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J Electrounal Chem.. 199 (1986) 207-210
Elsewer Sequoia S.A.. Lausanne - Printed m The Netherlands 207
Short communication
ELECTRODEPOSITION OF TITANIUM AND ITS DIOXIDE FROM ILMENITE
L.H. MADKOUR *
Cherntsty Department, Faculiy of Sctence, Tantu lJmaerst&, Tunta (Egvpt)
A.S. FOUDA
Chemtstn Department, Faculty of Sctence, Mansouro Unwerstty, Munsour~~ (Egvpt)
(Recewed 15th April 1985: in revised form 13th September 1985)
INTRODUCTION
The aim of the present work was to develop a simple and rapid electrolytic extraction process of titanium [l-3] and its dioxide from the ilmenite ore of the Eastern Desert. The ore mother liquor used for the electrolysis process is either produced by direct leaching with 98% H,SO, (S/L = 1 : 15), 35% HCl (S/L = 1: 20) and alkaline digestion with caustic soda in a ball-mill autoclave at 175°C under a pressure of 9.5 kg cmP2, or it is prepared through the fusion method using NaOH or Na,S,O, separately as fluxes at 600-700°C.
EXPERIMENTAL
Ti and TiO, were prepared by electrodeposition on platinum sheets as described previously [3-61. All the chemicals used were of BDH Analar grade and were used without further purification; 0.1 M ore leach chloride and sulphate were prepared from doubly distilled water and their concentrations were determined as given by Vogel [7].
RESULTS AND DISCUSSION
Baths suitable for the electrodeposition of Ti and TiO, are indicated in Table 1. The production of titanate and its dissolution are assumed. The effects of current density, complexing agents. ammonium salt, temperature and current efficiency were studied. Also, we confirmed the presence of positively and negatively charged complex species by carrying out experiments using the ion-exchange resin technique
l To whom correspondence should be addressed.
0022-0728/86/$03.50 ‘a 1986 Elsewer Sequoia S.A
TA
BL
E
1
Suita
ble
bath
s fo
r th
e el
ectr
olyt
tc
extr
actio
n of
ttt
aniu
m
and
its d
ioxr
de
from
rl
men
ite
ore
Bat
h C
ompo
sttio
n of
ele
ctro
lyte
so
lutio
n
(in
500
cm3
ore
liquo
r)
PH
Cur
rent
Pr
oduc
t C
ompl
ex
spec
tes
Cur
rent
R
ecov
ery
dens
ity/
efft
cten
cy
/W
mA
cm
e2
/%
Sulp
hate
Chl
orid
e
Am
mon
ia
Bor
ate
Ace
tate
Tar
tara
te
Bro
mid
e
Fluo
ride
Oxa
late
Ure
a
Sodi
um
hydr
oxid
e
Ore
le
ach
sulp
hate
(0
.1
M)
and
20 c
m3
1 M
H
,SO
.,
Ore
le
ach
chlo
ride
(0
.1
M)
and
10 c
m3
perc
hlor
ic
acid
Ore
le
ach
chlo
nde
(0.1
M
),
60 g
NH
,CI
and
NH
,OH
(1
: 1)
Ore
le
ach
chlo
nde
(0.1
M
).
60 g
NH
,CI,
3 g
bora
x an
d N
H,O
H
(1:
1)
Ore
le
ach
chlo
ride
(0
.1
M),
30
g N
H,C
l,
50 c
m3
(1 M
) ac
etic
ac
id
and
NH
,OH
(1
: 1)
Ore
le
ach
chlo
ride
(0
.1
M),
40
g N
H,C
I,
50 c
m3
(1 M
) ta
rtan
c ac
id
and
NH
,OH
(1
: 1)
Ore
le
ach
chlo
ride
an
d 20
cm
3 2
M
HB
r
Ore
le
ach
chlo
ride
(0
.2
M).
50
g
NH
,CI,
N
aF
and
NH
,OH
(1
: 1)
Ore
le
ach
chlo
ride
(0
.1
M).
60
g N
H,C
l,
50 c
m3
(1 M
) ox
alic
ac
id
and
NH
,OH
(1
: 1)
Ore
le
ach
chlo
ride
(0
.1
M)
and
5 g
urea
Ore
le
ach
chlo
nde
(0.1
M
),
60 g
NaO
H
and
15 c
m3
glyc
erol
[Ti(
OH
),HSO
,]‘+
[Tt(
OH
)Cl,
+TI]
‘+
FXN
H3)
,13+
[Ti(
B40
7)12
’
4.0
250
T1
99.3
96
.2
3.8
240
TI
99.4
95
.6
9.0
200
Ti
98.7
97
.1
9.0
400
7.5
230
Tl
TI
99.6
94
.3
99.8
96
.2
5.0
250
TI
[TK
&$H
,)I’
+
99.6
93
.4
4.0
300
Ti
[Tt(
OH
)Br2
+
Ti]
j+
99.4
94
.7
8.0
200
99.2
95
.2
8.0
600
8.0
300
TiO
2
[TC
,)12
-
Ti
[Ti(C
,Q,
)12’
T
i lT
WW
H,)
,),1
3+
99.5
96
.3
98.6
94
.5
10.0
30
0 T
I [T
i(O
H),
]”
99.4
93
.8
209
[8,9]. The structures of titanium complexes of the type [Ti(NH,),13+ were proved [lo]. Also, the tartarate 1111, oxalate 1121, bromide, chloride 1131, perchlorate 1141, sulphate [14], urea [14] and fluoride [15] [Ti(F,)12- complexes of titanium were identified and proved conductometrically. The formation of Ti and TiO, is dis- cussed. The results of chemical and spectrophotometric analyses indicate that the purity of titanium is 99.1%. Also the electron micrograms confirmed by the X-ray standard tables (ASTM) for TiO, coincide well with those given by chemical analysis.
The reaction of ilmenite ore with NaOH and its dissolution in H,SO, and WC1 can be represented as follows:
FeTiO, + 2 NaOH + Na zTiO, + Fe0 +H,O
(1) NaZTiO, C 3 H,S04 -+Ti(SO,),+Na,SO,+3 H,O
Ti(SO,), + H,O + TiOSO, + H *SO,
(2) Na,TiO, + 4 HCI -+Ti(OCl)z+2 NaCl +2 Hz0
Ti The following equation represents the mechanism of formation of the element
from the different baths used 1161:
Ti(L)“++ ne”-+Ti+L
where L is the ligand of the complex species and n is the number of positive charges on the species. Adsorption of hydrogen ions and complex species on the surface of Ti protects it from oxidation.
During the deposition of TiO,, the complex species [TiF612- migrated towards the anode, where it loses its negative charge and dissociates yielding Ti4’ ions. These ions are oxidized by the OH. radicals at the anode to form TiOz [17].
[TiF612- +Ti4++6 F-
Ti4++ 2 H,O~TiO~+4 H” i
Effect of current density At low current density (200 mA cme2}, only a thin layer of Ti was deposited and
an oxide with low oxygen content was obtained in the case of TiO, deposition. At higher current densities (> 400 mA cm-‘), a non-adherent and randomly oriented deposit [18] of Ti and an oxide with higher oxygen content were obtained. Suitable current densities for cathodic and anodic deposition are shown in Table 1.
Effect of complexmg agent/metal ion ratto
Smooth deposition of bright grey-silver Ti was obtained at low concentration ( = 0.1 M) of complexing agent. Also, the adsorption of complexing agents at the cathode prevents the oxidation of Ti.
Effect of ammonium salt Ammonium salt acts as a buffering medium for the bath; it assists the stability of
the Ti complexes. prevents the precipitation of Ti hydroxide as the pH is raised. and increases the conductance of the solution.
Effect of temperature Increasing the temperature from 25 to 50°C favours the deposition of Ti and TiO,
owing to the acceleration of both the ionic migration of the complex species and the oxidation of Ti” at the anode.
Current efficiency In the ammonia and urea baths the current yield is nearly 99%. The platinum
plate and the dilute solution of Ti are responsible [19] for the current yield being
slightly lower than 100%.
ACKNOWLEDGEMENT
The author would like to thank the Egyptian Geological Survey and Mining Authority. A.R.E.. for kindly supplying a sample of the title ore.
REFERENCES
1 T. Hammada. Japanese Patent. 2357 (55). 11 Apnl (1957) 51.
2 N.T. Kudryavtsev and R.G. Golovchanskaya, USSR Patent 127. 10 March (1960) 121.
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810
15 Ya.A. Buslaev, V.A. Boekbareva and N.S. Nikolaev, Izv. Akad. Nauk SSR Otd. Khim. Nauk. 3 (1962) 388.
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19 AS. Fouda and M.M. Eisemongy, J. Electroanal. Chem.. 124 (1981) 301.