U.S. patent number 3,926,832 [Application Number 05/383,677] was granted by the patent office on 1975-12-16 for gettering structure.
This patent grant is currently assigned to S.A.E.S. Getters S.p.A.. Invention is credited to Aldo Barosi.
United States Patent |
3,926,832 |
Barosi |
December 16, 1975 |
**Please see images for:
( Certificate of Correction ) ( Reexamination Certificate
) ** |
Gettering structure
Abstract
A non-evaporating getter device and composition and process for
producing such which is optionally heatable employing a getter
material comprising at least one non-evaporable getter metal
preferably selected from the group consisting of Zr, Ta, Hf, Nb,
Ti, Th and U in intimate mixture with a zirconium-aluminum
alloy.
Inventors: |
Barosi; Aldo (Milan,
IT) |
Assignee: |
S.A.E.S. Getters S.p.A. (Milan,
IT)
|
Family
ID: |
11222826 |
Appl.
No.: |
05/383,677 |
Filed: |
July 30, 1973 |
Foreign Application Priority Data
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|
|
|
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Aug 10, 1972 [IT] |
|
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28053/72 |
|
Current U.S.
Class: |
252/181.6;
148/105; 419/2; 75/246; 378/123 |
Current CPC
Class: |
H05B
3/00 (20130101); H01K 1/56 (20130101); H01J
7/18 (20130101) |
Current International
Class: |
H01J
7/00 (20060101); H01J 7/00 (20060101); H01K
1/00 (20060101); H01K 1/00 (20060101); H01J
7/18 (20060101); H01J 7/18 (20060101); H01K
1/56 (20060101); H01K 1/56 (20060101); H05B
3/00 (20060101); H05B 3/00 (20060101); H01j
007/18 (); H01j 035/20 (); H01j 001/50 () |
Field of
Search: |
;252/181.1,181.6,464,517,518,520 ;75/.5BB,177 ;29/182,191.2 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
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|
|
|
|
|
404,129 |
|
1965 |
|
JA |
|
1,302,951 |
|
1971 |
|
DT |
|
1,011,259 |
|
1965 |
|
UK |
|
Primary Examiner: Cooper; Jack
Assistant Examiner: Wheelock; Eugene T.
Attorney, Agent or Firm: Littlepage, Quaintance, Murphy
& Dobyns
Claims
What is claimed is:
1. A gettering structure comprising:
A. a sintered particulate non-evaporable getter metal selected from
the group consisting of Zr, Ta, Hf, Nb, Ti, Th and U,
B. a particulate zirconium-aluminum alloy comprising 5 to 30 weight
percent aluminum balance zirconium wherein the particles of the
zirconium-aluminum alloy are larger than the particles of the
non-evaporable getter metal and are distributed throughout the
non-evaporable getter metal wherein the weight ration A:B is from
19:1 to 2:3 and wherein said particles of zirconium-aluminum alloy
are generally spaced out of contact with each other.
2. A gettering structure comprising:
A. a sintered particulate non-evaporable getter metal, selected
from the group consisting of Zr, Ta, Hf, Nb, Ti, Th and U,
B. a particulate zirconium-aluminum alloy comprising 5 to 30 weight
percent aluminum balance zirconium wherein the particles of
zirconium-aluminum alloy are larger than the particles of the
non-evaporable getter metal and are distributed throughout the
non-evaporable getter metal, wherein the sintered non-evaporable
getter metal has a surface area after sintering substantially equal
to its surface area prior to sintering wherein the weight ratio A:B
is from 19:1 to 2:3 and wherein said particles of
zirconium-aluminum alloy are generally spaced out of contact with
each other.
3. A gettering structure comprising:
A. particulate zirconium, the particles of which pass through a
U.S. standard screen of 200 mesh per inch,
B. a particulate alloy of 84 weight percent zirconium and 16 weight
percent aluminum, the particles of which pass through a U.S.
standard screen of 60 mesh per inch and are retained on a U.S.
standard screen of 100 mesh per inch
with the provisos that:
1. the composition is sintered,
2. the composition exhibits a compressive strength of at least 300
kg/cm.sup.2,
3. the total surface area of the zirconium particles after
sintering is equal to at least 95% of their surface area before
sintering;
4. the particles of zirconium are in contact with one another,
5. the particles of the alloy are distributed evenly throughout the
particles of zirconium,
6. the particles of the alloy are generally spaced out of contact
with one another,
7. the weight ratio of A:B is 10:1 to 1:1.
4. A gettering structure comprising:
A. sintered particulate zirconium,
B. a particulate zirconium-aluminum alloy comprising 5 to 30 weight
percent aluminum balance zirconium wherein the particles of the
zirconium-aluminum alloy are larger than the particles of zirconium
and are distributed throughout the particles of zirconium in an
amount such that the particles of zirconium-aluminum alloy are
generally spaced out of contact with each other.
5. A gettering structure comprising:
A. sintered particulate zirconium,
B. a particulate zirconium-aluminum alloy comprising 5 to 30 weight
percent aluminum, balance zirconium wherein the particles of the
zirconium-aluminum alloy are larger than the particles of zirconium
and are distributed throughout the particles of zirconium wherein
the weight ratio A:B is from 19:1 to 2:3 and wherein said particles
of zirconium-aluminum alloy are generally spaced out of contact
with each other.
Description
BACKGROUND OF THE INVENTION
The invention is directed to a getter device and composition for
electrical discharge, vacuum and rare gas filled vessels employing
a non-evaporable getter metal which preferably contains at least
one metal selected from a group consisting of Zr, Ta, Hf, Nb, Ti,
Th and U which is optionally heatable during operation of the
vessel. In the past, such getter devices were constructed in the
form of an open metal cup or pot-shaped vessel which was associated
with an insulated heating coil of the type of an indirectly heated
cathode with such metal vessel consisting of the getter metal or at
least provided with a surface coating of such metal.
Getter devices employing zirconium, particularly correspondingly
thick layers thereof produced by pressing and sintering of
zirconium powder provide a considerably increased gas sorption
speed and gas sorption capacity at temperatures above 600.degree.C,
but at intermediate and lower temperatures the gas sorption
capacity is considerably limited by the fact that the gas diffusion
into the interior of the zirconium is reduced whereby the gettering
action is mainly due to the slight surface sorption of the
zirconium. However, an increase of the gas sorption capacity of the
getter at room temperature is absolutely necessary to ensure
maintenance of the necessary vacuum or rare gas atmosphere of
electronic tubes and other vessels under storage conditions.
An increase of the gas sorption capacity at room temperature can be
achieved with a porous unpressed zirconium body, and in an effort
to achieve greater porosity in sintered bodies of zirconium powder
for getter purposes, molybdenum or tungsten powder was admixed with
the zirconium powder. This arrangement, however, has the
disadvantage, among others, that zirconium and molybdenum form an
alloy at 1500.degree.C (2732.degree.F), as a result of which the
sintering and degasification temperatures of such operating
electrodes is considerably limited at the upper end.
Perdijk et al. in U.S. Pat. No. 2,855,368 suggest the addition of
various powdered materials which react in a chemical or physical
way with the powdered zirconium such as to reduce the temperature
at which the activation of the zirconium takes place, thus reducing
the probability of complete sintering. Among these additions are
suggested aluminum, silicon, beryllium, tungsten, cerium and
lanthanum. However, such reactions are not well controlled and a
product of uncertain characteristics is obtained. In fact, in the
same reference it is suggested to add a refractory metal powder
such as tungsten to reduce the sintering of zirconium. TiAl.sub.3
is also suggested as an antisintering agent.
Non-metallic antisintering agents have also been suggested such as
by Wooten in U.S. Pat. No. 2,368,060 who adds powdered silica. In a
further attempt to overcome the problems of sintering of the Zr
powder non-evaporating getters Wintzer in U.S. Pat. No. 3,584,253
proposes the use of powdered graphite as an antisintering agent to
maintain the large surface area of the active gas sorbing material.
It shall be understood that these so-called "antisintering agents"
do not prevent sintering, which is desirable in the present
invention, but only retard sintering to a degree to make it more
readily controllable.
Even though the introduction of poisonous gases into the electronic
tube or other device by graphite is much reduced when compared with
a similar gas transfer by the previously suggested metallic
additions of molybdenum or tungsten powder, it must be realized
that graphite can still introduce undesirable gases into the tube.
Other antisintering agents such as refractory metallic oxides or
other oxides such as silica are also known to introduce
considerable amounts of poisonous gases into electronic tubes.
Furthermore, the additional antisintering materials proposed
perform no other function apart from that of mechanically
distancing the getter particles in such a way that sintering is
reduced to a minimum. They also uselessly occupy space artifically
increasing the volume of the getter composition.
Accordingly, it is an object of the present invention to provide an
improved getter device and composition which is substantially free
from one or more disadvantages of the prior art.
A further object is to provide a getter composition having at least
equal gettering properties compared with traditional getter
composition at room temperature and improved gettering properties
at higher temperatures.
A further object is to provide a getter device having a means for
preventing excessive sintering of the particulate powdered getter
metal, said means itself performing a gettering function.
Additional objects and advantages of the present invention will be
apparent by reference to the following detailed description thereof
and drawings wherein:
FIG. 1 is a top view of a getter device of the present
invention;
FIG. 2 is a sectional view taken along line 2--2 of FIG. 1;
FIG. 3 is a top view of a modified getter device of the present
invention, and
FIG. 4 is a sectional view taken along line 4--4 of FIG. 3;
FIGS. 5 and 6 are further getter devices;
FIG. 7 is yet another modification of a getter device;
FIGS. 8 and 9 are log-log graphs showing the sorption properties of
getters of the present invention and corresponding properties for
prior art getter compositions;
FIG. 10 is a schematic representation of a sectional view of the
getter composition of the present invention magnified approximately
110 times;
FIG. 11 is an enlarged sectional view of the indicated portion of
FIG. 10, the diameter of FIG. 11 being approximately 40
microns.
According to the present invention there is provided a getter
device comprising a holder which contains or supports a
non-evaporable getter metal wherein said getter metal preferably
comprises at least one metal selected from the group consisting of
Zr, Ta, Hf, Nb, Ti, Th and U in intimate mixture with a
zirconium-aluminum alloy. These zirconium-aluminum alloys are
themselves non-evaporable getter materials and are characterized by
(1) a sorptive capacity for noxious gases such as oxygen, carbon
monoxide and water vapor, and (2) a vapor pressure at 1000.degree.C
of less than 10.sup.-.sup.5 torr. The preferred zirconium-aluminum
alloys comprise from 5 to 30 and preferably 13 to 18 weight percent
aluminum, balance zirconium. The most preferred Zr alloy is one of
16 percent aluminum, balance zirconium, available from SAES Getters
S.p.A., Milan, Italy, under the trademark St 101. The present
invention proceeds upon the concept of utilizing the Zr-Al alloy in
conjunction with the non-evaporable getter metal in which the
complete sintering of the particles of the getter metal is avoided
during the heat treatment by employing Zr-Al alloy particles which
are for example utilized by mixing Zr-Al alloy powder with the
first getter material powder and applying the mixture to a support
means. By the addition of Zr-Al alloy granules, for example,
pressed layers with a higher porosity can be achieved than with
ductile molybdenum or tungsten, and at the same time the poisonous
gas transfer is lower than that of graphite. Getter devices of the
present invention can be utilized with particular advantage in
applications where a definite lack of space exists. In accordance
with one method of the invention for producing getter devices of
the type described, a heating means, already provided with a
sinteredon insulation layer, is suitably coated with a mixture of
powdered getter metal and powdered 16% weight Al-Zr alloy and
subsequently heat treated in high vacuum at
800.degree.-1200.degree.C. The powder mixture may be in the form of
an alcoholic suspension and applied by a dipping operation or the
dry powder mixture may be pressed within a pressing die, at low
pressure, and the molded material subsequently subjected to the
desired heat treatment. Alternatively, the mixed getter powder may
be supported as a layer of particles on at least one side of a
supporting metal strip by a process as described by della Porta et
al. in U.S. Pat. No. 3,652,317 or U.S. patent application Ser. No.
249,772 filed May 3, 1972. The powder may also pressed directly
into a ring shaped holder well known in the art or may be painted,
in the form of a liquid suspension, directly onto a suitable
surface such as an electron tube electrode.
The getter devices and compositions produced according to the
teachings of the present invention show a higher gas sorption speed
and capacity at superambient temperatures compared to traditional
getter devices and compositions using a graphite antisintering
agent, in spite of the fact that the preferred Zr-Al alloy of 16%
weight Al, balance zirconium, alloy is well known to sinter at the
heat treatment temperatures of the present invention. This
sintering is well described by della Porta in U.S. Pat. No.
3,203,901. The non-evaporable getter materials are characterized by
(1) a sorptive capacity for noxious gases such as oxygen, carbon
monoxide, and water vapor, (2) a vapor pressure at 1000.degree.C of
less than 10.sup.-.sup.5 torr. Examples of suitable non-evaporable
getter materials include among others Zr, Ta, Hf, Nb, Ti, Th and U,
mixtures thereof, alloys thereof with one another and with other
metals, which alloys have satisfactory gettering properties. The
preferred non-evaporable getter material is zirconium.
The non-evaporable getter metal and the Zr-Al alloy are preferably
employed as finely divided particulate solids in intimate mixture
one with the other. The weight ratio of the non-evaporable getter
metal to the Zr-Al alloy is generally between 19:1 and 2:3 and
preferably between 10:1 and 1:1. At higher ratios the Zr-Al alloy
is not present in sufficient quantity to prevent excessive
sintering of the non-evaporable getter metal. At lower ratios the
getter metal is not present in sufficient quantity to perform its
desired gas sorbing function especially at low temperatures. Both
the Zr-Al alloy and the non-evaporable getter metal can be employed
as particles of widely varying sizes. However, the non-evaporable
getter metal is generally employed in particle sizes which pass
through a screen of 100 mesh per inch and preferably those which
pass through a screen of 200 mesh per inch. The Zr-Al alloy is
generally employed in particle sizes which pass through a screen of
32 mesh per inch and preferably those which pass through a screen
of 60 mesh per inch, and are retained on a screen of 100 mesh per
inch.
The holder can be in any physical shape which will carry the getter
composition. In one embodiment, the holder is an annular ring
similar to the one commonly employed to hold vaporable getter
metals such as barium. In another embodiment, the holder is a
substrate which is preferably metallic and which has the
particulate composition embedded in at least one of its
surfaces.
The same substrate may be used as a support for other materials
which might be useful within the tube such as mercury releasing
materials.
In a further embodiment, the holder is in the form of a wire or rod
around which is formed a pill or pellet of the getter
composition.
The present invention is applicable to a wide variety of electron
tubes, examples of which include, among other, radio receiving and
transmitting tubes, X-ray tubes, television and radar kinescopes,
klystrons, travelling wave tubes, mercury discharge tubes including
fluorescent lamps. It is also applicable in rare gas purifiers,
hydrogen purifiers, and in vacuum pumps.
Referring now to the drawings and in particular to FIGS. 1 and 2,
there is shown a device 10 of the present invention. In the getter
device 10 the holder is in the form of an annular ring 11 having a
cavity 12, and a non-evaporable getter composition 13 within the
cavity 12.
Referring to FIGS. 3 and 4, there is shown a getter device 30 which
is connected to a similar getter device 30' which in turn is
connected to yet another similar getter device 30". The getter
devices 30, 30', 30", etc., form a continuous running length of
devices. In the device 30, the holder is in the form of a substrate
31 having the getter composition 32 in particulate form partially
embedded in the upper and lower planar surfaces of the substrate
31. In operation, the getter device 30', for example, is separated
from the devices 30 and 30" by severing the substrate 31 in the
vicinity of the small bridging attachments 33, 34, 35, and 36.
FIG. 5 shows a getter device 50 in the form of a pellet in which
the holder is in the form of a rod 51 having the getter composition
52 compressed around and supported by said rod.
FIG. 6 shows a non-evaporating getter device 60 in the form of a
pellet in which the holder 61 is an insulated wire of high ohmic
resistance in the form of a heating coil 62 around which is formed
the getter composition 63.
FIG. 7 shows a non-evaporating getter device 70 wherein the holder
consists of a wire spiral heatable by an electrical current and
covered with an electrically insulating coating 72. A covering of
getter material 73 is applied by a method already described or by
other methods well known in the art.
Referring now to FIG. 10, there is shown a getter composition 80 of
the present invention. The composition 80 comprises particles 81,
81' of a sintered particulate non-evaporable getter metal. The
composition also comprises particles 82, 82' of a
zirconium-aluminum alloy. As can be seen by reference to FIG. 10,
the particles 82, 82' of the Zr-Al alloy are larger than the
particles 81, 81' of the getter metal. It can also be seen than the
particles 82, 82' of the Zr-Al alloy are distributed throughout the
particles of the getter metals 81, 81'. Furthermore, the particles
of the Zr-Al alloy 82, 82' are generally spaced out of contact with
one another.
Referring now to FIG. 11, there is shown an enlarged view of a
portion of the particles 81, 81' of FIG. 10. As shown in FIG. 11,
particles 83, 83' corresponding to particles 81, 81' are in contact
with one another and are sintered to one another. In accordance
with the present invention, the particles 83, 83' have a surface
area after sintering which is substantially equal to and generally
is at least 95% their surface area before sintering. Surface area
measurements are made by the B.E.T. technique. See Volume LX of The
Journal of the American Chemical Society, Feb. 1938, p. 309-319.
See also Methods for the Determination of Specific Surface of
Powders, Part I Nitrogen Adsorption (B.E.T. method) British
Standards Institution (BS 4359:Part 1:1969). On the other hand, the
sintering is conducted long enough in order to provide the
composition with a compressive strength of at least 50 and
preferably at least 300 kg/cm.sup.2.
The invention is further illustrated by the following examples in
which all parts and percentages are by weight unless otherwise
indicated. These non-limiting examples are illustrative of certain
embodiments designed to teach those skilled in the art how to
practice the invention and to represent the best mode contemplated
for carrying out the invention.
EXAMPLE 1
The tests of this example were performed to show the behavior of a
prior art getter device. Particulate zirconium was mixed with
particulate graphite as taught by Wintzer in U.S. Pat. No.
3,584,253 and then made into a fairly fluid paste in the form of an
alcoholic suspension. A quantity of paste containing 100 mg of the
powder mixture was placed in a ring holder to form a getter device
10 as illustrated in FIGS. 1 and 2.
The getter device 10 was then placed in a vacuum of about
10.sup.-.sup.5 to 10.sup.-.sup.6 torr. The temperature was
increased from room temperature to between 900.degree. and
1100.degree.C during a period of 25 minutes. The temperature
between 900.degree. and 1100.degree.C was maintained for a further
5 minutes. The treated getter device was allowed to cool to room
temperature and then removed from the vacuum furnace.
The getter ring 11 was attached to a thermocouple support and then
mounted in a vacuum system, of design well known in the art and
capable of reaching pressures less than 10.sup.-.sup.8 torr, to
measure the gettering characteristics of the device. The whole
system was then degassed by overnight heating of 350.degree.C. When
the pressure in the system was of the order of 10.sup.-.sup.8 torr
the getter device was activated by heating the ring 11, by means of
high frequency heating, to 900.degree.C for 10 minutes. When the
system was again at a pressure of the order of 10.sup.-.sup.8 torr
and the getter ring 11 had cooled down to room temperature, carbon
monoxide was allowed to flow into the system through a conductance,
C, of value 40cc/sec (for CO) in such a way that the CO gas
pressure above the getter device, Pg, was maintained at a constant
value of 3 .times. 10.sup.-.sup.6 torr. At various intervals of
time (t) the CO gas pressure (Pm) at the conductance inlet,
required to maintain Pg at the constant value, was measured.
From the values of C, Pm, Pg and t obtained a curve of CO gas
sorption rate as a function of total gas quantity sorbed by the
getter material can be constructed. These results are shown in
graphical form in FIG. 8 as curve 1.
EXAMPLE 2
The procedure of Example 1 was followed in all respects except that
during the CO sorption step the getter ring was maintained at
400.degree.C by means of high frequency heating.
The results are shown in FIG. 8 as curve 2.
EXAMPLE 3
The tests of this example were performed to show the behavior of
getter devices of the present invention.
The procedure of Example 1 was followed in all respects except that
the graphite was replaced by an equal volume of a
zirconium-aluminum alloy of composition 16 weight percent aluminum,
balance zirconium. In this example, the weight ratio of Zr to Zr-Al
alloy is 3:2.
The results are shown in FIG. 8 as curve 3.
EXAMPLE 4
The tests of this example were performed to show the behavior of a
getter device of the present invention.
The procedure of Example 3 was followed in all respects except that
during the CO sorption step the getter ring was maintained at
400.degree.C by means of high frequency heating.
The results are shown in FIG. 8 as curve 4.
DISCUSSION
It is seen from FIG. 8, by comparing curve 2 with curve 4 and by
comparing curve 1 with curve 3, that at 400.degree.C the getter
materials of the present invention have a higher gas sorption
speed, at a given quantity of gas already sorbed, than that of
traditional getters and that at room temperature the gettering
properties are at least equal.
The results shown in FIG. 8 have been confirmed by further
experimentation since the filing of Italian application Ser. No.
28,053 A/72 on Aug. 10, 1972, now Italian Pat. No. 963,874, under
which priority rights are claimed. The average results of the
further experimentation are shown in FIG. 9 wherein curve 1'
corresponds to curve 1 of FIG. 8, etc.
Although the invention has been described in considerable detail
with reference to certain preferred embodiments thereof, it will be
understood that variations and modifications can be effected within
the spirit and scope of the invention as described above and as
defined in the appended claims.
* * * * *