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Transcript
The development of the chemical bath deposition (CBD)
technique has gained lots of attention during the last years
as a method for preparing thin films of chalcogenide
compounds. The majority of the studies related to CBD
are normally restricted to the characterisation of deposited
films. Hence, the basic chemical aspects related to
solution chemistry and reaction kinetics of that process are
most of the times neglected. This leads to a limitation to
the development of the CBD method on comprehensive
grounds. On the basis of our experience in the field of the
chemical bath deposition of In(OH)xSy thin films [1, 2, 3]
we present here our studies concerning the composition of
the bath before and after the In(OH)xSy deposition.
The solutions used in the chemical bath deposition of
In(OH)xSy contain InCl3, acetic acid and thioacetamide.
As it was stated in a previous work [4], the chemical
species present in the solution and the rate of
thioacetamide hydrolysis, depend on the solution pH.
Therefore, the pH of solutions containing thioacetamide,
acetic acid and InCl3 was measured at room temperature.
In all cases, the addition of thioacetamide did not change
the solution pH. In the case where no InCl3 was added, the
theoretical values almost matched the experimental ones.
In contrast, when InCl3 was present, the solution pH was
always lower than the calculated values. This deviation of
the experimental pH can be in part due to the ionic
strength of the solution and in part due to the formation of
either indium-acetate complexes or other complexes
containing hydroxide ions or even to the formation of
hydroxide colloids [3, 5, 6].
From the pH values the molar percentage of the species
present in the solution can be calculated using the
equilibrium constants found in the literature [7]. In Figure
1 it can be seen that the predominant species in our system
are the chloro complexes, the acetate complexes, and the
chloro-hydroxo complexes and that this predominance
depends on the acetic acid concentration and therefore on
the solution pH.
The hydrolysis reaction of the sulphide precursor is
another point that should be considered when a CBD
process is studied. In the case of the thioacetamide, the
most recent mechanism for the hydrolysis in an acidic
medium has been proposed by O. M. Peeters and C. J. de
Ranter [8]. From the kinetic equations deduced by these
authors the molar percentage of the reaction products can
be calculated as a function of the reaction time. An
example of such calculations is represented in Figure 2. In
order to compare the theoretical values with experimental
results the organic products formed after the In(OH)xSy
precipitation were investigated using gas-mass
chromatography. The compounds identified were mainly
acetonitrile and thioacetic acid, but surprisingly no
acetamide was detected. The In(OH)xSy precipitation
therefore seems to take place through a mechanism which
is not the hydrolysis of the thioacetamide and which leads
to different products depending on the solution pH. As a
This work has been supported by JOR3-CT97-0124 and
TIC 96-0479 projects.
60
3+
Species percentage
R. Bayón, J. Herrero*
Hahn-Meitner Institut, Glienicker Straße 100, 14109
Belin, Germany
(*) Departamento de Energías Renovables (CIEMAT),
Av. Complutense 22, 28040 Madrid, Spain.
result of these investigations a reaction mechanism for the
formation of In(OH)xSy can be proposed.
[In ]
2+
[InCl]
+
[InCl 2 ]
[InCl 3 ]
50
40
+
[InCl(O H)]
2+
[In 2 Cl 2 (O H) 2 ]
[In(AcO ) n ]
3-n
[InCl n (AcO ) m ]
3-n-m
30
20
10
0
0.0
0.1
0.2
0.3
[H AcO ] (M )
Figure 1. Calculated molar percentage of the species
composing the In(OH)xSy deposition bath as a function of
[HAcO].
2.25
o
Tem perature 70 C
pH 2.45
2.00
Species percentage
Solution chemistry and reaction mechanism
taking place during the chemical bath
deposition of In(OH)xSy
1.75
H 2S
1.50
Acetam ide
1.25
1.00
0.75
NH4
+
0.50
Thioacetic acid
0.25
Acetic acid
0.00
0
20
40
60
80
100 120
Tim e (m in)
Figure 2. Calculated molar percentage of the products
formed during the thioacetamide hydrolysis.
[1] R. Bayón, C. Guillén, M. A. Martínez, M. T.
Gutiérrez and J. Herrero, J. Electrochem. Soc. 145
(8) (1998) 2775.
[2] R. Bayón, C. Maffiotte and J. Herrero, Thin Solid
Films 353 (1999) 100.
[3] R. Bayón and J. Herrero, Appl. Surf. Sci. 158 (2000)
49.
[4] R. Bayón and J. Herrero, Thin Solid Films 387
(2001) 111.
[5] C. Kaufmann, P. J. Dobson, S. Neve, W. Bohne, J.
Klaer, R. Klenk, C. Pettenkofer, J. Röhrich, R. Sheer
and U. Störkel, 28th IEEE PVSC, Anchorage 2000.
[6] C. Kaufmann, R. Bayón, W. Bohne, J. Rohrich, R.
Klenk and P. J. Dobson, J. Electrochem. Soc. 149
(1) (2002) C1.
[7] J. Kragten , Atlas of Metal-Ligand Equilibria in
Aqueous Solution, Ellis Horwood Limited Edition
1978.
[8] O. M. Peeters and C. J. de Ranter, J. Chem. Soc,
Perkin II (1974) 1832.