Title of Invention

SILVER/CARBON -BASED MATERIAL AND METHOD FOR PRODUCING THE SAME

Abstract The invention relates to a method for producing a silver/carbon-based material, comprising the following steps: (i) providing a carbon particle suspension; and (ii) adding a solution from a silver compound and a reducing agent so that a silver-containing precipitate is deposited onto the carbon particles, the carbon particles having an average diameter of 200 nm or more. The invention also relates to materials obtained by this method, and to the use of the materials in protective switches for low-voltage power engineering.
Full Text 040056 TM
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Silver/carbon-based material
and method for producing the same
Description
The present invention relates to a process for preparing a material based on silver-
carbon and a material obtainable therefrom. The use of the material is likewise
described.
Materials for electrical contacts in power engineering consist generally of silver and
particular metallic and/or nonmetallic or oxidic additives. Such materials are produced
predominantly by a powder metallurgy route. In this method, the components are mixed
with one another in powder form.
The application profile of such contact materials is determined crucially by the
switching device type, the magnitude of the switching current and the type of electrical
load. The operating conditions require low electrical wear, i.e. high arc erosion
resistance, and low welding force with simultaneously low contact resistance.
Contact materials based on silver-carbon, especially silver-graphite, have found use
particularly in the sector of circuit breakers in low-voltage power engineering. The
crucial factor here is especially ultra-high reliability with respect to the welding of the
contact pieces.
Improvement in the processing and contact properties of these materials is the constant
motivation for further material and technology developments. At the forefront is the
optimization of the two switch properties of arc erosion resistance and welding
resistance. These are actually opposing with regard to the carbon content. In other
words, with increasing carbon content, protection against welding generally becomes
better, but the arc erosion resistance decreases (E. Vinaricky "Elektrische Kontakte,
Werkstoffe und Anwendungen" [Electrical contacts, materials and applications!;
2nd edition, Springer Verlag; 2002; p. 251-255).
The addition of carbon also brings about mechanical strengthening of the material, such
that the producibility and processibility of the material becomes more difficult with
rising carbon content. This effect occurs especially when a powder metallurgy mixture
of the two components is to be compacted and reshaped by extrusion. At carbon
contents of more than about 5%, the material can be extruded only with very great

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difficulty.
EP-A-311 134 discloses a material produced by powder metallurgy for electrical
contacts composed of silver with from 2 to 7% by weight of graphite and a specific
additive which enhances the strength of the material.
EP-A-736 885 describes a material for electrical contacts composed of silver-carbon,
which has improved arc erosion properties. This material comprises carbon exclusively
in the form of carbon black with a mean primary particle size of less than
150 nanometers. The material is produced by cold isostatic pressing and sintering.
WO 92/18995 relates to a particular composite material for electrical contacts. The
composite material is based on silver and contains from 0.5 to 10% by weight of carbon,
carbon powder being processed in combination with carbon fibers in a mass ratio of
from 10:1 to 1:10 together with the silver component by powder metallurgy to give a
material. On average, the length of the carbon fibers is more than double the diameter of
the carbon powder particles.
A further composite material for electrical contacts is disclosed in EP-A-729 162. It is
produced using carbon fibers which have been subjected to a specific comminution
process.
In the above-described publications, the material was produced by powder metallurgy.
In the Chinese patent CN-A-1396025, a chemical reduction process for producing
silver-graphite material is presented. In this process, graphite nanopowder having a size
of about 20 nm is used. The graphite powder is introduced into a reaction vessel and
mixed with silver nitrate solution. Subsequently, hydrazine hydrate solution is added,
such that a silver layer is deposited onto the graphite nanopowder. The graphite
nanopowder coated with a silver layer is subsequently processed further by means of
individual pressing and sintering. This process has the disadvantage that the hydrazine
hydrate used is hazardous to health and is consequently undesirable for industrial scale
application. The present inventors have additionally found that the material obtained by
this process is not sufficiently finely dispersed and homogeneous. Furthermore, the
material has excessively high strengthening, such that processing by extrusion is
possible only under costly conditions, if at all. The processing by individual pressing
proposed in CN-A-1396025 is usually comparatively undesirable on the industrial scale
from an economic point of view.
DE-A-100 17 282 describes a particular two-nozzle precipitation process for producing

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composite powder. The composite powders are, unlike the inventive materials, not
materials based on silver-carbon but rather materials based on silver-tin oxide. Silver-tin
oxide contact materials and, more generally, silver-oxide contact materials are used
mainly for contactors which switch under air for low-voltage and high-voltage
engineering. The main objective of their function is to ensure very many switching
cycles, for example for an engine control system. The material and switching device are
such that several tens of thousands (AC4 switching response) to millions of switching
cycles (AC3 or AC1 switching response) are possible according to the switching
conditions. Accordingly, these materials must have good arc erosion behavior and
acceptable reliability with respect to welding.
Materials based on silver-carbon, in contrast, are used very predominantly in circuit
breakers (for example line circuit breakers, engine circuit breakers, power switches) in
low-voltage power engineering. The switches serve here for the safety of people and
equipment. In the case of failure, for example a short circuit, ultra-high requirements are
made here on welding reliability, i.e. they must never become welded. Since the
switches should be triggered only in the case of emergency, a significantly lower
number of switching operations is accepted here. According to the switching condition,
this may only be a few dozen, or a few hundred up to a maximum of a few thousand
switching cycles. Frequently, asymmetric material pairs are used in order to take
account of peculiarities in construction and economic aspects. These are material pairs
such as AgC with Cu, AgW, Ag-metal oxide or AgNi. There is therefore no
comparability with silver-tin oxide materials.
It was an object of the present invention to provide materials based on silver-carbon,
which have improved welding resistance, arc erosion resistance and/or processibility.
Accordingly, the invention relates to a process for producing a material based on silver-
carbon, comprising the steps of:
(i) providing a suspension of carbon particles; and
(ii) supplying a solution of a silver compound and of a reducing agent, such that a
silver-containing precipitate is deposited onto the carbon particles,
where the carbon particles have a mean diameter of 200 nm or greater.
The invention further relates to a material obtainable by this process, and to the use of
the material in circuit breakers for low-voltage power engineering.

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Figure 1 shows a schematic illustration of an apparatus which can be used in a preferred
embodiment of the process according to the invention.
A reaction vessel (1) is initially charged with a suspension of carbon particles (2). These
are mixed intensively by a stirrer (3). By means of two separate feed lines (4; 5), whose
nozzles are below the liquid level of the suspension (2), one solution in each case of the
silver compound (4') and reducing agent (5') are fed to it simultaneously, as a result of
which silver-containing precipitate is deposited onto the suspended carbon particles.
In the process according to the invention, a suspension of carbon particles is initially
provided. The carbon particles are not particularly restricted. It is possible to use all
carbon particles which are typically used in materials based on silver-carbon. They are
preferably selected from graphite powder, carbon fibers and carbon black, and also
combinations thereof, particular preference being given to graphite powder and carbon
fibers. The carbon fibers preferably have a mean diameter of from 500 to 15 000 nm,
more preferably from 2000 nm to 7000 nm.
The carbon particles can, for example, be divided into spherical and fibrous carbon
particles. Spherical carbon particles, for instance graphite powder and carbon black,
generally have an essentially spherical shape. In this context, "spherical" means that the
particles have essentially equal longitudinal dimensions in all three spatial directions.
The mean diameter of the spherical carbon particles is 200 nm or greater. In contrast to
these are fibrous carbon particles such as carbon fibers. Fibrous carbon particles are
defined here as particles which, in one spatial direction, have a longer dimension than in
the other two spatial directions. Typically, the fiber length, relative to the fiber diameter,
has a ratio of at least 2:1, preferably at least 5:1. The maximum fiber length is, for
example, 20:1 in relation to the fiber diameter. The mean diameter (fiber diameter) of
the fibrous carbon particles is 200 nm or greater. Typical fibrous carbon particles have a
diameter of from 0.5 to 30 µm, preferably from 1 to 20 µm, particularly preferably from
3 to 10 µm and have corresponding fiber lengths in each case.
In one embodiment, the carbon particles are a mixture of graphite powder and/or carbon
blackxarbon fibers in a ratio of from 20:1 to 1:20. The mixture consists preferably of
from 100% by weight to 98% by weight of graphite powder and from 0% by weight to
2% by weight of carbon black (based on the total weight of graphite and carbon black)
in combination with carbon fibers. This is advantageous when the arc erosion resistance
and welding resistance are to be balanced with respect to one another for a specific
switching device. In another embodiment, only graphite powder is used as carbon

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particles. This is of interest when an optimal welding reliability is to be achieved. In a
third embodiment, only carbon fibers are used as carbon particles. This allows the arc
erosion resistance to be enhanced.
The carbon particles are suspended in a liquid. The type of liquid is not particularly
restricted. However, it should react neither with the carbon particles, nor the silver
compound, nor the reducing agent, nor the silver-containing precipitate. Examples of
suitable liquids are water, suitable organic solvents (e.g. alcohols) and combinations
thereof. In addition, it is possible to use wetting aids, for example surfactants, in order
to facilitate the suspension of the carbon particles. Preference is given to using water.
The concentration of the carbon particles in the suspension is likewise not particularly
restricted. It is generally selected such that the suspension has a suitable viscosity and
the subsequent reduction proceeds advantageously. Too high a liquid content should,
however, be avoided, since the liquid has to be removed again. The optimal
concentration can be selected in a suitable manner without any problem by the person
skilled in the art. It is preferably in the range from 0.1 to 25% by weight of carbon
particles in the suspension.
In order to deposit a silver-containing precipitate onto the carbon particles, a solution of
a silver compound and a reducing agent is added to the suspension of carbon particles.
The solution of the silver compound can be added to the suspension of carbon particles
before, after or simultaneously with the reducing agent. A preferred addition process is
described in DE-A-100 17 282. The process described relates to the chemical reductive
precipitation of silver-containing precipitate onto tin oxide particles. However, it can be
used analogously for the chemical reductive precipitation of silver-containing
precipitate onto carbon particles.
The silver compound used is not particularly restricted and may, for example, be any
soluble silver salt. Examples thereof are nitrates, acetates, carbonates, citrates and
oxalates. Preference is given to using nitrates. The silver compound used is preferably
dissolved in water or a suitable organic solvent (e.g. alcohol). In general, water is used
as the solvent.
The silver-containing precipitate is preferably metallic silver.
Useful reducing agents are all compounds which can reduce the silver compound.
Typical examples are ascorbic acid, citric acid, oxalic acid, formic acid and
hydroxylamine. The reducing agent may likewise be dissolved in water or a suitable

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organic solvent (e.g. alcohol) and be supplied in dissolved form.
In order to achieve the uniform precipitation of silver-containing precipitate onto the
carbon particles, the silver compound and the reducing agent are appropriately added
continuously over the course of the reduction, simultaneously but with separate supply
and in stoichiometrically equivalent amounts. Intensive mixing is likewise
advantageous during the reduction. The supply is effected advantageously below the
liquid surface.
The proportions of silver compound and carbon particles are guided by the end use of
the material and can be selected suitably by the person skilled in the art.
Advantageously, the material contains from 0.5 to 12% by weight, preferably from 1 to
12% by weight, more preferably from 2 to 10% by weight, even more preferably from 2
to 8% by weight, of carbon. The material may contain further components or impurities
in an amount of up to 1% by weight. The remaining fractions in the material are silver.
The process according to the invention allows the preparation of materials based on
silver-carbon. It is possible by the process according to the invention to achieve more
homogeneous distribution of the carbon particles than in customary powder metallurgy
mixing processes. This is particularly advantageous in the case of fibrous or very fine
particles which are difficult to mix. In addition, a higher ductility is achieved, such that
processibility is facilitated, for example in the extrusion and in the subsequent shaping.
A further advantage is that higher fill levels can be achieved with the process according
to the invention compared to processes which are based on mixing by powder
metallurgy means. Consequently, a saving of the noble metal silver is possible.
Moreover, a better switching response in circuit breakers is observed, compared to
materials which are produced by means of mixing by powder metallurgy means.
The carbon particles coated with the silver-containing precipitate can subsequently be
separated from the solvent, optionally dried and then processed further. Although
individual sintering is possible, it is not preferred for economic reasons. In a preferred
embodiment, the coated carbon particles, under cold isostatic conditions, are pressed,
sintered and extruded. However, it is possible to employ any other known processes for
further processing.
Typical conditions for the cold isostatic pressing are from 60 to 90 MPa. The sintering
is typically performed at from 800 to 900°C under protective gas such as N2/H2 (50:50).
Subsequently, extrusion is performed. To this end, bolts are preheated, for example, to

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from 750 to 850°C before the pressing by means of induction heating, and then
introducing directly into the preheated recipients (for example from 400 to 500°C) and
pressed out in the defined form through the selected die.
The materials produced by the process according to the invention are notable for a
particularly homogeneous and dispersed distribution. In addition, they surprisingly have
excellent welding resistance with equal or possibly better arc erosion resistance and
good processing performance even at relatively high carbon contents.
The resulting materials based on silver-carbon can be used in all fields of use in which
materials based on silver-carbon have been used to date. However, they are particularly
suitable for circuit breakers in low-voltage power engineering.
EXAMPLES
The examples which follow are intended to illustrate the invention. However, they
should not be regarded as a restriction. Instead, the scope of protection is determined by
the claims.
The following abbreviations are used:
IS individual sintring
WCP wet-chemical precipitation
EX extrusion
Example 1
Material A is produced as a comparison by means of extrusion.
19 kg of silver spray powder having a particle diameter of less than 63 µm were mixed
in dry form with 1 kg of graphite powder (d50 4.4 µm). The mixture was subsequently
pressed to bolts under cold isostatic conditions with a pressure of 60 MPa, sintered
under H2/N2 (50:50) protective gas and, after inductive preheating of the bolt to 780°C,
extruded. The switch samples were machined from the extruded wires such that the
switch surface was at right angles to the direction of extrusion. The graphite particle
agglomerates pulled apart in fibrous form by the extrusion were thus at right angles to
the switch surface. In the case of agglomerates, the mean diameter is based essentially
on the mean diameter of the particles of which the agglomerates are composed. To
obtain a solderable and weldable layer, the particles were fired under air at 520°C for

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approx. 15min and then sawn through, such that an unfired switch surface was
available.
Example 2
The inventive materials B, C, D, E and I were produced by chemical reductive
precipitation and extrusion.
Material B
To produce a 1.5 kg batch of a composite powder with a 5% by weight carbon content,
2244 g of silver nitrate, 75 g of graphite particles (d50 = 4.4 µm) and 1186.6 g of
ascorbic acid were used. The graphite particles were suspended in distilled water with
the aid of a disperser and then transferred to a reaction vessel. The silver nitrate was
made up as a 3.5 molar solution and the ascorbic acid as a 1.7 molar solution. By means
of simultaneous and equal addition of stoichiometric amounts through two separate
feeds as shown schematically in figure 1, and with simultaneous intensive mixing by
means of a high-energy stirring system, metallic silver was precipitated onto the
graphite particles at a constant rate of approx. 130 g/min. The coated graphite particles
thus produced were separated from the liquid by means of a suction filter, washed, dried
and prescreened to 250 µm. The further processing was effected as in example 1 by
means of extrusion.
The sampling of the switch samples was again also effected such that the switch surface
was at right angles to the direction of extrusion. Owing to the actually individually
embedded particles, though, the structure here was so homogeneous that fibrous
alignment of the graphite particles was virtually indiscernible.
Materials C, D and E
Materials C, D and E were produced like material B, with the difference that other
carbon contents or carbon types were used. Material C contained 6% by weight of
graphite particles, material D contained 4% by weight of graphite particles and 2% by
weight of carbon fibers, and material E contained 7% by weight of graphite particles.
Material I
Material I was produced like material B, with the difference that the switch surface was
aligned parallel to the direction of extrusion in the sampling of the switch samples.

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Example 3
Material F was produced by means of individual sintering as a comparison.
2 kg of silver spray powder having a particle diameter of less than 63 µm were mixed in
dry form with 100 g of graphite powder (d50 = 4.4 µm). The mixture was subsequently
sintered individually. To this end, the powder mixture was filled into corresponding
press molds, pressed (approx. 200 MPa) and sintered under a protective gas atmosphere
(sintering temperature: 880°C; t = 3 h, atmosphere: 80/20 N2/H2; then calibration
pressing at approx. 800 MPa). To obtain a solderable and weldable layer, a pure silver
layer of approx. 10% of the total amount of sample was first introduced here into the
press mold. Subsequently, the powder mixture was added.
Example 4
The inventive materials G and H were produced by chemical reductive precipitation and
individual sintering.
Material G
To produce a 1.5 kg batch of a composite powder with a 5% by weight carbon content,
2244 g of silver nitrate, 75 g of graphite particles (d50 = 4.4 µm) and 1186.6 g of
ascorbic acid were used. The graphite particles were suspended in distilled water with
the aid of a disperser and then transferred to a reaction vessel. The silver nitrate was
made up as a 3.5 molar solution and the ascorbic acid as a 1.7 molar solution. By means
of simultaneous and equal addition of stoichiometric amounts through two separate
feeds as shown schematically in figure 1 and with simultaneous intensive mixing by
means of a high-energy stirring system, metallic silver was deposited onto the graphite
particles at a constant rate of approx. 130g/min. The coated graphite particles thus
produced were separated from the liquid by means of a suction filter, washed, dried and
prescreened to 250 µm. The further processing was effected as in example 3 by means
of individual sintering technology.
Material H
Material H was produced like material G, with the difference that 6% by weight of
graphite particles were used.

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Test methods
Determination of the mean particle diameter
The diameter of the spheres is defined as the particle diameter in the case of essentially
spherical particles. In the case of nonspherical particles, the shortest diameter is defined
as the particle diameter. For example, in the case of fibrous particles, the diameter of the
fibers is defined as the particle diameter. To determine the mean particle diameter, the
particle diameter of at least 25 particles is determined, for example, by means of
microscopy. Subsequently, the mean is calculated.
Switching response
The switching response of the materials was studied both in a switch-on model switch
and in a switch-off model switch.
The switch-on model switch and switch-off model switch corresponded to the test
apparatus described in "Uber den Einfluss des Herstellverfahrens auf das
Schaltverhalten von Kontaktwerkstoffen der Energietechnik" [The influence of the
production process on the switching response of contact materials in power
transmission], Poniatowski, Schroder, Schulz; 7th Int. conference on electrical contacts.
Paris 1974.
Welding force
To measure the welding force in the switching-on operation, the apparatus was
equipped with a pressure measurement cell which enabled the force to be measured
(referred to as the welding force) which has to be applied in the currentless separation of
a weld.
Specific arc erosion
The specific arc erosion is determined in each case by weighing, by measuring the mass
loss of the contact pieces after a particular number of switching operations and dividing
it by the electric arc energy likewise determined.
Specific switching conditions
Switch-on test: Test current = 700 A, 230 V, alternating current
300 switching operations

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Measurement of the welding force by means of a pressure measurement cell,
specification of the 95% value, i.e. 95% of the welding forces measured are below the
value specified
Alignment of the elongated carbon particles always at right angles to the direction of
extrusion and hence to the switch surface; only material I was aligned in parallel.
In the case of individually sintered material, the switch surface is always at right angles
to the direction of uniaxial pressing.
Switch-off test: Test current = 1300A; 230V, alternating current, magnetic
blowout field 30 mT/kA
150 switching operations
Alignment of the elongated carbon particles always at right angles to the direction of
extrusion and hence to the switch surface; only material I was aligned in parallel.
In the case of individually sintered material, the switch surface is always at right angles
to the direction of uniaxial pressing.
Example 5
In this example, the welding behavior of the materials produced by extrusion or
individual sintering was tested in the switch-on model switch.

Material Welding force
[N]
A1 (5% graphite, comparison, EX) 4.4
A2 (5% graphite, comparison, EX) 5.0
B1 (5% graphite, WCP EX) 1.8
B2 (5% graphite, WCP EX) 2.2
C1 (6% graphite, WCP EX) 0.7
C2 (6% graphite, WCP EX) 1.1
D1 (4% graphite + 2% fiber, WCP EX) 2.9
D2 (4% graphite + 2% fiber, WCP EX) 3.2
E1 (7% graphite, WCP EX) 0.4

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Table 1: Welding force in the switch-on model switch, sample production by
extrusion
In the case of equal graphite contents, about a halving of the welding force compared to
comparative material A1 and A2 is observed (compare samples A1 and A2 with
samples B1 and B2). The process according to the invention additionally enables higher
graphite contents than 5% also to be established, since the homogeneous embedding of
the carbon particles into the silver matrix still allows sufficiently good processing
properties to be realized. In the case of comparative material A1 and A2 in contrast,
generally no graphite contents significantly higher than approx. 5% should be used,
since the processing complexity which is then higher cannot be justified by
correspondingly better switch properties.
In contrast, the inventive materials can also be processed efficiently with graphite
contents of 6 and 7% by weight. When the graphite content is increased, the welding
force falls further once again, but the arc erosion surprisingly remains at about the same
level, while the technical literature reports an increase in arc erosion with rising carbon
content (see Vinaricky; see table 1). The process according to the invention also allows
a portion of the graphite to be replaced by carbon fibers. The welding forces are
lowered somewhat compared to the comparative material, without the arc erosion rising
in the case of elevated carbon content (cf. table 1 & table 3). It is therefore possible here
too to establish higher carbon contents and hence to save silver. It is also of particular
interest that an inventive material provides positive switching results when the switch
surface is aligned parallel to the direction of extrusion. In the technical literature
(Vinaricky, page 252), in the case of such an alignment, about a doubling in arc erosion
is observed compared to alignment at right angles. Such a material has the great
advantage that switch pieces can be produced with significantly higher yield from the
extrudate owing to the different alignment than when the switch pieces have to be
produced with alignment at right angles to the direction of extrusion. This is
economically advantageous.

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Table 2: Welding force in the switch-on model switch, sample production by means
of individual sintering
In the case of individually sintered materials, the welding forces are generally very low,
such that no significant differences are noticeable here. The advantages of the process
according to the invention lie here in the comparatively better arc erosion behavior (see
table 4).
Example 6
In this example, the arc erosion behavior of the materials produced by extrusion or
individual sintering was tested in the switch-on model switch.

Table 3: Specific arc erosion in the switch-on model switch; sample production via
extrusion

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The arc erosion resistance is no better than for the comparative material at the same
carbon content, but this arc erosion resistance is maintained even at higher carbon
contents, while it has been reported in the prior art that it otherwise generally decreases
with rising carbon content (see Vinaricky). In other words, it is possible to utilize the
better welding resistance of the materials with higher carbon contents without the arc
erosion behavior becoming significantly poorer as a result. There is an additional
economic advantage through saving of silver. As a further positive aspect, the still good
processibility should be mentioned, even in the case of material I with parallel
alignment.

Table 4: Specific arc erosion in the switch-on model switch; sample production via
individual sintering
The individually sintered material exhibits generally poorer arc erosion behavior than
the extruded material. However, the values in table 4 show that the worsening in this
property in the inventive materials does not assume such serious proportions as in the
comparative material.
Example 7
In this example, the arc erosion behavior in the switch-on model switch is tested.


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Table 5: Specific arc erosion in the switch-off model switch; sample production via
extrusion
In the switch-off model switch, a comparable picture is found to that in the case of the
switch-on model switch. Here too, the arc erosion resistance is maintained up to higher
carbon contents or even improves somewhat (see table 5).

Table 6: Specific arc erosion in the switch-off model switch; sample production via
individual sintering
The results of the individually sintered samples in the switch-off tests correspond again
to the trends in the switch-on tests. The inventive material is better than the comparative
material. This advantage is maintained even at 6% by weight of carbon.

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CLAIMS
1. A process for producing a material based on silver-carbon, comprising the steps
of:
(i) providing a suspension of carbon particles; and
(ii) supplying a solution of a silver compound and of a reducing agent, such that
a silver-containing precipitate is deposited onto the carbon particles,
where the carbon particles have a mean diameter of 200 nm or greater.
2. The process as claimed in claim 1, wherein the solution of the silver compound
and the reducing agent are added continuously over the course of the reaction with
mixing, with simultaneous but separate supply and in stoichiometrically
equivalent amounts.
3. The process as claimed in claim 1 or 2, wherein the silver compound is a silver
salt which is selected from the group of silver nitrate, silver acetate, silver
carbonate, silver citrate and silver oxalate.
4. The process as claimed in one of claims 1 to 3, wherein the reducing agent is
selected from the group of ascorbic acid, citric acid, oxalic acid, formic acid and
hydroxylamine.
5. Process according to one of claims 1 to 4, wherein the carbon particles arc
selected from graphite powder, carbon fibers and carbon black, and combinations
thereof.
6. The process as claimed in claim 5, wherein the carbon particles are a mixture of
graphite powder and/or carbon black: carbon fibers in a ratio of from 20:1 to 1:20.
7. The process as claimed in claim 5 or 6, wherein the carbon particles are from
100% by weight to 98% by weight of graphite powder and from 0% by weight to
2% by weight of carbon black (based on the total weight of graphite powder and
carbon black) in combination with carbon fibers.
8. The process as claimed in claim 5, wherein the carbon particles are carbon fibers.
9. The process as claimed in claim 8, wherein the carbon fibers have a diameter of"

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17
from 0.5 µm to 30 µm and the length is at least twice as great as the diameter.
10. The process as claimed in one of claims 1 to 9, wherein the mean particle
diameter of the carbon particles is from 0.2 µm to 15 urn
11. The process as claimed in one of claims 1 to 10, wherein the proportions of silver
compound, carbon particles and further components are selected such that from
0.5 to 10% by weight of carbon, from 0 to 1% by weight of further components,
remainder silver are present in the material.
12. The process as claimed in one of claims 1 to 11, wherein the coated carbon
particles obtained in step (ii), under cold isostatic conditions, are pressed, sintered
and extruded.
13. The process as claimed in one of claims 1 to 11, wherein the coated carbon
particles obtained in step (ii) are processed to give the material by individual
sintering.
14. A material obtainable by a process as claimed in one of claims 1 to 13.
15. The material as claimed in claim 14, which is a contact material.
16. The material as claimed in claim 14 or 15, which consists of from 0.5 to 10% by
weight of carbon, from 0 to 1% by weight of further components, remainder
silver.
17. The material as claimed in claim 16, which contains from 2 to 8% by weight of
carbon.
18. The use of the material as claimed in one of claims 14 to 17 in circuit breakers for
low-voltage power engineering.

The invention relates to a process for producing a material based on silver-carbon,
comprising the steps of:
(i) providing a suspension of carbon particles; and
(ii) supplying a solution of a silver compound and of a reducing agent, such that a
silver-containing precipitate is deposited onto the carbon particles,
where the carbon particles have a mean diameter of 200 nm or greater.
The invention further relates to a material obtainable by this process and to the use of
the material in circuit breakers for low-voltage power engineering.

Documents:

00610-kolnp-2008-abstract.pdf

00610-kolnp-2008-claims.pdf

00610-kolnp-2008-correspondence others.pdf

00610-kolnp-2008-description complete.pdf

00610-kolnp-2008-drawings.pdf

00610-kolnp-2008-form 1.pdf

00610-kolnp-2008-form 2.pdf

00610-kolnp-2008-form 3.pdf

00610-kolnp-2008-form 5.pdf

00610-kolnp-2008-international publication.pdf

00610-kolnp-2008-international search report.pdf

00610-kolnp-2008-pct request form.pdf

610-KOLNP-2008-(10-09-2013)-ABSTRACT.pdf

610-KOLNP-2008-(10-09-2013)-ANNEXURE TO FORM 3.pdf

610-KOLNP-2008-(10-09-2013)-CLAIMS.pdf

610-KOLNP-2008-(10-09-2013)-CORRESPONDENCE.pdf

610-KOLNP-2008-(10-09-2013)-OTHERS.pdf

610-KOLNP-2008-(10-09-2013)-PETITION UNDER RULE 137.pdf

610-KOLNP-2008-CORRESPONDENCE 1.1.pdf

610-KOLNP-2008-CORRESPONDENCE OTHERS 1.1.pdf

610-KOLNP-2008-CORRESPONDENCE OTHERS 1.2.pdf

610-KOLNP-2008-CORRESPONDENCE.pdf

610-KOLNP-2008-EXAMINATION REPORT.pdf

610-KOLNP-2008-FORM 18-1.1.pdf

610-kolnp-2008-form 18.pdf

610-KOLNP-2008-FORM 26.pdf

610-KOLNP-2008-GRANTED-ABSTRACT.pdf

610-KOLNP-2008-GRANTED-CLAIMS.pdf

610-KOLNP-2008-GRANTED-DESCRIPTION (COMPLETE).pdf

610-KOLNP-2008-GRANTED-DRAWINGS.pdf

610-KOLNP-2008-GRANTED-FORM 1.pdf

610-KOLNP-2008-GRANTED-FORM 2.pdf

610-KOLNP-2008-GRANTED-FORM 3.pdf

610-KOLNP-2008-GRANTED-FORM 5.pdf

610-KOLNP-2008-GRANTED-SPECIFICATION-COMPLETE.pdf

610-KOLNP-2008-INTERNATIONAL EXM REPORT.pdf

610-KOLNP-2008-INTERNATIONAL PUBLICATION.pdf

610-KOLNP-2008-INTERNATIONAL SEARCH REPORT & OTHERS.pdf

610-KOLNP-2008-INTERNATIONAL SEARCH REPORT 1.1.pdf

610-KOLNP-2008-OTHERS-1.1.pdf

610-KOLNP-2008-OTHERS.pdf

610-KOLNP-2008-PA.pdf

610-KOLNP-2008-PCT REQUEST FORM 1.1.pdf

610-KOLNP-2008-PETITION UNDER RULE 137.pdf

610-KOLNP-2008-REPLY TO EXAMINATION REPORT.pdf

610-KOLNP-2008-TRANSLATED COPY OF PRIORITY DOCUMENT-1.1.pdf

610-KOLNP-2008-TRANSLATED COPY OF PRIORITY DOCUMENT.pdf

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Patent Number 258724
Indian Patent Application Number 610/KOLNP/2008
PG Journal Number 06/2014
Publication Date 07-Feb-2014
Grant Date 03-Feb-2014
Date of Filing 12-Feb-2008
Name of Patentee UMICORE AG & CO. KG,
Applicant Address RODENBACHER CHAUSSEE 4, 63457 HANAU-WOLFGANG
Inventors:
# Inventor's Name Inventor's Address
1 KEMPF, BERND RIEMENSCHNEIDERSTRASSE 38 63839 KLEINWALLSTADT
2 BOEHME, CARSTEN IN DEN BAUMSTUECKEN 10, 63791 KARBEN
3 ROTH, WERNER HANAUER LANDSTR. 19 63594 HASSELROTH
4 KOFFLER, ANDREAS SAAL-BURGSTR. 63, 61130 NIEDERAU
5 WOLMER, ROGER ALTE LANGGASSE 16, 63457 HANAU GROSSAUHEIM
PCT International Classification Number H01H 1/027
PCT International Application Number PCT/EP2006/007915
PCT International Filing date 2006-08-10
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 102005038233.9 2005-08-12 Germany