FRIEDMAN MARK M (IL)
US5181969A | 1993-01-26 | |||
US4021371A | 1977-05-03 | |||
US4935055A | 1990-06-19 | |||
US4847048A | 1989-07-11 | |||
US4629505A | 1986-12-16 | |||
US4874578A | 1989-10-17 | |||
US4072516A | 1978-02-07 | |||
US4100038A | 1978-07-11 | |||
US4536259A | 1985-08-20 | |||
US4146678A | 1979-03-27 | |||
US3960607A | 1976-06-01 |
1. | A method of making material for use in fabricating an anode for use in a chemical current source, comprising (a) heating a mixture including aluminum and magnesium to at least the fusion point of said mixture in the presence of hydrogen to form a molten mass; and (b) cooling said molten mass to form the anode material. |
2. | A method as in claim 1 wherein said mixture further includes solder, potassium hydroxide, nitride of nickel, nitride of zinc, or nitride of titanium, or combinations thereof. |
3. | A method as in claim 2 wherein said mixture includes magnesium, aluminum, solder, potassium hydroxide, nitride of nickel, nitride of zinc, and nitride of titanium. |
4. | A method as in claim 3 wherein said mixture includes 752 wt% magnesium, 3884 wt% aluminum, 24 wt% solder, 0.51.5 wt% potassium hydroxide, 0.51. |
5. | wt% nitride of nickel, 3. |
6. | wt% nitride of zinc, and 14 wt% nitride of titanium. |
7. | 5 A method of making material for use in fabricating an anode for use in a storage battery, comprising (a) heating a mixture including aluminum and magnesium to at least the fusion point of said mixture in the presence of hydrogen to form a molten mass; and (b) cooling said molten mass to form the anode material. |
8. | A method as in claim 5 wherein said mixture further includes solder, potassium hydroxide, nitride of nickel, nitride of zinc, nitride of titanium, nickel hydroxide, or combinations thereof. |
9. | A method as in claim 6 wherein said mixture includes magnesium, aluminum, solder, potassium hydroxide, nitride of nickel, nitride of zinc, nitride of titanium and nickel hydroxide. |
10. | A method as in claim 7 wherein said mixture includes 752 wt% magnesium, 3884 wt% aluminum, 24 wt% solder, 0.51.5 wt% potassium hydroxide, 0.51.5 wt% nitride of nickel, 35 wt% nitride of zinc, 14 wt% nitride of titanium and 35 wt% of nickel hydroxide. |
11. | An anode made by the method of claim 1. |
12. | An anode made by the method of claim 5. |
13. | A chemical current source, comprising: (a) an anode made by the method of claim 1 serving as an anode; (b) a cathode; (c) an electrolyte into which said anode and said cathode are immersed. |
14. | A chemical current source as in claim 11 wherein said cathode is made of activated carbon. |
15. | A chemical current source as in claim 11, further comprising a heater for heating said anode. |
16. | A storage battery, comprising: (a) an anode made by the method of claim 5 serving as an anode; (b) a cathode; (c) an electrolyte into which said anode and said cathode are immersed. |
17. | A storage battery as in claim 14 wherein said cathode is an oxygennickel cathode. |
18. | A storage battery as in claim 14, wherein said electrolyte is an alkaline solution containing zincates, stannates, aluminates, fluoric sodium, or potash, or combinations thereof. |
19. | An energy plant, comprising: (a) a chemical current source according to claim 11; and (b) a storage battery according to claim 14, said anode of said storage chemical current source being electrically connected to said anode of said storage battery and said cathode of said storage chemical current source being electrically connected to said cathode of said storage battery. |
FIELD AND BACKGROUND OF THE INVENTION
The present invention relates to a chemical current source and
storage batteries and, more particularly, to methods of preparing water-
activated batteries with soluble anodes of a chemical current source and
storage batteries.
Many chemical current sources are known. These differ in their
dimensions, in their manner of construction and in the nature of the
electrochemical reactions which take place in the sources. The current
sources also vary in their use-related properties, such as, for example, their
applicability to underwater or above-water devices, rescue and signaling
equipment, electric vehicles, and the like.
It is common to intensify the reactions taking place at the electrodes
of a chemical current source by making use of various metallic alloys for
the fabrication of the negative electrode (anode).
Chemical current sources can be described and rated in terms of
various performance indicators, such as their energy density, their capacity,
and their internal resistance per unit area of electrode surface or per unit
mass or per unit volume of the cell.
Additional considerations are cost and availability of the materials
needed for the construction of the electrodes, and the service life and shelf-
life of the current source, as well as the ecological effects of its production,
use and discarding.
The active portions of the electrodes may, in theory, be made of any
of a large variety of metalloids, including those which are aluminum and
magnesium based. Based on energy density consideration, the choice is
usually limited to metalloids which include lead, nickel, cadmium, iron,
manganese, zinc, lithium, silver, alone or in combination.
There have been attempts to produce chemical current sources with
electrodes of aluminum and magnesium, but these attempts have not found
wide application due to their inherent shortcoming of the high resistivity
of the protective oxide layer which tends to form around the anode and
which leads to a potential barrier of about 1 volt. This potential barrier,
in turn, produces a highly negative differential effect which increases the
corrosion current and increases of the anodic current density.
It is largely this limitation which has tended to rule out the use in
chemical current source anodes of aluminum alloyed with rare metals, such
as indium, thallium and gallium. Other considerations, such as the high
cost and relatively high toxicity, also played a role.
A further shortcoming of known water-activated chemical current
sources, and of air-magnesium cells in particular, is their inability to
operate intermittently. This is caused by the high self-discharge and the
corrosion of the anode, which is permanently activated following its initial
operation.
There is thus a widely recognized need for, and it would be highly
advantageous to have, an inexpensive and long-lasting chemical current
source, capable of generating a large current density over a long period,
including in intermittent use.
SUMMARY OF THE INVENTION
According to the present invention there is provided a method of
making material for use in fabricating an anode for use in a chemical
current source, comprising: (a) heating a mixture including aluminum and
magnesium to at least the fusion point of the mixture in the presence of
hydrogen to form a molten mass; and (b) cooling the molten mass to form
the anode material, and an anode made in this way.
Also according to the present invention there is provided a method
of making material for use in fabricating an anode for use in a storage
battery, comprising: (a) heating a mixture including aluminum and
magnesium to at least the fusion point of the mixture in the presence of
hydrogen to form a molten mass; and (b) cooling the molten mass to form
the anode material, and an anode made in this way.
According to further features in preferred embodiments of the
invention described below,
According to still further features in the described preferred
embodiments, the mixture used to fabricate an anode for use in a chemical
current source further includes solder, potassium hydroxide, nitride of
nickel, nitride of zinc, or nitride of titanium, or combinations thereof. A
mixture used to fabricated an anode for use in a storage battery is further
made up of nickel hydroxide.
An anode according to the present invention can be used, along with
a cathode and an electrolyte, to form a chemical current source, which
preferably features means for heating the anode.
Anodes according to the present invention can be used, along with
appropriate cathodes electrolytes, to form an energy plant which includes
a chemical current source and an electrically connected storage battery.
BRIEF DESCRIPTION OF THE DRAWINGS
The invention is herein described, by way of example only, with
reference to the accompanying drawing, which schematically depicts an
energy plant.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
The present invention is of a method of fabricating an anode and of
an anode, for use in chemical current sources and in storage batteries.
The present invention addresses the task of improving the
performance characteristics of chemical current sources by making use of
a water-activated negative electrode (anode) made of a magnesium-
aluminum alloy impregnated with hydrogen. The magnesium-aluminum
is brought to the molten state under an atmosphere of hydrogen, in the
presence of one or more additives which facilitate the impregnation of the
melt by hydrogen.
To fabricate an anode according to the present invention, magnesium
and aluminum granules are mixed one or more additives, such as granules
of solder, granules of potassium hydroxide, powdered nitrides of nickel,
zinc and titanium, and the like. Any suitable proportions may be used.
Preferably, the magnesium, aluminum, solder, potassium hydroxide, nitrides
of nickel, nitrides of zinc and nitrides of are in the following mass-
proportions: 7-52%, 38-84%, 2-4%, 0.5-1.5%, 0.5-1.5%, 3-5% and 1-4%,
respectively.
The mixture is heated under hydrogen atmosphere, to above the
melting temperature, so as to form a molten mass. The melt is
subsequently cooled or allowed to cool and harden to some suitable
temperature, forming the anode material. Preferably the cooling takes
place in molds which are shaped and sized so as to result in a finished
anode after cooling.
Without in any way limiting the scope of the present invention, it
is believed that these operations result in the formation of solid solutions
and compounds. The resultant anode possesses higher electrochemical
activity.
Without in any way limiting the scope of the present invention, it
is believed that the heat treatment of the aluminum/magnesium alloy at the
liquefying point under hydrogen, at adequate pressure, affects the electronic
state and modifies the structural parameters of the aluminum and of the
magnesium initiating the penetration into their crystalline lattice of
hydrogen atoms, that is, of protons, which are all bound in a medium
replete with free electrons. The number of electrons at the bound level
may be two, that is, hydrogen plus whatever ion forms an H ' , which causes
less anode metal polarization and heightens the resistance to corrosion,
typically be a factor of 2, on account of the higher toughness due to
intensive hydrogen penetration into the metal surface, which passivates it.
The formation of the H " ion causes a shift of the potential of the
chemical current source at the magnesium/aluminum anode, without the
formation or release of any toxic admixtures. The resultant anode has
increased resistance to electrochemical corrosion.
The discharge current density is capable of instantaneously reaching
from 2 to 500 milliamperes/cm.sq., and higher.
The higher stability of magnesiunValuminum alloys and the reduced
corrosion due to the negative differential effect testify to the effect which
passivation has at relatively low current densities and chemical current
source self-discharge. The increased corrosion resistance throughout the
anode volume is therefore practically realized by the anode reagent all over
the magnesium-aluminum electrode volume. The working under hydrogen
also has a beneficial influence on the electrochemical activity of the
resultant intermetallic compounds of aluminum-magnesium-tin-lead-zinc-
nickel.
The method for fabrication of chemical current source according to
the present invention achieves improved technical characteristics, and yields
chemical current sources which are capable of fast discharge.
EXAMPLE
Granules of magnesium and aluminum were mixed with granules of
solder and KOH and nickel, zinc and titanium nitride at the following mass
proportions: 44%, 45%, 3%, 1%, 1%, 4% and 2%, respectively. The
mixture obtained was enclosed in an electrical graphite crucible, and heated
to the fusion point under hydrogen. The resultant substance was cooled
down to an acceptable temperature for fabrication of electrodes.
A chemical current source anode made as described above may be
used to fabricate a chemical current source. The anode is immersed in an
electrolyte, which is preferably water. Also immersed in the electrolyte is
a cathode which can be made from any suitable material, preferably
activated carbon. Preferably, means are provided to heat the anode of the
current source in order to improve its performance.
Precisely the same techniques described above can be used to
fabricate an anode for use in a storage battery. Preferably, the mixtures
used to fabricate an anode for use in a storage battery will, in addition, also
contain 3-5 wt% of nickel hydroxide.
A storage battery anode made as described above may be used to
fabricate a storage battery. The anode is immersed in an electrolyte, which
is preferably an alkaline solution containing one or more of the following:
zincates, stannates, aluminates, fluoric sodium, or potash. Also immersed
in the electrolyte is a cathode which can be made from any suitable
material, preferably an oxygen-nickel cathode.
A chemical current source and a storage battery as described above
may be combined to form an energy plant. One example of such an
energy plant is depicted schematically in the Figure. The energy plant is
made up of a chemical current source 10 and a storage battery 12.
Chemical current source 10 includes a current source anode 14 and a
current source cathode 16 immersed in a current source electrolyte 18.
Heating means 20 are available to heat current source anode 14.
Storage battery 12 includes a battery anode 22 which is electrically
connected to current source anode 14, and a battery cathode 24 which is
electrically connected to current source cathode 16. Battery anode 22 and
battery cathode 24 are immersed in a battery electrolyte 26.
While the invention has been described with respect to several
preferred embodiments, it will be appreciated that many variations,
modifications and other applications of the invention may be made.
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