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T = 160 ºC
Yield = 0.99
0
1
2
3
4
5
6
7 0
0
-0.5
-0.5
-1
-1
PZTVPPT
-1.5
-1.5
-2
-2
-2.5
-2.5
0
1
2
3
m (C4H13NO)
4
5
6
7
Figure 10.39 Calculated yield of PbTiO 3 in the Pb Ti H 2 O complexing agent system for
various Pb/Ti ratios [170] .
greatly in the hydrothermal synthesis of phase-pure ceramics. Figure 10.39 shows
the calculated yield of PbTiO 3 in the Pb
H 2 O complexing agent system for
various Pb/Ti ratios. A majority of the PZT systems incorporate intolerable
amounts of alkaline metals, which are introduced in the form of mineralizers. In
recent years, organic mineralizers are being used by a large number of workers.
For example, Riman et al. [170] have found that tetramethylammonium hydroxide
[N(CH 3 ) 4 OH] is a favorable substitute for alkaline metal hydroxide mineralizers in
producing phase-pure PZT. Phase-pure MeTiO 3 (Me
Ti
Ca, Sr, and Ba) can be
obtained at input molalities of Ba, Sr, and Ca greater than 7
5
10 2 5 ,10 2 6 , and
3
10 2 5 , respectively. Otherwise, the relative location of the 99.995% yield
regions for the three titanates will be similar to the pattern noted for stability dia-
grams [163] . In concentrated solutions, the consumption of OH 2 ions is caused by
the following predominant reactions:
5
3
Me 2 1 1
2OH 2 5
ð
:
Þ
TiO 2 1
MeTiO 3 1
H 2 O
10
1
Thus, 2 M of OH 2 is consumed for the synthesis of 1 M of MeTiO 3 , and only a
relatively small amount of OH 2 is necessary to ensure correct pH for respective
alkaline earth. Unlike the synthesis with nitrates,
the use of metal hydroxide
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