Note: Descriptions are shown in the official language in which they were submitted.
37
The invention relates to an electrode for electrochemical process
and, more particularly, to such an el0ctrode having a base formed of passi-
vatable material and a covering layer of activating substance at least partly
covering the base, and to a method of production of such an electrode.
Numerous electrochemical processes have been introduced in the
field of engineering, for example, for producing chlorine and alkalis from
salt solutions in quicksilver - or diaphragm cells, chlorates, hypochlorides
and the like, for oxidation of organic substances, for desalinization of, for
example, sea water, and for protection against cathodic corrosion. It has
been known heretofore, to employ cathodes and anodes of graphite or impreg-
nated graphite for such electrochemical processes, wherein the graphite ano-
des are depleted or reduced by electrochemical reaction so that, in order to
maintain a constant spacing between the electrodes, the anodes must be adjus-
ted periodically and finally replaced. In addition, it has become known,
heretofore, to produce anodes of passivatable metals, such as titanium, zir-
conium, niobium, tantalum, tungsten, aluminum, iron, nickel, lead and bismuth,
for example, which are virtually stable under electrolysis conditions i.e.
the dimensions thereof virtually remain unchanged. The preferably oxidic
passivating layer that forms on the surface of such a metal anode lends to
the anode an outstanding durability or stability against corrosive attack,
however, due to its relatively great electrical resistance, it simultaneously
effects a marked increase in voltage drop. To avoid this disadvantage, it
has become known to provide metal anodes with covering layers containing
activating substances, such as platinum metal, compounds of platinum metal
alone or together with oxides of non-noble metals, such as manganese, lead,
titanium or tantalum. Moreover, the provision of a covering layer with
numerous other compounds, such as carbides, borides, sulfides, phosphides
and mixed oxides, has also been proposed heretofore.
Essential criteria for the utility of a covering layer are dura-
bility or stability in the respective electrolyte, resistance to erosion or
-1- ~'
L3~
corrosion, and especially the adhesion of the layer to the electrode base.
Numerous methods of improving the adhesive strength have become kno~m which
are determined essentially by the type of coating or layer-forming process,
the composition of the covsring layer substance, and the characteristics of
the surface to be coated. It has also been known to dispose an additional
intermedia~e layer between the base and the covering layer as "adhesion
helper" or "intermediary". Partial loosening or detachment of the covering
layer cannot be eliminated, however, with the heretofore known types of base-
covering layer pairings.
The connection between the electrode base and the current supply
rods formed, for example of titanium, which are in turn electrically connec-
ted through busbars or conductor bars to a rectifier is essential for the
utility of the electrodes. The quality of the mechanical and electrical
connection is not ultimately determined by the weldability or solderability
of the materials used for producing electrode bases and current or power
supply rods.
In performing electrochemical reactions, it is generally advanta-
geous to remove the reaction products rapidly and as completely as possible
from the electrode surfaces and to ensure simultaneously the constant and
intensive supply of fresh electrolyte, in order to avoid impairment of the
efficiency of the reactions.
In the aqueous electrolysis of alkali halogenides according to the
quicksilver method, the voltage drop of the cell, for example, is increased
to an undesired extent by gas bubbles and gas films adhering to the anode
surface. To avoid this effect, numerous forms of anodes having bases of
graphite or of solid metals, such as titanium, for example, and which pro-
mote the loosening and transport of the gas bubbles, have been proposed here-
tofore. However, they have proven to be of limited suitability because of
the required, relatively high processing expense for electrodes of a sin-
tered metal or of a metallic compound.
3'7
It is accordingly an object of the invention ~o provide an elec-
trode for electrochemical processes wherein the adhesion of the covering
layer to the electrode base is so improved that reductions in the electrochem-
ical activity of the electrode due to partial loosening or detachment of the
covering layer are completely avoided.
It is another object of the invention to provide such an electrode
with a mechanical and electrical connection between ~he electrode base and
power supply rods of ti~anium, which are, in turn, connected by conductor
bars to a rectifier, that is much improved in durability over that of the
heretofore known devices of this general type.
It is a further object of the invention to provide an electrode of
the foregoing type which is of relatively simple construction and in which
there is a marked reduction of gas bubble polarization as compared to here-
tofore known electrodes of this type.
It is yet another object of the invention to provide a method oE
producing such an electrode that employs relatively simple and inexpensive
means.
With the foregoing and other objects in view, there is provided in
accordance with the invention, an electrode for electrochemical processes
comprising a base formed of passivatable material, and a covering layer of
activating substance at least partly covering the base, the material of the
base consisting of titanium oxide TiOX, wherein x = 0.25 to 1.50.
In accordance with a preferred embodiment of the invention,
x = 0.42 to 0.60.
In accordance with another feature of the invention, 20 to 50% by
volume of the base is formed of pores having a mean diameter of 0.5 to 5 mm.
In accordance with a further feature of the invention, the elec-
trode base has a surface facing away from the covering layer, that surface
being provided with a layer of metallic sintered titanium to improve the
; 30 weldability and solderability thereof.
- 3 -
L3~7
In accordance with an additional feature of the invention and to
minimize gas bubble polarization, the electrode of the invention is provided
with a rectangular bottom surface wherein a series of slots of uniformly in-
creasing depth are formed extending from side to opposing side of the elec-
trode.
In accordance with an added feature of the invention, the electrode
has a top surface that is inclined with respect to the bottom surface thereof.
In accordance with yet another feature of the invention, the slots
are defined by surfaces extending vertically along respective edges formed at
the bottom surface of the electrode, the edges formed between the vertical
surfaces of the slots and the bottom surface being rounded.
In accordance with still another feature of the invention, a shield
is mounted at the side of the electrode at which the slots are deepest and
extends a given vertical distance so as to be just below a desirable electro-
lyte surface level.
In accordance with a concomitant feature of the invention, the el-
ectrode base is formed with a bottom, a top and a lateral surface, at least
one of the surfaces being provided with rib-like reinforcing members.
In accordance with one mode of the method of producing the elec-
trode for electrochemical processes according to the inventionl the follow-
ing steps are performed: mixing titanium powder and titanium dioxide powder
in a ratio of 7 : 1 to 1 : 3, adding a binding agent thereto, compressing
the resulting mixture and sintering it at temperature of 1200 to 1400C in
an argon atmosphere, and coating the thus compressed and sintered body with
a covering layer containing an activating substance.
In accordance with another mode of the method of the invention,
after forming the foregoing compressed and sintered body and before perform-
ing the coating step, the method includes the steps of: comminuting the
compressed and sintered body into TiOX powder, compressing the TiOX powder
at pressures of 300 to 2500 kp/cm2 into a plurality of molded members, sin-
- 4 -
L37
tering the molded members at temperature of 1200 to 1400C, and then coating
the sintered molded members with the layer of activating substance.
In accordance with a further mode of the method, a layer of TiOX
powder is covered with a layer of titanium powder and compressed with pres-
sure of from 300 to 3000 kp/cm2 (kilopond per square centimeter), molded and
sintered by heating in an inert gas atmosphere to a temperature of from 1100
to 1400C, and after cooling the sintered body, applying to the free TiOX
surface thereof a covering layer containing an activating substance.
More specifically, to produce the base of the electrode of the in-
vention, titanium metal and titanium oxide, both in powder form, are mixedin a ratio of 7 : 1 to 1 : 3, if desired, after adding thereto an aqueous
solution of polyvinyl alcohol for example; the mixture is then compressed
into plates, rods or members having other shapes suitable as electrodes; and
the thus-formed compressed or molded members are then sintered in an inert
atmosphere in the temperature range of 900 to 1500C.
Mixtures with relatively higher oxygen content are expediently sin-
tered at higher temperatures than oxygen-poorer mixtures. To improve the
uniformity or homogeneity of the sintered TiOX members, a two-stage produc-
tion method may be of advantage wherein the sintered molded members formed
in the just-described manner are comminuted and ground, and the powder there-
by obtained, if desired after the addition thereto of a compression supple-
ment such as paraffin, wax, polyethylene, polytetrafluorethylene and the like,
is compressed into plates or rods. Through expediently shaped press dies,
reenforcement ribs and/or recesses interspersing the electrode base and
serving as gas discharge or escape channels, are impressed into the plates
or rods. The molded members are then heated in a protective gas, such as
argon for example, to a temperature of about 1200 to 1400C.
Through the single or double heat treatment of the compressed Ti-
TiO2 powder mixture, substantially uniform TiO-phases corresponding to the
respective stoichiometric composition are formed, the crystal lattices of
~ ~4U13'7
which are considerably disrupted. Thus, for example, in the range x = 0.6 to
1.25, a compound of the NaCl-type withalattice replete with a multiplicity of
gaps exists, in the range x < 0.42, the ~ -titanium lattice is expanded by
occluded oxygen, and in the ranges x = 0.42 to 0.60 or x = 1.25 to 1.50, the
electrode base is formed of mixtures of the disrupted ~ -Ti and TiO-phases or
the TiO and Ti203-phases.
In accordance with a further embodiment of the invention, the poro-
sity of the base is about 20 to 50% by volume. To produce a porous base,
sintered pre-molded members having the composition TiOX, wherein x = 0.25,
to 1.50, are comminuted, fractions thereof having grain sizes between 1 and
12 mm, that are obtained by means of sieves, are compressed, and are then
heated, for example, in an argon atmosphere to about 1200 to 1400C. The
mean pore diameter is expediently substantially 0.5 to 5 mm. The large outer
surface of such a base affords the impingement thereon of very large currents
without damage to the covering layer. Of further advantage are the numerous,
statistically uniformly distributed pores interspersed through the base and
serving as gas discharge or escape channels, and the relatively low weight of
a porous base.
To supply current to the electrode of the invention, one or more
titanium rods are secured to the base and are, in turn, connected through
current conductors or rails, for example, to a rectifier. To produce the
connection between the current supply rods and the base, conventional methods
such as hard soldering and especially welding are of little suitability foT
electrode bases of TiOX wherein x = 0.25 to 1.50, because, even with care-
ful handling, crac~s or tears in the solder layer or in the welding seam
and also in the base are unavoidable, and the drop in voltage due to these
defects increases to undesired high values during operation of the electrode.
The weldability and solderability of the electrode base is improved in ac-
cordance with the invention by applying to a surface of the molded member a
layer of titanium powder mixed with a binding agent, such as etherized cell-
- \
1 3L3~7
ulose, by means of a spatula or also by compression and then firmly bound to
the TiOX base by sintering at a temperature of about 1200C in an argon
atmosphere. In accordance with other modes of the method of the invention,
the titanium layer is applied to the base by flame-spraying or plasma-spray-
ing.
The electrodes can also be produced by compressing porous or spongy
titanium into plate-shaped members, covering the lattice with a powder mix-
ture of titanium- and rutile powder, or with a TiOx-powder, and then sinter-
ing the powder-covered members at a temperature of about 1100 to 1400C. In
accordance with a preferred mode of the method of producing the electrode of
the invention, a layer of TiOx-powder is covered with a layer of titanium
powder in a die, then both layers at pressures of from 300 to 3000 kp/cm2
are compressed, molded and sintered.
The sintered base is then provided with a covering layer which con-
tains at least one metal of the group platinum, palladium, iridium, ruthe-
nium, osmium, rhodium, gold and silver or of a compound of these metals, such
as an oxide, nitride or sulfide thereof. Suitable methods of applying the
covering layer are, for example, precipitation from solutions, the spreading
on of a suspension, galvanic deposition, plasma-spraying, flame-spraying or
pyrolytic deposition from the gas phase. The covering layer which is baked
or burned on by heating to about 300 to 600C, should cover at least 5% of
the surface of the electrlc base and should have a thickness of about 0.5
to 10 ~m.
The covering layer of electrodes according to the invention, is
firmly anchored in the disrupted crystal lattice of the base material so
that, even after repeated tempering with subsequent quenching of the elec-
trode, no loosening of the layer nor reduction of the electrochemical activ-
ity is detectable. Abrasion of the covering layers under erosive or corro-
sive conditions, as are present, for example, in electrolyte cells with
rapidly flowing electrolyte, is extraordinarily low. The fissured porous
3~7
surface of the base is, in addition, considerably larger than the surface of
a solid metal electrode of corresponding dimensions so that, per unit of area,
a larger quan~ity of activating substance can be applied and the electrode
can be subjected to a greater current density without damaging the activating
substance.
A further advantage of the electrode of the invention is that gas
discharge or escape channels, reenforcing ribs and the like can be impressed
into the base during the production thereof, thereby dispensing with any
additional subsequent machining or other operation.
Electrodes produced in accordance with the ;nvention are advanta-
geously formed with three layers, a first layer facing toward the electro-
lyte, containing noble metals or compounds of noble metals, a second layer
of a titanium oxide TiOX wherein x = 0.25 to 1.50, and a third layer of
titanium. The layers are connected one to another so as to be mechanically
undetachable or unloosenable, the middle layer essentially assuring the firm
anchoring of the first layer to the electrode base and the third layer assur-
ing the weldability of the base to the current supply rods of titanium. The
electrode of the invention thus combines the advantage of a base of metallic
titanium with respect to weldability with the advantages of a base of TiOX
with respect to the firm bonding of the covering layer. The thickness of
the Ti0X and Ti-layers forming the base, and the ratio of the thickness of
both layers is determined exclusively by their functional efficiency, by
which is to be understood mechanical stability and the weldability of the
base as well as the bonding of the covering layer. Advantageously, the
thickness ratio is substantially from 10 : 1 to 1 : 10. Porosity and pore
size distribution are variable and can be matched to the respective operat-
ing conditions by varying the grain size of the powder being used as well as
the compression and sintering conditions, for example for the formation of
suitable gas discharge or escape channels.
The preferred embodiment of the electrode of the invention effects
- \
'7
an escape of the gas bubbles, accumulating in the slots, at the side of the
electrode at which the slots have the greatest depth whereby, due to the gas
flow as well as the hydrostatic pressure diference in the cell, a fresh cir-
culation flow transporting brine deple~ed of gas bubbles from the upper sur-
face of the electrode to the underside thereof is produced, which simultan-
eously entrains gas bubbles that have formed at the underside of the elec-
trode. The shortened duration of the gas bubbles leads to a reduction of the
detrimental covering of gas on the electrode surface and thereby to a reduc-
tion of the voltage drop due to gas bubble polarization. The slope or inclin-
ation of the slots which, depending upon the respective current density, re-
sults in a maximal circulation effect, and the most advantageous slot volume
can be determined by simple tests. The slot volume is directly proportional
to the employed current density or to the quantity of gas formed in the unit
of time, the slot inclination for anodes used in horizontal quicksilver-cells
being substantially 1 to 15. Still greater inclination angles produce no
additional advantages because, with increasing cross section of the slot out-
let, the flow velocity and therewith the electrolyte circulation reduces.
The disposition o a shield secured to the side of the electrode having the
greatest slot depth and extending just short of the surface of the electro-
lyte, and through which a slot-shaped channel is formed between shield and
cell wall or between the shields of two adjacent electrodes, produces an addi-
tional circulation-intensifying impetus.
The production of slotted forms of electrodes of solid metals, such
as titanium, for example, demands a high machining or other processing expense
and requires high material losses. Metal sheets, such as titanium sheets,
for example, are not suited for these advantageous forms of electrodes be-
cause of unsatisfactory mechanical stability. Furthermore, the slot lengths
of electrodes of a material that is not dimensionally stable, such as graph-
ite, for example, is shortened due to burn-off or abrasion in the course of
the electrolysis process, the circulation effect becoming increasingly lower
~4~3~
as the operating period increases.
Electrodes according to the invention are suited for electrolyses
of all types, for example for aqueous alkali chloride electrolysis, the elec-
trolysis of hydrochloric acid and of water, and they are suited for carrying
out organic oxidation and reduction processes, as anodes for cathodic corro-
sion protection, for fuel cells and galvanic cells.
Following are different examples of the method of producing the
electrode of the invention:
Example 1:
Titanium powder with a grain size < 0.06 ~m and rutile TiO2 powder
with a grain size < 0.01 ~m were premixed in a high-speed blade mixer, 5
parts by weight of a 2% aqueous polyvinyl alcohol solution was added thereto,
and the mixture was then mixed for an additional 10 minutes. The ratio of
Ti-powder to TiO2 powder was 7 : 1 to 1 : 3. The resultant mixture was com-
pressed in a forging press at a pressure of 2 Mp/cm2 into cylindrical members
having a diameter of 100 mm and a height of 50 mm, which were initially dried
at a temperature of 105C and then heated and sintered in argon at 1250C.
The cylinders were then provided by flame-spraying with a platinum
layer having a mean thickness of about 5 ~m, the adhesive strength of which
was tested by quenching the cylinders that had been heated to 200C in water
of about 18C. In comparison, coated cylinders of oxygen-free titanium,
after quenching only three to five times, already exhibited local cracks or
ruptures in the covering layer; with cylinders having the composition TiOX,
wherein 0.25 < x < 0.42 and wherein 0.60 < x < 1.50, the first very small
defects were able to be observed after quenching more than ten times; and
the covering layer of cylindrical members of the composition TiOX, wherein
x = 0.42 to 0.60 remained free of defects even after being quenched twenty
times, A further advantage of members having an oxygen-content of from 0.42
to 0.60 is the relatively low specific electrical resistance thereof~ where-
as members having an oxygen content x > 1.50 are little suited for electrodes
- 10 -
3~7
because of their high electrical resistance.
~xample 2-
61.4 parts by weight of titanium powder, having a grain size
< 0.06 ~m, and 38.6 parts by weight of rutile powder, having ~ grain size
< 0.01 ~m, the mol ratio being about 8 : 3, after an addition thereto of 5
parts by weight of a 2% aqueous solution of polyvinyl alcohol, were mixed in
a high-speed mixer for 10 minutes, and then compressed in a forging press at
a pressure of about 50 kp/cm2 into cylindrical members having a diameter of
50 mm. The pre-cast members were then dried at a temperature of 105C,
heated within four hours in an argon atmosphere at 1250C, then were commi-
nuted in a jaw crusher and ground in a vibratory mill to a grain size
< 0.06 ~m. The brittle, gray cast iron-colored powder had a composition of
Ti0.56-
5 parts by weight of a 10%-solution of hard paraffin in toluene
were added to 100 parts by weight of powder, which was then mixed for 5 min-
utes in a turbulence mixer, and the mixture subsequently compressed in a
forging press at a pressure of 2.5 Mp/cm2 into plates having dimensions of
350 x 450 x 10 mm and provided on one side thereof with ribs and cylindrical
recesses having a diameter of 2.5 mm. The plates were then dried at 110C,
and heated in a pass-through furnace in an argon atmosphere to 1300C for a
period of three hours. The electrical resistance of the densely sintèred
plates provided with a metallic polish was ahout 1.8 Q mm2/m, the available
pore volume was about 15%.
The plates provided as anode bases for alkali chloride electrolyte
cells were coated, on the side thereof facing the electrolyte bath, with
acidic alcoholic solutions of 10 Mol% Ru~13(H2O)1 5and 10 Mol% H2PtC16, and
heated in an argon atmosphere to 700C to burn or bake in the covering layer.
After cooling, the plates were coated with an alcoholic solution of 25Mol%
RuC13(H2O)1 5 and then heated in steam-saturated air to 650C. The very ad-
hesive, dark gray-to-black covering layer contained about 1.4 mg/cm2 noble
- 11 -
metal.
The plates were tested as anodes in an alkali chloride-amalgam cell.
The brine contained about 300 g/l NaCl, ~he temperature was 80C and the spac-
ing between electrodes was 2 mm. The plates were, respectively, subjected to
current densities of 10,000 to 20,000 A/m2 for 200 hours, and then microscop-
ically examined for changes in the covering layer. No damage to or loss of
the covering layer material was observed. The anode potential measured by
the Haber-Luggin capillary was 1.33 v with respect to a normal hydrogen elec-
trode and also remained unchanged.
Example 3:
37.5 parts by weight of titanium powder and 62.5 parts by weight of
rutile powder, the molar ratio being about 1 : 1, was mixed with 5 parts by
weight of an aqueous polyvinyl alcohol solution as in the foregoing Example 2,
compressed, dried and then heated in an argon atmosphere to 1300C. The re-
sulting pre-molded members having the mole ratio Ti : oxygen of 1 : 1 were
broken up, the fraction thereof having a width of 2 to 8 mm was separated by
a sieve, a 5% solution of a mineral wax in benzene was added thereto, and the
fraction and additive were then mixed and compressed with a pressure of 1.5
Mp/cm2 into plates having the dimensions 300 x 200 x 8 mm. A rib-like pat-
tern was simultaneously impressed into the surface thereof. The plates werethen sintered for three hours at a temperature of 1250C in a pure argon
atmosphere. The pore volume of the plates were abou~ 40%, and the mean pore
diameter was about 2 mm. The plates were then provided by flame-spraying
with a 0.9 ~m thick equimolecular platinum-iridium covering layer and heated
in argon to 700C to burn or bake-in the layer.
The plates were tested as anodes in a diaphragm test cell for pro-
ducing chlorine and soda lye at a current density of 6 kA/m2 and a brine tem-
perature of 70C. The loss of noble metal was less than 0.1 g/t (grams per
ton) of chlorine produced.
- 12 -
3'7
Exam~le 4:
61.4 parts by weight of titanium powder having a grain size
< 0.06 ~m and 38.6 parts by weight of rutile powder having a grain size
< 0.01 ~m, the molar ratio thereof being about 8 : 3, were mixed in a high-
speed mixer for 10 minutes after the addi~ion thereto of 5 parts by weight
of a 2~ aqueous polyvinyl alcohol solution, and then compressed in a forging
press at a pressure of about 50 kp/cm2 into cylindrical members having a dia-
meter of 50 mm. The thus-formed pre-molded members were dried at a tempera-
ture of 105C, were heated in an argon atmosphere to 1250C for four hours,
then comminuted in a jaw crusher, and ground to a grain size < 0.06 ~m in a
vibratory mill. The brittle, grey cast-iron colored powder had a composition
of TiOo 56. The powder was then placed in a die and covered with a layer of
titanium powder having a grain size < 0.1 mm. The powder layers were then
compressed with a pressure of 2.5 Mp/cm2 into plates having the dimensions
350 x 450 x 10 mm and having on one side thereof ribs and cylindrical reces-
ses with a diameter of 2.5 mm, and the TiOx-sides of the plates were coated
with an acidic alcoholic solution of 10 Mol% RuC13(H20~1 5 and 10 Mol%
H2PyC16, then dried at 110C and thereafter heated in a pass-through furnace
in an argon atmosphere to 1300C, the dwell time therein being three hours.
After cooling, the plates were coated with an alcoholic solution of 25 Mol%
RuC13(H20)1 5 and then heated in steam-saturated air to 650C.
With respect to the foregoing example, welding of the current or
power-supply rods of titanium to the titanium side of the electrode base was
effected according to the metal-inert gas method with titanium fusing elec-
trodes, according to the tungsten-inert-gas method with titanium as additive
material, and according to the resistance welding method respectively under
argon as protective gas. The connections produced in accordance with the
welding operation were free of cracks or tears, and the few millivolts ~ol-
tage-drop between the base and the current-or power-supply rods remained
constant when employine the elec~rode~ in an alkali chloride electrolyte cell.
~';
Other features which are considered as characteristic for the in-
vention are set forth in the appended claims.
Although the invention is illustrated and described herein as elec-
trode for electrochemical processes and method of producing the same, it is
nevertheless not intended to be limited to the details shown, since various
modifications may be made therein without departing from the spirit of the
invention and within the scope and range of equivalents of the claims.
The invention, however, together with additional objects and ad-
vantages thereof will be best understood from the following description when
read in connection with the accompanying drawing, in which:
Figure 1 is a plot diagram of the electrical resistance of Ti0X;
Figure 2 is a diagrammatic perspective view of an electrode accord-
ing to the invention having parallel top and bottom surfaces;
Figure 3 is a view similar to that of Figure 2 showing another em-
bodiment of the electrode having an inclined upper surface; and
Figure 4 is another diagrammatic perspective view of the embodiment
of Figure 2 in a cell and showing the direction of flow of brine or electro-
lyte and gas bubbles.
Referring now to the drawing and first, particularly to Fig~lre 1
thereof, there is shown a plot diagram of the specific electrical resistance
of a cylindrical electrode constructed in accordance with the invention
against the oxygen content thereof. The resistance increases at a constant
rate from virtually oxygen-free titanium, passes through a maximum at x =
0.25 and decreases at a constant rate to a minimum at x = 0.50. In region I
of Figure 1, there is under consideration an C~ - Ti addition mix-crystal
with oxygen held in octahedral gaps or vacancies, in region III the compound
TiO is stable, the points of the lattice structure thereof being incomplete-
ly occupied. The resistance increases in the latter region and passes through
an intermediate maximum and minimum at x = 0.9 and x = 1.0, respectively. In
the region II, which extends between x = 0.42 and x = 0.60, the disrupted
- 14 -
L3~
G~ -Ti and TiO-phases occur side-by-side. In the regions IV and V wherein
the resistance further increases, there are presented, finally, mixtures of
TiO and Ti203 and Ti203, respectively.
An electrode 1 of sintered titanium oxide TiOX, according to the
invention, is shown in Figure 2. The covering layer containing activating
material as well as the connection of the electrode to the current or power
source is not illustrated in the figure. Inclined slots 2 extend from one
side 3 to the opposite side 4 of the electrode 1, at an inclination to the
bottom surface of the electrode 1, the slots 2 being deepest at the side 3
of the electrode.
The embodiment of the electrode 1', according to the invention,
shown in Figure 3, has an upper surface 5 that is inclined with respect to
the lower surface thereof, as viewed in that figure, whereas the correspond-
ing surfaces in the embodiment of Figure 2 extend substantially parallel to
one another. With respect to cost of material, the embodiment of Figure 3
is more advantageous over that of Figure 2. The inclination of the upper
surface 5 expediently corresponds to the inclination of the slots 2 formed
in the lower surface. A titanium shield or plate 6 is secured by any suit-
able means such as welding, to the side 4 of the electrode 1' to increase the
upward drive of the gas bubbles, and extends up to just below the non-illus-
trated surface of the electrolyte in a cell wherein the electrode l' is re-
ceived.
In Figure 4, there is shown a trough 7, filled with non-illustrated
electrolyte wherein the electrode 1 of Figure 2 is immersed. The gas bubbles
rising at the side 4 of the electrode 1, as represented by the upwardly direc-
ted arrows located thereat, effect a displacement of the spent electrolyte
` in the same direction, while fresh, gas-bubble-free brine or electrolyte flows
; downwardly from the upper side 5 of the electrode 1 as shown by the arrows
on the right-hand side 3 of the electrode 1, takes the place of the gas bub-
bles that had formed at the underside of the electrode 1, and rises as gas
~`
; - 15 -
l~U~3'7
bubble-enriched brine between the left-hand surface 4 and the wall of the
trough 7 adjacent to and spaced there~rom.
The voltage drop of a horizontal alkali chloride cell with quick-
silver i.e. mercury, cathode and an anode in the embodiment of Figure 2 was
4.0 to 4.1 v for a current density of 10 kA/m2 and a K-value of 0.09 vm2/kA.
Under the same conditions, the voltage drop of a cell with an anode formed
of a succession of parallel-disposed vertical titanium bands was 4.25 to
4.30 v.
- 16 -
