Note: Descriptions are shown in the official language in which they were submitted.
This application describes and claims certain improvements in the
basic electrochemical cell disclosed in United States patent 3,791,871.
The basic mechanism of the cell is described in United States pat-
ent 3,791,871. Briefly, the cell utilizes a reactive metal anode highly
reactive with an aqueous electrolyte and spaced from the cathode by an elec~,
trically insulating film which forms naturally on the anode in the presence
of water. This thin film permits the cathode to be placed in direct contact
with the anode. The resulting reduction in the anode-cathode spacing to a
thickness no greater than the thickness of this film greatly reduces the I2R
-` 10 losses which would otherwise be present and results in increased power output
and energy density. The anode and cathode operate in an aqueous electrolyte
which supports the beneficial electrochemical reaction. The cathode is
beneficially formed of an open-mesh metallic screen contoured to contact the
anode over substantially the entire operating surface.
~uring operation of the cell, molarity of the electrolyte increases
with a resulting decrease in power output. Further, excess heat must be re-
moved from the electrolyte which would otherwise result in a loss of effici-
ency. Likewise, depolarization of the cell must be accomplished by removal
of hydrogen gas evolved at the cathode. Accordingly, the electrolyte is
` 20 normally pumped through the cell in order to remove heat, bring in additional
;; oxidant to maintain desired molarity and remove hydrogen. The use of mech-
anical pumps and heat exchangers for this purpose are cumbersome, consume
power and generate noise, all of which are undesirable.
This invention relates to a self-pumping reactive metal anode-
aqueous electrolyte electrochemical cell consisting essentially of a vertical
hollow tubular casing, a reactive anode bonded to the interior surface of
said casing, said anode naturally forming on its surface a protective insul-
ating film in the presence of water, an expandable coiled metal open-mesh
- screen cathode positioned within the interior of said tubular casing and con-
tacting said insulating film over substantially all of the anode surface
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facing said cathode, said cathode pressing continuously against said
insulating film during operation of said cell, an aqueous electrolyte filling
the interior cavity of said hollow tubular casing and flowing from the bottom
to the top of said cell, and a reservoir containing aqueous electrolyte in
fluid communication with the top and bottom of said cell, whereby electrolyte
is drawn up through said cell by evolved heat and gas generated during
operation of said cell and electrolyte is drawn down through said reservoir
as it cools.
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Briefly, in accordance with the invention, there is described a
configuration which dispenses with the necessity of mechanical pumps and
heat exchangers and, by use of the products of the electrochemical reaction,
is self-pumping, the pumping force being supplied by the waste heat and
hydrogen gas evolved. The configuration has the further advantage of reduc-
ing non-working anode edge surfaces which would normally be exposed to the
electrolyte and therefore subject to parasitic erosion.
More particularly, in accordance with the invention, a reactive
anode is bonded to the interior surface of a tubular casing and a coiled
metal screen cathode is positioned within the casing. The coiled screen
presses continuously against the working surface of the anode during the
lifetime of the battery. The circular construction of the anode does not
provide ~ny non-working exposed edges other than the small top and bottom
seams at the ends of the tube and parasitic erosion is accordingly minimized.
- During operation, reaction of the lithium with the electrolyte in the in-
terior cavity of the casing causes the electrolyte to be heated thereby
establishing a thermal gradient in the cell. This gradient and the buoyancy
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of the hydrogen gas evolved at the cathode creates a flow of electrolyte
through the cell, with hot electrolyte containing hydrogen gas exiting from
- 20 the top of the cell and fresh oxidant being drawn into the bottom of the cell.
The various features and advantages of the invention will become
apparent upon consideration of the following description taken in conjunction
with the accompanying drawing of the preferred embodiment of the invention.
The views of the drawing are as follows:
~ FIGURE 1 is a top view of two self-pumping cells of the invention
.- operating from a common reservoir; and
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FIGURE 2 is a edge cross-sectional view of the cells of Figure l.
With reference to Figures 1 and 2, where like reference characters
designate corresponding parts throughout the several views, there is depicted
two cells of the invention 1 and 2 operating, in this.embodiment, from a com-
mon reservoir 3. Reactive metal anodes 4 are bonded, for example by metal-
urgical means, to the inside walls of the tubular metal casings 5. me in-
sulating film 6 which forms naturally on anodes 4 electrically separates an-
odes 4 from expanding coiled metal screen cathodes 7. As the anode 4 is con-
sumed in operation, the cathode 7 expands to maintain contact with the anode.
A cathode current collector 8 is bonded to each screen cathode 7 and an an-
ode connector 9 is bonded to the exterior of each cell casing 5.
In the embodiment shown in the drawing, two cells l and 2 are con-
nected to a central reservoir 3 by means of pipes 10 and 11. me upper pipes
10 are for egress of the circulating electrolyte 12 and the lower pipes ll
are for ingress of the electrolyte into the cells. To enhance rejection of
heat to the environment the depicted cells and central reservoir may be im_
mersed in a liquid bath such as water. If the liquid bath is an electrically
conducting fluid, the exterior surfaces of metal casings ~5) are electrically
insulated, for example, with an insulating epoxy paint, not shown. Natur- --
ally, there may be only one or more than two cells connected to a central
reservoir instead of the two cells depicted in the drawing.
; As the cells operate, the electrolyte 12 circulates down through
the reservoir 3 as it cools and evolves the entrained hydrogen and enters the
cells 1 and 2 by way of pipes 11. Evolved hydrogen is vented through relief
valve 13. Oxidant, norm~lly water, is admitted through inlet pipe 14 as ~e-
quired to keep the cells operating at the desired power level.
; As discussed in United States Patent 3,791,871, molarity of the
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electrolyte is varied to control power output of the ceIls. Whereas conven-
- tional batteries decline in both voltage and power during discharge reaching
a point of unacceptable low voltage before the active materials are consumedS
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voltage and power in the cells of the invention are maintained at the desired
level throughout the life of the anode. The voltage and power output per unit
area of cel~s of the invention are primarily dependent on electrolyte concen-
tration and temperature. The temperature is maintained relatively constant by
the configuration of the cells of the invention. Accordingly, control of
voltage and power is accomplished by varying the molarity of the electrolyte~
~uring operation, the cells of the invention produce a reactive metal hydrox-
ide at the anode which tends to reduce power output as the concentration ex-
ceeds in optimum molarity which can be readily calibrated. Accordingly, an
oxidant, typically water, is added to the electrolyte to control molarity,
that is, reduce the hydroxide concentration~ The control function used to
control power output is total cell voltage. Variations of voltage above or
below the desired level is sensed by an electronic sensor which actuates a
solenoid value which in turn controls the rate of water addition through pipe
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14 to the electrolyte. Excess electrolyte generated by such oxidant additions
is vented through valve 13.
Anode 4 is formed of a reactive metal such as sodium or lithium
which is highly reacting with and in the presence of water naturally forms
on its surface a protective insulating film. Alloys and compounds of such ;
alkali metals and other reac~ive metals should be equally feasible for use
as the anode provided they are substantially as reactive with water as are
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sodium and lithium and furtherprovided, in common with sodium and lithium,
they naturally form a continuous insulating film in the presence of water.
The open-mesh screen cathode is of any suitable electrically conductive
material which is non-reactive with water and will permit electrochemical
reduction of water during operation of the cell. Illustratively, iron and
nickel are preferred materials with black platinum and black nickel provid-
ing increased efficiency at the expense of high cost and reduced durability.
The minimum size of the screen is governed by the need to get
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electrolyte to the anode face plus the need to remove the products of reaction
away from the face. The maxLmum screen si~e is governed by the desire to
keep all parts of the anode face as near as possible to the cathode. Illus-
tratively, for an anode surface measuring 5 inches by 11 inches, a metal
screen- with 0,003 inch metal and 0 1 inch by 0.5 inch openings has produced
excellent results.
During operation, the cells of the invention produce a metal hydr_
oxide, the particular metal being dependent on the composition of the anode.
Accordingly, for ease of operation, the aqueous electrolyte is preferably the
same as that produced by the reactive metal-water reaction. However, any one
of a number of other aqueous solutions sho~ld be equally feasible as a s~art-
ing electrolyte provided such electrolytes have the requisite film forming
charac~eristics, When dry storage is desired the reservoir 3 may be filled
with appropriate dry electrolytes such as lithium hydroxide monohydrate and
the cell activated by the introduction of water into the reservoir~
While a central reservoir is not required for single or multiple
cell operation, it is considered desirable for multiple cell operation in that
the reservoir contributes to maintaining electrical balance between multiple
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-~ cells by providing all cells with electrolyte of equal molarity and temper-
ature.
Illustratively, four tubular cells, 6 inches long and 1 inch in
diameter, containing 1/8-inch of lithium bonded to the ~nner walls of each
` tube for a length of 52linches, were operated connected to a central reservoir
containing 1,0 molar lithium hydroxide solution in LiC1 for two hours at a
power level of 50 watts. The temperature of the electrolyte was 28C and the
unit was operated in aqueous media at a temperature of 25C,
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