electrically
insulating materials; or (2) use of metallic cells in which
the container is usually one electrode, with a second electrode
positioned in the melt. The latter type of cells have cell
constants of the order of a few tenths cm !, requiring very
accurate measuring bridges and determination of lead resist-
ances. Since the value of measured resistance in such cells
is less than 1@, errors due to temperature gradients, changes
in cell constant with temperature, and polarization become a
significant problem. Hence, cells of type (1) are clearly
desirable for use in molten salts. However, electrically
insulating materials for capillary construction which are
resistant to attack by molten fluorides are scarce.
Measurement of electrical conductivity in molten salts
differs from similar studies in aqueous solutions in several
significant aspects. It is often the practice to employ some
form of a Wheatstone bridge(7) (Figure 1) in which the two
upper arms are matchéd, standard resistances, and the imped-
ance of the cell in one lower arm is balanced by a variable
impedance, Z, in the fourth arm. The balancing impedance is
usually a variable resistance, Rp, and capacitance, Cp,
connected in parallel. The solution resistance, R and
S’
solution-electrode interfacial capacitances, Cs’ in the cell
(8)
are considered to be in series (Figure 2). By requiring
one electrode to have a much greater area than the other, the
impedance associated with such an electrode becomes negligible,
and the equivalent circuit reduces to that shown in Figure 3.
(Alternatively, one can employ electrodes of similar area and
treat the capacitance resulting from their series combination
as a single total capacitance, é— = %— + 6L .)
S @2
s
tance resulting from the electrode leads is in parallel across
The capaci-
the entire cell shown in Figure 2. However, at frequencies
ordinarily employed, and with some care in positioning, this
capacitance can be neglected.
When a sinusoidal alternating potential is impressed across
the cell, a sinusoidal alternating current results. If the
potential is insufficient to cause electrochemical reactions
to occur at the electrodes, the equivalent circuit of Figure 3
is valid, and the interfacial capacitance is charged and dis-
charged during each half-cycle through the solution resistance.
By employing an oscilloscope as the null detector, one can
balance the cell impedance with the parallel combination of Rp
and Cp showe in Figure 1. The two balance equations (when the
standard resistances are matched) are
R C
S P _
+ == =1 (1)
R_ Cg
and
2 =
RSRpCSCp(ZHf) 1 (2)
These may be combined into
= 1 2 2 2
R, R[1 + s (21f)2] (3)
It is often the practice to equate Rp ( the value of the bridge
dials) to RS (the true solution resistance).(g’lo) (In the case
of unmatched standard resistors, their ratio is used.) This
is usually valid in aqueous solutions where RS and CS are such
as to result in szcpz(ZHf)2 being negligibly smaller than
unity. However, in molten salts experimental conditions for
the measurement of electrical conductance can result in
considerable error if tfiese equations are not considered when
using parallel components in the balancing arm of a Wheatstone
bridge. For example, on rewriting equations (2) and (3) in
the form
1
R_ = Rs[l + E;ffi;??ifi;jf ] (4)
p
it is evident that in molten salts, where RS2 may be smaller by
*
a factor of 10! % that in aqueous solutions (CS having approxi-
(13))
mately similar values an awareness of these relations is
necessary.
Use of equation (3) to calculate R, is limited by the
accuracy with which the values of the variable capacitance,
Cp, and the frequency are known. Use of precision capacitors
can be avoided by employing a bridge in which the balancing
components are in series.(l4) Then in the case of no electro-
chemical reaction, the value of RS is well represented by the
reading on the balanced bridge; however, this method does
require the use of large capacitors.
When a sufficiently large a.c. potential is impressed on
the cell that charge is transferred across the solution-
electrolyte interfaces during part of each half-cycle, corres-
ponding to an electrochemical reaction, the situation becomes
considerably more complex. However, it is under these conditions
—%
The measured resistance of 0.0005 m KC1 in cells employed
by Jones and Bollinger(ll) was approximately 50,000 £. Cuthbertson
(12)
0.5 in molten cryolite.
and Waddington report a measured resistance of approOximately
that conductivity measurements are usually performed. Based
(15)
on the work of Jones and Christian, resistance in aqueous
systems is generally measured at a series of frequencies and
extrapolated to infinite frequency employing the functional
form f_%. Use of this particular functional form is attri-
buted(15) (16,17) (18)
to Warburg and Neumann who, on the basis
of Fick's laws of diffusion, predicted that the polarization
resistance (that part of the measured resistance due to elec-
trode polarization) was inversly proportional to NT.
Applying the concepts resulting from electrode process
studiesflg-?l) one may envision the equivalent circuit shown
in Figure 4 for an electrode-solution interface across which
charge is being transferred. {%?represents the impedance
associated with the reaction, which is in parallel with the
solution-electrode interfacial capacitance. Under the exact-
ing assumptions of faradaic impedance studies, zrnmy be re-~
presented by a frequency-independent resistance, 6, in series
with a frequency-dependent impedance, -W-, the Warburg imped-
ance. The latter is conveniently represented gg a resistance
and capacitance in series, Rr and Cr’ at constant frequency
(Figure 5). At a given frequency the impedances resulting from
R, and C, are equal., However, both vary as f_%.
The assumptions upon which the mathematical analysis
which results in f”% dependance oer and Efi%fi; rests include
1) semi-infinite linear diffusion of reactants and products
and 2) a small amplitude a.c. potential superimposed on a net
d.c. polarizing potential. These are not the conditions of
conductivity measurements. However, during that part of each
half-cycle during which reaction is occurring at the electrodes,
the equivalent circuit of Figure 4 is a useful concept, even
though Zr may not be treated rigorously according to Figure 5.
‘That the above considerations lead to the same frequency
dependence as that experimentally determined for many conduc-
tivity measurements(l59 renders this conceptual analysis
worth considering.
In brief, then, one may consider the equivalent circuit
of Figure 4 as a rough analog of the solution resistance,
electrode-solution interfacial capacitance, and reaction
impedance (bearing in mind that . cannot be represented
exactly by any finite combination of resistance, capacitance,
and inductance which will render it frequency independent).
During that part of each half-cycle in which the potential is
below that which results in an electrode reaction, the equi-
valent circuit of Figure 4 reduces to that of Figure 3, i.e.,
Zr becomes infinite. It is also useful to consider the equi-
valent circuit of Figure 4 in view of the practice of extra-
polating measured resistance to infinite frequency. It can
be seen that at infinite frequency the impedance of Cs is
infinitely less than that of Zr’ and Figure 4 again reduces
to Figure 3.
It should be emphasized that while one measures resist-
ance at a series of frequencies and extrapolates to infinite
frequency, one does not make measurements at frequencies
which approach infinity. In fact, very high fréquency measure-
ments (in the megahertz range) are to be avoided because of the
increased admittance of the leads and the fact that at very high
frequencies one ceases to measure a property assoicated with ionic
mobility and observes properties associated with dipole moments
and polarizabilities. Hence the question of concern remains
viz, what functional form of the frequency does one employ to
extrapolate the measured resistance to infinite frequency?
(22)
Robinson and Stokes consider this question in terms
of electrode process concepts as applied to aqueous media and
give balance equations for a bridge with a parallel-component
balancing arm, assuming various relative magnitudes of Rs’ o,
(15)
and Rr' Under the conditions employed by Jones and Christian,
1
f 2 dependence is predicted. Robinson and Stokes conclude that
one should measure resistance as a function of frequency and
extrapolate to infinite frequency in accordance with the observed
behavior. This is also the conclusion of Nichol and Fuoss,(23)
who observed a f ! frequency dependence of resistance in methanol
solutions.
In molten salts frequency dependence of the resistance has
been reported at polarizing potentials much lower than required
(24,25) (26)
for faradaic processes. Buckel and Tsaussoglou have
found that measured resistance vs. frequency plots show a plateau
in the range 10-100 kHz in adqueous potassium chloride and molten
potassium bromide. They suggest that extrapolation of resistance
1
vs. £ 2 would lead to erroneous conductances and that one should
study frequency dispersion in a particular apparatus and select
a frequency-independent region for performing conductivity
(27) reported that in molten nitrate
1
melts plots of measured resistance vs. f 2 were not linear, but
experiments. De Nooijer
approached linearity as the frequency approached infinity. His
values of measured resistance at 20 kHz only differed from values
extrapolated to infinite frequency by about 0.1 %. Winterhager
(28,29)
and Werner have considered frequency dispersion in molten
nitrate, chloride, and fluoride melts and have applied '"electrical
locus curve theory"(3o)
to their results obtained employing a
Thomson-type bridge. They conclude that at sufficiently high
frequencies measured resistance becomes independent of frequency,
and they employ a measuring frequency of 50 kHz., Therefore, in
this review particular attention will be given to the observed
behavior of resistance with frequency and to the condition of
the electrode surfaces, since in aqueous mdeia it is observed
that frequency dispersion is less in cases of heavy platiniza-
tion (increased CS).(ll)
In light of the foregoing discussion the following informa-
tion was sought from each study which was consulted:
A. Cell material, its general design, and the resulting cell
constant, (£/a), or general range of measured resistance,
iR} .
B. Electrode material, shape, size, and surface character.
C. Type of bridge employed.*
D. Frequency range employed.
E. Dependence of measured resistance on frequency.
F. Voltage applied to the bridge.
G. Results. Results are reported either in terms of the
The general types of bridge circuits employed are shown
in Appendix I as an aid in description. The circuits actually
employed were usually modified versions of those shown. For
details of circuity, the reader is referred to the cited work,
specific conductance, «, the equivalent conductance, qu,
or the molar conductance,‘Am. These quantities are defined
as
_ 1
kK = fi-(fl/a) (5)
eq _ equivalent weight
A - density (6)
m _ molecular weight
A « - density (1)
These quantities are reported as functions of temperature for
the minimum, maximum, and one intermediate value for pure salts.
For binary mixtures a 3 x 3 grid also stating the extremes and
one intermediate value of composition is employed where conven-
ient. Conductivities of mixtures of more than two components
are presented in a manner designed to convey maximum information.
The tabulation is ordered according to the system under
consideration; and within each system, by date of publication,
the earliest appearing first. Where one investigation has
covered several systems, a cross reference is given. Additional
values of k and A may be found in Janz's Molten Salts Handbook(31)
for many of the systems reported here. As previously stated,
the primary concern of this review is topics A-F. The results
presented herein are given for comparison and completeness and
were, in all cases, taken from the original publications
(exception: Appendix II).
It will be observed below that a number of publications
have not addressed themselves to some of the questions raised
above, If this review serves only to remedy this practice, it
is considered justified.
TABULATION
f .
Cell Pridge Range vop Results _
J System Ref i or (4fa) Electrodes ] {(Detector) (kHz) R va. f {v) T(°C) w2 lem ) or Alem?legq™ (mol™'))
‘“;‘ LiF 32 Pt crucible iR} = 0,182 Pt crucible and platinized Pt ¥Wheatstone 6 N.8. = Not N.S8. K
foil (3 x 4 mm) (telephone} Stated 905 20.2
950 23.4
. .- 995 27.2 (+5 to 10%)
2 LiF 33 Two Pt (80%) - Rh hemispheres (d = " &|Two Pt (B80%) - Rh rods (d - .01")| Specially develd N.S. N.S8 N.8 847 _ ) et
2"), These are also current electrodes |These are potential-measuring oped by E. Fair- 102; kK = 3.805 + 1,004x10 2T(°C) - 3.516x10 *T
electrodes. stein. (34)
f range=.2-6 kHZ
R range=.01-108
(oscilloscope) - -
$ 4 - (g-.0082 1cm 1)
3 LiF 35 Hot-pressured BN ecylinder (id - 3/16") |Inconel red and inconel plate ¥heatstone, na 2 "did not vary (N.8.{ gqno K = 8.43
36 surrounded by grthite {RS ~ 3-6 1. acrogs ends of BN cylinder. capacitors appreciably O=1.05 A% - 158
s/a) — 17-39 cm (oscilloscope) between 1 and
20 kHz (£ 1%)
4 LiF 24 | Pt crucible (vol. 319 em) {(f/a) = Two platinized Pt foils (10 x 10 | Thomson-type 50 f-dependency |~.05]| g75 8.663
29 0,28 cm ! mm) (oscilloscope) at lower f, 958 9.058
independent at 1037 9.306
50 kHz
& LiF 37 Graphite crucible (1d 3.5, 5" deep) [Two " Mo tubes fitting into Jones (null 10 f independent { N.S 870~ kK = 9.06 + 5.83x1072(T~-870°C)
containing 2 BN cylinders (id ~ 3/16") |upper portions of BN cylinders detector) 1-20 kHz 1010 A%9 . 1p0.8
encased in graphite and enlarged at tog o=1.2 .
to accomodate e¢lectrodes, (£/a) & 100cm (41%)
& NaF 38 | Pt crucible (400 ml), (£/a) = 0.0835cm?|Hemispherical Pt electrodes, Kelvin N t‘fi Ro £2 1o K A9
39 platinized originally. 4 extrapolated 1000 5.52 118
to f = @ 1040 5.74
o 1080 5.95% (tseveral %)
I e .
7 NaF 40 | Pt crucible (0.2 mm wall) ER} o 0.02 2(Crucible and a Pt cylinder (area | N.S. .15 | N.8. N.S.| 997 K o= 5.2
. o -~ 2 cm?), both platinized to 8
¢ : ’ #3 43 #3 #3
8 NaF :Z #3 #3 # # " # 1020 k = 6.15
- A®9 .
o O=1.05 A 113 (£ 19)
9 NaF 28 | #4 #4 #4 #4 | #4 #4 1003 4.960
29 1086 5.179
1138 5.335%
- s 5 #5 5 | #s #5 - -
S e & ‘ # iggg K = 5.29 + 5,.64x10 ¥ (T-1030°C)
eq
e=1. - .
1.2 A 156.6 (£1%)
11 | x¥ 3z| A1 #1 #1 # 4 #1 K
860 4.14
900 4.28
1 .7
000 4.7 (x5 to 10%)
12 | KF 13| 42 #2 #2 #2 | #2 #2 | se9 K = —3.493 + 1.480x1072T(°C)
1040 -6.608x10 °T? - -
(o=.009% lcm™ 1)
0T
£ Result
Cell Bridge Range Vpp esults L _
System Ref fR} or (2/a) Electrodes (Detector) (kHz) Rvs. f (v) T(°C) (2 lem ™) or Alem?Q leq™! (mol™!))
13 | XF 35 | #3 #3 #3 #3 #3 #3 900 xe= 3.80
36 e=1.05 A% = 124 (£1%)
14 | KF 28 | #4a #4 #4 #4 #4 #4 859 3.573
29 938 3.793
1012 4.021
15 KF 3% MgO, single crystal, dip cell; Pt Container and Pt electrode Jones .5-10] varied <0.3% | N.S 905 3.77 (2%
43 copntainer over £ range 2
-2 o
16 | CsF 33 1 #2 42 #2 #2 2 #2 725~ « = -4.511 + 1,642x10 2T(°C)
® ' # # 921 -7.632x10 ¢T? (o=.0092 cm™)
17 CsF 42 | #15 #15 #15 #15 #15 #15 737 2.51
43 784 2.73
852 3.03
18 | AgF 28 | # 4 4 4 4 4 590 4.0%
g 28 $4 # # # # # 670 6.0%
19 BeF, 44 Pt-Rh (20%) crucible_(id = 2", ht, Crucible and Pt-Rh (20%) bob "Wheatstone 2-10 f independent | N.S. ® -5
45 | (2/a) = .11 or .28cm ! R-C bridge" 2-10 kHz 700 ¢.71 x 10_5
(scope or VTVM) 800 15.3 x 1(_)5
950 236 x 10 (£10%)
2y | CcaF, 46 | carbon crucible Mo electrodes N.S. N.S. [N.S. N.s. | 1418 « = 3.56
21 { MnF 28 | #4 4 #4 #4 4 4 940 4.7,%
: 29 # # # # 990 5.0% -
22 | CuF 28 | #4 4 4 q 4 4 970 2.2¥
uF, 28 # # # # # # 1110 2.5%
23 | ZnF 28 | #4 1 4 4 4 #4 900 3.24%
e 29 | # # # # 960 3.7%
z4 | poF, 28 | #4 #4 #4 #4 #4 #4 820 5.1%
29 1000 5.8%
25 KBF, 28 #a #4 #4 #4 #4 #4 545 1.052
¢9 569 1.126
652 1.245
26 | Na,TaF, |28 | /4 4 #4 #4 #4 4 702 1.165
$TaF; |28 # # 733 1.396
814 1.595
27 | K,TiF, |28 | #4 #4 #4 44 Ad #4 343 1.346
29 888 1.435
976 1.604
28 | K,TaF 28 | 44 #4 #4 #4 #4 #4 747 0.7285
2 7 39 800 0.9193
887 1.0366
1T
cell Br idge Range vop Results
(g * - - - - -
System Red R} or (i/a) Electrodes {Detector) kHz) R vs. f (v) T(°C) k(2 tem 1) or Alem*Q'eq ! (mol7!))
A T T— L L mmmnd - = -
20 | LigAtF, |38 | 91 Wi #3 #3 | #3 #3 1800 ko= 3.45%
' i) 920 K = 3.87%
T WA AIF, T17 | Fuscd Mg tube (d .99, £ - 10.3 cm) “1draphite plates across ends of Wheats tone, K two | N.S, N.S.
(2/2) - 0752 em ! tube and £ in 'y 1020 x = 1.5
parallel cor
{telephone)}
- - —" - . L3
51| NaGAVE. | 391 F6 #6 #6 #e | #e #6 11000 2.80 980
1040 2.90 A®Y = 2,744 - wrvpy
L 1080 3.00 (» severalD
32 | Na,ALF, |40 | 47 #7 #7 #7 #7 #7 [lol3 K o= 2.8;*
o o | #3 #3 #3 #3 #3 3 at
3t | Na,AlF, 3 ‘ ” ! 1000 2.8O* 284 at 1010°
36 1060 2.95% 296 at 1040°
34 | Na;ALF, 28 | 4 #4 #4 #4 #4 #4 1025 2.8¢%
29 1120 3.0,*
i+ | Na,a1F, [ 47 | Pt nemisphere (od - 4 em), (t/a) - Container and Pt rod (d = 3 mm) Thomson plus 5 N.8 ¥.5- 11000 2. 84
386 em phase indicator 1040 z.92
1080 3,00
o | KoALE, N PN #3 #3 #1 | #3 #3000 5 32e
36 1060 2.42%
S ;‘A . ) LiF-ThF
i !nig * T " #3 #5 #5 #5 #s §E.§-3.5(m%) kK = 7,14 + 10.97x10 ¥ (T-880°C)
* A - 117.2, for @ = 1.2
78-22 (m%) x = 2,50 + 7.58x107 % (T-640°C)
A®9 - 29,9, for 0 = 1.2
50,2-49.8(m%) x = 2.13 + 4.19x107*(T-820°C)
aA%q . 31,0, for & = 1.2 (1%
14 LiF+UF, 37 F #s #5 #5 #5 #5 #5 LiF.UF -
I35 (wh) K = 7.55 + 5.86x1073(T-900°C)
eq
A =99,3, for © = 1.2
60-40(m%) « = 2.17 + 5.68x1073(T-700°C)
A®9 - 23,8, for @ - 1.2
40~60 (m%) kK = 2.89 + 3,29x107% (T-900°C)
A% = 33,5, for @ = 1.2 (.,
39 | NaF 48} Pt crucible {R}> 0.1 Curcible and Pt rod, both Carey-Foster 1 N.S. N.8. 500 837
CaF, platinized originally 1000 ‘;'373
(67 wi) °
1100 5.879 (z.5%)
gt
£ Vpp Results
Cell . Bridge Range - - - - -
o System Ref Rt or (i/a) Electrodes (Detector) (kHz) R vs, f v) T(°C) k(@ tem™) or A(em*2 leq”! (mol™}))
®
40 | NaF + 481 439 739 #39 #39 #39 #39 1900 4,441
SrF, 1000 4,961
(67 wh) 1100 5.642 (,5%)
K
41 | NaF + 48 | #39 #39 #39 #39 #39 #39 900 4.027
BaF, 1000 4.602
(67 wi) 1100 5.319 (£.5%)
®
42 NaF + 49 | Hot-pressed BeQ tube in a_cylindrical Pt crucible across bottom of Wheatstone, _R" 1 N.S8. N.S.N F-ZrF 565° 7300.‘ aBs®
ZrF, Pt crucible {(#/a) & 24 cm'! the tube and Pt rod at top and 2 in a ; r- ) ]
parallel - ! ’ - :
(oscilloscaope) 50-50(m%) 0.52 0.92 1,73 (£10%)
43 | NaF + 37| #5 #5 #5 #5 #5 #5 [NaF-ThF _
T 'EB-IZTn% k = 3,49 + 3.74x107*(T-900°C)
A%9 - 71,3, for ©@ = 1.2
67-33(m%) k = 1.76 + 3.88x107* (T-800°C)
A®% - 28.1, for © = 1.2
50-50(m%) ® = 1,48 + 5,23x10 2 (T-800°C)
A9 - 28.6, for 8 = 1.2 (£1%)
; ; NaF-UF ' _
# 3:‘? ’ ks #s #s #s #5 #3 BE-TETm) x = 2.81 + 3.56x10 2 (T-850°C)
A®% - 57,7, for @ = 1,2
65-35(m%) k = 1.37 + 4.65x1072 (T-700°C)
A®% - 25,6, for & = 1.2
25+ 75 (m%) k = 2,18 + 3.56x10 ? (T-900°C)
Aeq = 36,9, for 8@ = 1.2 (£1%)
K
45 | NaF + 50 | Described in Ref. 51, not readily Pt electrodes Wheatstone, 5 N.8. N.S.| NaF-NaBF 450° 650° 800°
NaBF, available with balancing -4 A - - T.502
o 40-60(wth) 0.965 6.350 14.10s
(oscilloscope) 10-90{(w%) 2.408 8.801 14.978
K Aeq
46 | NaF + 3B | #6 #6 #6 #6 #6 #6 | NaF-NajAlF 1000° 1040° 108¢° 1006°
Na,AlF, |19 7692 T 3. To0 T4
50-50(m%) 3.19 3.30 3.41 99
35.7-64.3 (m%) 3.12 3.23 3.33 100
o
47 | KF + 50 | #45 #45 #45 #45 #45 #45 | KF-KBF 450° 650° goa°
KBF, TO-30Te%) = —— T5.o01
40-60 (W) - 2.255 11.495
10+90 (w¥h) 0.281 3.601 12.703
Wheatstone, BT (data taken Irom graphs)
48 | MgF; + 52| Pt cell N.S. and & in N.8.| N.S8 N.S| MgF, -Na,ALF. %1070
Na,AlF, parallel = W =3
(oscilloscope) 10-90 (wdl) 2.2
1-99 (w%) 2.8
¢T