M. Ali Basu et al. / Journal of Alloys and Compounds 352 (2003) 140–142
141
the available thermodynamic information of Te vapor [5]
revealed that the compound incongruently volatilize pre-
dominantly as:
d the orifice-to-collimator distance. The vapor pressure
expression for Te (g) in the Knudsen cell obtained by
2
equating the rate of the observed effusion with that
obtainable from the kinetic theory of gas is given by:
RuTe (s) 5 Ru(s) 1 Te (g)
(1)
2
2
2
2
d
2
1
/ 2
p
s
Te2
d
5 (1/A)
s
wTe /t
d
fsr 1 d
/r
g
f
2pRT/MTe2
g
(3)
Under the volatilization equilibrium, the vapor pressure of
Te (g) remains constant at any temperature. This result
was considered while carrying out the vapor pressure
analysis from Knudsen effusion technique.
2
where A is the orifice area, R is the gas constant, and T the
temperature of the Knudsen cell monitored during vapor
collection. The vapor pressures of Te (g) over Ru(s)1
2
For the effusion run, about 1 g of the sample was taken
in a quartz cup inside a Knudsen cell having a knife-edged
orifice with the diameter of 0.0010 m. The cell typically
made of inconel or molybdenum was thoroughly degassed
at high temperature beforehand. The Knudsen cell loaded
with the sample was immediately mounted inside an all
quartz vacuum system and heated by a tungsten furnace.
Temperature measurement was done using Pt/Pt–13% Rh
thermocouple. Temperature stability within the cell could
be maintained within 62 K. The forward collection
arrangement of effusate was identical to that given in Ref.
RuTe (s) at different temperatures were calculated from
2
the experimentally determined parameters involved in the
right hand side of Eq. (3) and are presented in Table 1.
The tabulated pressures above the temperature of 1026 K
are those after correction for the deviation from Knudsen
flow [7] due to high value of pTe2 at high temperatures.
The correction involves the use of the collision diameter sc
of Te (g) which was taken to be 670 pm. This value of s
2
c
for the molecule Te (g) could be arrived from its
2
Leonard–Jones potential parameter s by linear interpola-
tion of s versus s for the known cases. The maximum
c
[6]. In the above experiment the vertical separation be-
correction results in about 38% reduction in the pressure
value observed at the highest temperature, i.e. 1148 K. The
logarithm of the corrected pressures are plotted as a
function of the reciprocal of the temperatures as shown in
Fig. 1. The linear least square fit of ln pTe2 versus 1/T
could be represented as:
tween cell orifice and collimator defining the collection
geometry was typically 0.07 m while the collimator
diameter was 0.022 m.
Several effusion runs were carried out to monitor the
rates of collection of Te on the targets at different
temperatures within the range of 831–1148 K. The collec-
tion period was controlled by interposing a shutter between
the collimator and the vapor source. Frequent monitoring
of the cell temperature was done and found to be constant
during vapor collection on the target made of tantalum.
After the experiment phase analysis of the residue in the
cup was done by XRD to confirm the existence of the
ln( p/Pa)(60.33) 5 2 33231.2/T
1
33.67 (831 # T/K # 1148)
(4)
Table 1
Vaporization data and the third law enthalpy change for the reaction
RuTe (s)5Ru(s)1Te (g)
2
2
biphasic mixture of Ru(s) and RuTe (s). The tellurium
2
a
content on the targets was analyzed by bringing the Te-
deposit into solution of 5% nitric acid and making up the
volume to 10 ml in each case and then, by using ICPAES
technique with proper standard. Some of the ICPAES
results were cross checked by XRF analysis of Te prior to
the dissolution of the deposit.
Temp
Time
(s)
Mass loss (kg)
w(Te)310
Pressure
(Pa)
Third law
DH8298.15 (kJ mol
9
21
(
K)
)
831
5760
3660
3240
1860
1200
960
1080
600
2400
840
840
600
1200
600
450
0.6
0.5
2.0
6.2
7.5
0.002
0.003
0.025
0.080
0.145
0.574
0.518
1.894
2.746
3.126
3.126
6.424
6.360
9.116
20.371
29.371
55.146
66.686
122.732
278.3
282.3
279.9
276.1
278.8
273.5
274.3
285.5
280.6
280.5
280.8
280.9
281.5
278.6
278.0
275.4
276.4
274.9
276.7
8
8
9
9
9
9
52
93
09
34
53
53
23.6
24.0
47.2
268
108
107
164
319
243
440
630
827
1060
1390
1
1
1
014
026
030
3
. Results and discussion
The effusion results were analyzed on the basis of
vaporization equilibrium expressed in Eq. (1) that involves
1031
1
1
1
055
057
058
1085
087
1115
116
1148
Te (g) as the predominant vapor species. The rate of
2
effusion of Te (g) from the orifice was obtained from the
2
observed tellurium content on a target collected over time t
and the geometry of the forward collection as given by:
1
450
300
300
210
1
2
2
2
dE/dt 5
s
wTe /td s1/MTe2
d
fsr 1 d
d
/r
g
(2)
2
1
D H8
(Third Law)5278.664.0 kJ mol .
r
298
where, wTe is the amount of tellurium, M
is the
21
Te2
D H8
298
(Second Law)5283.267.0 kJ mol .
2
2
2
r
a
molecular weight of the Te species and (r 1 d )/r is the
2
Pressures corresponding to temperatures greater than 1026 K have
been corrected for deviation from Knudsen flow.
geometric factor, with r as the radius of the collimator and