EP0559283B1 - Cathode with porous cathode element - Google Patents
Cathode with porous cathode element Download PDFInfo
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- EP0559283B1 EP0559283B1 EP93200563A EP93200563A EP0559283B1 EP 0559283 B1 EP0559283 B1 EP 0559283B1 EP 93200563 A EP93200563 A EP 93200563A EP 93200563 A EP93200563 A EP 93200563A EP 0559283 B1 EP0559283 B1 EP 0559283B1
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- cathode
- particles
- cathode element
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- high melting
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- 239000002245 particle Substances 0.000 claims description 49
- 229910052751 metal Inorganic materials 0.000 claims description 22
- 239000002184 metal Substances 0.000 claims description 22
- 239000011148 porous material Substances 0.000 claims description 21
- 238000002844 melting Methods 0.000 claims description 15
- 150000004706 metal oxides Chemical class 0.000 claims description 7
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 claims description 6
- 229910044991 metal oxide Inorganic materials 0.000 claims description 6
- 238000009826 distribution Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 150000002739 metals Chemical class 0.000 claims description 4
- 239000000758 substrate Substances 0.000 claims description 4
- 230000008018 melting Effects 0.000 claims 10
- 239000007789 gas Substances 0.000 description 6
- 229910052721 tungsten Inorganic materials 0.000 description 6
- 230000008020 evaporation Effects 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 5
- 238000010849 ion bombardment Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000011109 contamination Methods 0.000 description 3
- 239000011159 matrix material Substances 0.000 description 3
- 231100000572 poisoning Toxicity 0.000 description 3
- 230000000607 poisoning effect Effects 0.000 description 3
- 238000004544 sputter deposition Methods 0.000 description 3
- 239000002156 adsorbate Substances 0.000 description 2
- 238000005253 cladding Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 2
- 239000010937 tungsten Substances 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910021193 La 2 O 3 Inorganic materials 0.000 description 1
- -1 Sc 2 O 3 Chemical class 0.000 description 1
- 229910052776 Thorium Inorganic materials 0.000 description 1
- 150000004645 aluminates Chemical class 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000013528 metallic particle Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052762 osmium Inorganic materials 0.000 description 1
- HJGMWXTVGKLUAQ-UHFFFAOYSA-N oxygen(2-);scandium(3+) Chemical class [O-2].[O-2].[O-2].[Sc+3].[Sc+3] HJGMWXTVGKLUAQ-UHFFFAOYSA-N 0.000 description 1
- 238000004663 powder metallurgy Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000003870 refractory metal Substances 0.000 description 1
- 229910052702 rhenium Inorganic materials 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 229910052706 scandium Inorganic materials 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
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Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
- H01J1/00—Details of electrodes, of magnetic control means, of screens, or of the mounting or spacing thereof, common to two or more basic types of discharge tubes or lamps
- H01J1/02—Main electrodes
- H01J1/13—Solid thermionic cathodes
- H01J1/14—Solid thermionic cathodes characterised by the material
Definitions
- the invention relates to a cathode with a porous cathode element which contains at least one high-melting metal and nanostructured particles with an average diameter ⁇ 1000 nm.
- vacuum electron tubes for example picture tubes, X-ray tubes and generally tubes in high-frequency and microwave technology
- HDTV cathodes must allow emission current densities of 20 A / cm 2 , whereby the operating temperatures should be well below 1000 ° C and lifetimes of more than 20,000 h are required.
- Cathodes of modern high-performance X-ray tubes are said to deliver emission current densities of 10A / cm 2 at relatively high residual gas pressures of up to 10 -3 mbar and with intensive ion bombardment.
- the most important property criterion of a cathode is a constant high emission current density over the lifetime.
- the electron emission can be increased exponentially by increasing the temperature.
- a dispenser cathode with a thermionically emitting cathode element of the type mentioned at the beginning is known from EP-A-0442 163 as an I-cathode.
- Oxide particles such as BaO are embedded in a material structure.
- a cathode with a porous metal body is known from FR-A 1 410 641.
- the coarse porous body has a thin emitting layer on one surface, the porosity of which is so fine that there is a uniform emission.
- cathode with impregnated pores is known. This cathode contains both particles of high-melting metal and particles of scandium oxides.
- the invention has for its object to design a cathode element of the type mentioned in such a way that higher emission current densities with a long service life are made possible at a given temperature.
- the cathode element is formed entirely from particles whose average diameter is less than 1000 nm, and which are connected to one another in a homogeneous distribution, in that 5 to 90% of the total volume of the cathode element consists of unfilled and open pores, the free distances between adjacent particles formed by the pores being less than 1000 nm.
- Another cathode is characterized in that the porous cathode element contains both particles of high-melting metals and particles of metal oxides (such as Sc 2 O 3 , Y 2 O 3 , Eu 2 O 3 , La 2 O 3 , ThO 2 ) a heatable Substrate are applied.
- the porous cathode element contains both particles of high-melting metals and particles of metal oxides (such as Sc 2 O 3 , Y 2 O 3 , Eu 2 O 3 , La 2 O 3 , ThO 2 ) a heatable Substrate are applied.
- a cathode element according to the invention is referred to below as an “effusion cathode element”, since electrons “operate” from the near-surface, densely distributed pores into a vacuum during operation.
- An effusion cathode element in the sense of the present invention if it does not itself contain alkaline earth oxides, can be used as a cover element e.g. can be used for an I-cathode of known type.
- an effusion cathode element according to the invention can also contain particles of alkaline earth oxides, so that it can then be used as a full-fledged cathode element.
- a homogeneous distribution of the particles means that in each volume element with a volume (20 d ⁇ ) 3 the numbers of the respective particles with an average diameter d ⁇ deviate from each other by less than ⁇ 20%, d being defined as the mean of the statistically scattering diameter d of the particles.
- the diameter d of naturally not precisely spherical particles is to be understood as the mean value of the spatial extent of the particles measured in different angular positions.
- Effusion cathode elements according to the invention can additionally be provided with cover layers made of Os or Ru, which are known per se. Such cover layers should also be designed with open pores.
- an effusion cathode element In the case of an effusion cathode element according to the invention, the elements and compounds important for electron emission adjoin in a homogeneous fine distribution with a large total area of pores. Since the pores are open and thus accessible from the outer surfaces of the effusion cathode element in a manner free of solids, the active area of the effusion cathode body according to the invention is considerably enlarged. Subsequent delivery of alkaline earth atoms to near-surface areas is through the open pores facilitated. As a result, high emission current densities can be achieved even at relatively low operating temperatures.
- An arrangement according to the invention is also insensitive to ion bombardment (sputtering) and to residual gas occupancy (poisoning).
- sputtering ion bombardment
- residual gas occupancy residual gas occupancy
- the effusion cathode element consists of particles, of which at least 90% have a diameter in the range from 5 to 1000 nm, preferably 30 to 500 nm.
- the smaller the particle diameter the larger the ratio of the total available active surface to the outer surface of the effusion cathode element.
- particle diameters that are too small d ⁇ 1 nm
- pore diameters that are too small the effectiveness of the pores becomes too low, since structures made of particles with d ⁇ 1 nm do not remain stable in the long run at operating temperatures of 750 °. If more than 10% of the particles of the solid structure had diameters of more than 500 nm, the intrinsically excellent resistance of the cathodes according to the invention to ion bombardment was noticeably deteriorated.
- the high-melting metal components should have a proportion of> 30%, in particular about 50-90%, of the total volume of the solid particles. A value of about 50% has proven advantageous for effusion cathode bodies according to the invention containing alkaline earth oxide particles. With a metal content of less than 30%, a sufficiently good metallic conduction of the effusion cathode element can no longer be guaranteed.
- the oxidic particles are at least partially surrounded by a thin metal shell or that at least some of the metallic particles are enveloped by a thin oxidic cover layer.
- the cladding layers must of course be structured so thin or so permeable that the covered core can become active through the cladding.
- an effusion cathode element 1 is applied to an I-cathode element 2.
- the I cathode element 2 consists of a porous W matrix 3, which is impregnated with BaCa aluminate 4.
- the structure of a volume element of the effusion cathode element 1 is indicated in FIG. 1.
- Tungsten particles 5 with an average diameter of 30 nm form a supporting framework around pore spaces 6, in which an electron gas cloud is created during operation.
- Separate oxide particles 7 of Sc 2 O 3 with approximately the same diameter are embedded.
- a surface complex 9 made of Ba-Sc -O formed on surfaces of the W-particles 5 directed towards the pores.
- a surface complex 9 made of Ba-Sc -O formed on surfaces of the W-particles 5 directed towards the pores.
- an emission current density of 110 A / cm 2 was measured after 50 hours of operation (electron current direction according to arrows 10 and 11).
- These laboratory-made samples already showed significantly better values than were achieved with previously known cathode elements.
- lifetimes of more than 3000 hours were easily achieved.
- FIG. 4 shows a meandering foil-like effusion cathode element 20, with a structure according to FIG. 2, which is arranged on a support plate 21 which is preferably made of W, Ni or Ti.
- the carrier plate 21 can also be a substrate for the production of the layer of the effusion cathode element 20.
- the meandering effusion cathode element 20 can also be heated directly without a support plate 21. If the heating current (arrow 18) is passed through, an electron current can be generated in the direction of arrow 19.
- Indirect heating can of course also be provided.
- structured effusion cathode elements can be arranged on a resistance heating conductor according to FIG. 2.
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- Solid Thermionic Cathode (AREA)
Description
Die Erfindung bezieht sich auf eine Kathode mit einem porösen Kathodenelement, welches mindestens ein hochschmelzendes Metall sowie nanostrukturierte Partikel mit mittlerem Durchmesser <1000 nm enthält.The invention relates to a cathode with a porous cathode element which contains at least one high-melting metal and nanostructured particles with an average diameter <1000 nm.
Elektronenemitter von Vakuumelektronenröhren, beispielsweise von Bildröhren, Röntgenröhren und allgemein von Röhren in der Hochfrequenz- und Mikrowellentechnik sollen wegen steigender Leistungsanforderungen hohe Emissionsstromdichten bei möglichst niedriger Betriebstemperatur, eine hohe Lebensdauer, hohe Resistenz gegenüber Vergiftung durch Restgase und ein stabiles Verhalten bei Elektronenbeschuß aufweisen.Due to increasing performance requirements, electron emitters of vacuum electron tubes, for example picture tubes, X-ray tubes and generally tubes in high-frequency and microwave technology, should have high emission current densities at the lowest possible operating temperature, a long service life, high resistance to poisoning from residual gases and stable behavior when bombarded with electrons.
HDTV-Kathoden müssen Emissionsstromdichten von 20 A/cm2 zulassen, wobei die Betriebstemperaturen deutlich unter 1000 °C liegen sollen und Lebensdauern von mehr als 20 000 h gefordert werden. Kathoden moderner Hochleistungsröntgenröhren sollen Emissionsstromdichten von 10A/cm2 bei relativ hohen Restgasdrücken von bis zu 10-3 mbar und bei intensivem Ionenbeschuß liefern.HDTV cathodes must allow emission current densities of 20 A / cm 2 , whereby the operating temperatures should be well below 1000 ° C and lifetimes of more than 20,000 h are required. Cathodes of modern high-performance X-ray tubes are said to deliver emission current densities of 10A / cm 2 at relatively high residual gas pressures of up to 10 -3 mbar and with intensive ion bombardment.
Wichtigstes Eigenschaftskriterium einer Kathode ist eine über die Lebensdauer gleichbleibend hohe Emissionsstromdichte. Bei einem bekannten Material mit gegebener Austrittsarbeit für Elektronen läßt sich die Elektronenemission durch Temperaturerhöhung exponentiell erhöhen.The most important property criterion of a cathode is a constant high emission current density over the lifetime. In a known material with a given work function for electrons, the electron emission can be increased exponentially by increasing the temperature.
Dadurch können jedoch eine Erhöhung der Verlustleistung, eine Verminderung der mechanischen Stabilität des emittierenden Festkörpers bzw. seines Heizers und infolge Verdampfung des emittierenden Materials eine schnelle Erschöpfung des Vorrats und schädliche Kontaminationen von Systembauteilen einer Röhre (beispielsweise Gitter) verursacht werden, so daß einer hinsichtlich der Elektronenemission vorteilhaften Temperaturerhöhung Grenzen gesetzt sind.However, this can increase the power loss, reduce the mechanical stability of the emitting solid or its heater and, as a result of evaporation of the emitting material, rapid depletion of the supply and harmful contamination of system components of a tube (for example a grid), so that one with regard to the Electron emission advantageous temperature increase limits are set.
Für den Hochtemperaturbetrieb sind nur wenige hochschmelzende Metalle, insbesondere W, Re und Ta als Refraktärmetalle geeignet, da gleichzeitig die Forderung nach einer niedrigen Verdampfungsrate erfüllt werden muß.Only a few high-melting metals, in particular W, Re and Ta, are suitable as refractory metals for high-temperature operation, since at the same time the requirement for a low evaporation rate must be met.
Ein Vorteil des Hoch-Temperaturbetriebs reiner Metalle ist die geringe Kontamination (Vergiftung) der Kathodenoberfläche und die geringe Empfindlichkeit gegenüber Ionenbeschuß. Allerdings ist selbst reines Wolfram für hohe Emissionsstromdichten > 5A/cm2 und Lebensdauern von > 103h ungeeignet. Demgegenüber können solche Emissionsbedingungen durch Aufbau geeigneter Oberflächenkomplexe (Adsorbat/Substrat-Dipolschichten) erfüllt werden, wodurch die Elektronenaustrittsarbeit herabgesetzt wird. Damit erreicht man hohe Emissionsstromdichten bei relativ niedrigen Betriebstemperaturen und geringe Energieverluste. In der Praxis werden Materialkombinationen von W/ThO2, W/Th, W/Ba, W/BaO, W/SC2O3/BaO/CaO/Al2O3 verwendet.An advantage of high-temperature operation of pure metals is the low contamination (poisoning) of the cathode surface and the low sensitivity to ion bombardment. However, even pure tungsten is unsuitable for high emission current densities> 5A / cm 2 and lifetimes of> 10 3 h. In contrast, such emission conditions can be met by building up suitable surface complexes (adsorbate / substrate dipole layers), whereby the electron work function is reduced. This achieves high emission current densities at relatively low operating temperatures and low energy losses. In practice, material combinations of W / ThO 2 , W / Th, W / Ba, W / BaO, W / SC 2 O 3 / BaO / CaO / Al 2 O 3 are used.
Erstrebenswert ist dabei eine möglichst uniforme Belegung der emittierenden Fläche mit Komplexen, die eine niedrige Austrittsarbeit bei gleichzeitig geringer Abdampfrate haben. Dieses Ziel versucht man in der Praxis mit Hilfe strukturmodifizierter Kathoden, wie z.B. Imprägnations-, Top-Layer-, Mixed Metal Matrix-, Multilayer- und Controlled Porosity Dispenser-Kathoden zu erreichen. Die Gründe für die dennoch unzureichende Emission der konventionellen strukturmodifizierten Kathoden sind ein zu geringer Bedeckungsgrad der emittierenden Kathodenoberfläche - z.B. mit BaO bei imprägnierten Kathoden - durch ungenügende Nachlieferung aus den Poren oder Korngrenzen nach Abdampfung/Absputtern oder wegen der Kontamination von Oberflächenplätzen durch Restgase.It is desirable to have the most uniform possible coverage of the emitting surface with complexes that have a low work function and a low evaporation rate. This goal is tried in practice with the help of structure-modified cathodes, e.g. Impregnation, top-layer, mixed metal matrix, multilayer and controlled porosity dispenser cathodes. The reasons for the inadequate emission of the conventional structure-modified cathodes are that the degree of coverage of the emitting cathode surface is too low - e.g. with BaO for impregnated cathodes - due to insufficient subsequent delivery from the pores or grain boundaries after evaporation / sputtering or because of contamination of surface areas by residual gases.
Die grundsätzliche Möglichkeit, hohe Emissionsstromdichten über Temperaturerhöhungen einzustellen, wird bei derartigen Kathodenausführungsformen über eine niedrige Lebensdauer erkauft. Im schlimmsten Fall werden Oberflächenplätze irreversibel mit Elementen bzw. Molekülen belegt, welche die Austrittsarbeit sogar noch über den Wert des reinen Matrixmetalles erhöhen. Zwar regenerierbar aber in der Auswirkung ähnlich nachteilig ist der Verlust eines die Austrittsarbeit herabsetzenden Adsorbats (z.B. Sc aus Sc203) durch Verdampfung oder Ionenbeschuß.The basic possibility of setting high emission current densities via temperature increases is paid for in the case of such cathode embodiments over a short service life. In the worst case, surface spaces become irreversible with elements or molecules that increase the work function even more than the value of the pure matrix metal. Although regenerable, the disadvantage is similarly disadvantageous in the loss of an adsorbate which lowers the work function (for example Sc from Sc 2 0 3 ) by evaporation or ion bombardment.
Eine Dispenser-Kathode mit einem thermionisch emittierenden Kathodenelement der eingangs genannten Art ist durch die EP-A-0442 163 als I-Kathode bekannt. Dabei sind in einer Materialstruktur Oxidpartikel wie beispielsweise BaO eingebettet.A dispenser cathode with a thermionically emitting cathode element of the type mentioned at the beginning is known from EP-A-0442 163 as an I-cathode. Oxide particles such as BaO are embedded in a material structure.
Aus der FR-A 1 410 641 ist eine Kathode mit einem porösen Metallkörper bekannt. Der grob poröse Körper weist dabei an einer Oberfläche eine dünne emittierende Schicht auf, deren Porösität so fein ist, daß sich eine gleichmäßige Emission ergibt.A cathode with a porous metal body is known from FR-A 1 410 641. The coarse porous body has a thin emitting layer on one surface, the porosity of which is so fine that there is a uniform emission.
Aus der GB-A 21 16 356 ist eine Kathode mit imprägnierten Poren bekannt. Diese Kathode enthält sowohl Partikel aus hochschmelzendem Metall als auch Partikel aus Scandium-Oxiden.From GB-A 21 16 356 a cathode with impregnated pores is known. This cathode contains both particles of high-melting metal and particles of scandium oxides.
Der Erfindung liegt die Aufgabe zugrunde, ein Kathodenelement der eingangs genannten Art derart zu gestalten, daß bei gegebener Temperatur höhere Emissionsstromdichten bei hoher Lebensdauer ermöglicht werden.The invention has for its object to design a cathode element of the type mentioned in such a way that higher emission current densities with a long service life are made possible at a given temperature.
Die Lösung gelingt dadurch, daß das Kathodenelement vollständig aus Partikeln gebildet ist, deren mittlerer Durchmesser kleiner als 1000 nm ist, und welche in homogener Verteilung miteinander verbunden sind, daß 5 bis 90% des Gesamtvolumens des Kathodenelements aus ungefüllten und zur Umgebung offenen Poren besteht, wobei die von den Poren gebildeten freien Abstände zwischen benachbarten Partikeln kleiner als 1000 nm sind.The solution is achieved in that the cathode element is formed entirely from particles whose average diameter is less than 1000 nm, and which are connected to one another in a homogeneous distribution, in that 5 to 90% of the total volume of the cathode element consists of unfilled and open pores, the free distances between adjacent particles formed by the pores being less than 1000 nm.
Eine weitere Kathode ist dadurch gekennzeichnet, daß das poröse Kathodenelement sowohl Partikel aus hochschmelzenden Metallen als auch Partikel aus Metalloxiden (wie Sc2O3, Y2O3, Eu2O3, La2O3, ThO2) enthält, welche auf einem beheizbaren Substrat aufgebracht sind.Another cathode is characterized in that the porous cathode element contains both particles of high-melting metals and particles of metal oxides (such as Sc 2 O 3 , Y 2 O 3 , Eu 2 O 3 , La 2 O 3 , ThO 2 ) a heatable Substrate are applied.
Ein erfindungsgemäßes Kathodenelement wird im Folgenden als "Effusionskathodenelement" bezeichnet, da Elektronen bei Betrieb aus den oberflächennahen, dicht verteilten Poren ins Vakuum "effundieren". Ein Effusionskathodenelement im Sinne der vorliegenden Erfindung kann, wenn es selbst keine Erdalkalioxide enthält, als Deckelement z.B. für eine I-Kathode bekannter Art verwendet werden. Andererseits kann ein erfindungsgemäßes Effusionskathodenelement auch Partikel aus Erdalkalioxiden enthalten, so daß es dann als vollwertiges Kathodenelement verwendbar ist.A cathode element according to the invention is referred to below as an “effusion cathode element”, since electrons “operate” from the near-surface, densely distributed pores into a vacuum during operation. An effusion cathode element in the sense of the present invention, if it does not itself contain alkaline earth oxides, can be used as a cover element e.g. can be used for an I-cathode of known type. On the other hand, an effusion cathode element according to the invention can also contain particles of alkaline earth oxides, so that it can then be used as a full-fledged cathode element.
Eine homogene Verteilung der Partikel bedeutet, daß in jedem Volumenelement mit einem Volumen (20
Als Durchmesser d von natürlich nicht genau kugelförmig ausgebildeten Partikeln ist der Mittelwert der in verschiedenen Winkellagen gemessenen räumlichen Erstrekkung der Partikel zu verstehen.The diameter d of naturally not precisely spherical particles is to be understood as the mean value of the spatial extent of the particles measured in different angular positions.
Erfindungsgemäße Effusionskathodenelemente können zusätzlich mit an sich bekannten Deckschichten aus insbesondere Os oder Ru versehen sein. Solche Deckschichten sollten aber ebenfalls offenporig gestaltet werden.Effusion cathode elements according to the invention can additionally be provided with cover layers made of Os or Ru, which are known per se. Such cover layers should also be designed with open pores.
Bei einem erfindungsgemäßen Effusionskathodenelement grenzen die für die Elektronenemission wichtigen Elemente und Verbindungen in homogener feiner Verteilung mit einer hohen Gesamtfläche an Poren an. Da die Poren offen und damit auf festkörperfreiem Wege von den Außenflächen des Effusionskathodenelements her zugänglich sind, ist die aktiv wirksame Fläche des erfindungsgemäßen Effusionskathodenkörpers erheblich vergrößert. Eine Nachlieferung von Erdalkaliatomen zu oberflächennahen Bereichen wird durch die offenen Poren hindurch erleichtert. Infolgedessen lassen sich hohe Emissionsstromdichten bereits bei relativ niedrigen Betriebstemperaturen erreichen.In the case of an effusion cathode element according to the invention, the elements and compounds important for electron emission adjoin in a homogeneous fine distribution with a large total area of pores. Since the pores are open and thus accessible from the outer surfaces of the effusion cathode element in a manner free of solids, the active area of the effusion cathode body according to the invention is considerably enlarged. Subsequent delivery of alkaline earth atoms to near-surface areas is through the open pores facilitated. As a result, high emission current densities can be achieved even at relatively low operating temperatures.
Eine erfindungsgemäße Anordnung ist auch unempfindlich gegenüber Ionenbeschuß (Sputtern) und gegen Restgasbelegung (Vergiftung). Die Sputtereffekte betreffen nämlich nur die äußere Oberfläche, nicht aber die oberflächennahen Bereiche in der porösen Struktur. Unerwünschte Restgasbelegungen im Inneren der Struktur sind unter Betriebsbedingungen erschwert, weil die dort befindlichen freien Oberflächen der Partikel in hohem Maße mit erwünschten Atomen/Molekülen belegt sind.An arrangement according to the invention is also insensitive to ion bombardment (sputtering) and to residual gas occupancy (poisoning). The sputtering effects only affect the outer surface, but not the areas near the surface in the porous structure. Undesired occupancy of residual gas in the interior of the structure is difficult under operating conditions because the free surfaces of the particles located there are occupied to a large extent with desired atoms / molecules.
Diese Vorteile kommen insbesondere dann signifikant gegenüber bekannten Kathoden zur Geltung, wenn das Effusionskathodenelement aus Partikeln besteht, von denen mindestens 90% einen Durchmesser im Bereich von 5 bis 1000 nm, vorzugsweise 30 bis 500 nm aufweisen. Je kleiner die Partikeldurchmesser sind, um so größer wird das Verhältnis der insgesamt verfügbaren aktiven Oberfläche zur äußeren Oberfläche des Effusionskathodenelements. Bei zu kleinen Partikeldurchmessern (d <1 nm) und auch bei zu kleinen Porendurchmessern wird allerdings die Wirksamkeit der Poren zu gering, da Strukturen aus Partikeln mit d < 1 nm bei Betriebstemperaturen von 750° nicht auf Dauer stabil bleiben. Falls mehr als 10% der Partikel der Festkörperstruktur Durchmesser von mehr als 500 nm aufwiesen, wurde die an sich hervorragende Widerstandsfähigkeit erfindungsgemäßer Kathoden gegen Ionenbombardement merkbar verschlechtert.These advantages are particularly significant compared to known cathodes if the effusion cathode element consists of particles, of which at least 90% have a diameter in the range from 5 to 1000 nm, preferably 30 to 500 nm. The smaller the particle diameter, the larger the ratio of the total available active surface to the outer surface of the effusion cathode element. With particle diameters that are too small (d <1 nm) and also with pore diameters that are too small, however, the effectiveness of the pores becomes too low, since structures made of particles with d <1 nm do not remain stable in the long run at operating temperatures of 750 °. If more than 10% of the particles of the solid structure had diameters of more than 500 nm, the intrinsically excellent resistance of the cathodes according to the invention to ion bombardment was noticeably deteriorated.
Die hochschmelzenden metallischen Komponenten sollten einen Anteil von > 30%, insbesondere etwa 50-90% des Gesamtvolumens der Festkörperpartikel aufweisen. Ein Wert von etwa 50% hat sich dabei für Erdalkalioxid-Partikel enthaltende erfindungsgemäße Effusionskathodenkörper als vorteilhaft erwiesen. Bei einem Metallanteil von weniger als 30% ist eine genügend gute metallische Leitung des Effusionskathodenelements nicht mehr gewährleistet.The high-melting metal components should have a proportion of> 30%, in particular about 50-90%, of the total volume of the solid particles. A value of about 50% has proven advantageous for effusion cathode bodies according to the invention containing alkaline earth oxide particles. With a metal content of less than 30%, a sufficiently good metallic conduction of the effusion cathode element can no longer be guaranteed.
Gemäß einer Weiterbildung der Erfindung ist vorgesehen,
daß die oxidischen Partikel mindestens teilweise von einer dünnen Metallhülle umgeben sind oder daß mindestens ein Teil der metallischen Partikel von einer dünnen oxidischen Deckschicht umhüllt ist. Die Hüllschichten müssen natürlich so dünn bzw. so durchlässig strukturiert sein, daß der bedeckte Kern durch die Hülle hindurch aktiv wirksam werden kann.According to a development of the invention,
that the oxidic particles are at least partially surrounded by a thin metal shell or that at least some of the metallic particles are enveloped by a thin oxidic cover layer. The cladding layers must of course be structured so thin or so permeable that the covered core can become active through the cladding.
Besonders hohe Emissionsstromdichten wurden dadurch ermöglicht, daß das Porenvolumen im oberen Teil des Effusionskathodenelements größer als im unteren Teil ist.Particularly high emission current densities were made possible in that the pore volume in the upper part of the effusion cathode element is larger than in the lower part.
Weitere Ausgestaltungen der Erfindung ergeben sich aus den Unteransprüchen.Further embodiments of the invention result from the subclaims.
Die Erfindung wird anhand der Beschreibung von in der Zeichnung dargestellten vorteilhaften Ausführungsbeispielen näher erläutert.
- Fig. 1
- zeigt einen Schnitt durch ein Volumenelement eines erfindungsgemäßen Effusionskathodenelements, welches W- und Sc2O3-Partikel, aber keine Erdalkalioxid-Partikel enthält und als Auflage für ein I-Kathodenelement (Fig. 3) geeignet ist.
- Fig. 2
- zeigt eine Ausführung mit Erdalkalioxid-Partikeln, welches als vollwertiges Dispenserkathodenelement verwendbar ist.
- Fig. 3
- zeigt einen Schnitt durch ein Kathodenelement, bei welchem ein Effusionskathodenelement nach Fig. 1 auf einem I-Kathodenelement aufgebracht ist.
- Fig. 4
- zeigt eine strombeheizte mäanderförmige Ausführungsform eines Effusionskathodenelements mit einer Struktur nach Fig. 2.
- Fig. 1
- shows a section through a volume element of an effusion cathode element according to the invention, which contains W and Sc 2 O 3 particles but no alkaline earth oxide particles and is suitable as a support for an I-cathode element (FIG. 3).
- Fig. 2
- shows an embodiment with alkaline earth oxide particles, which can be used as a full dispenser cathode element.
- Fig. 3
- shows a section through a cathode element in which an effusion cathode element according to FIG. 1 is applied to an I-cathode element.
- Fig. 4
- shows a current-heated meandering embodiment of an effusion cathode element with a structure according to FIG. 2.
Gemäß Fig. 3 ist ein Effusionskathodenelement 1 auf einem I-Kathodenelement 2 aufgebracht. Das I Kathodenelement 2 besteht aus einer porösen W-Matrix 3, welche mit BaCa-Aluminat 4 imprägniert ist. Die Struktur eines Volumenelements des Effusionskathodenelements 1 ist in Fig. 1 angedeutet. Wolfram-Partikel 5 mit einem mittleren Durchmesser von 30 nm bilden ein tragendes Gerüst um Porenräume 6, in welchen bei Betrieb eine Elektronengaswolke entsteht. Eingelagert sind separate Oxidpartikel 7 aus Sc2O3 mit etwa gleichen Durchmessern. Infolge der Lieferung von Ba in Richtung des Pfeils 8 aus dem I-Kathodenelement 2 (Fig. 3) wird bei Betrieb der Kathode bei z.B. 900° C auf zu den Poren hin gerichteten Flächen der W-Partikel 5 ein Oberflächenkomplex 9 aus Ba-Sc-O gebildet. Bei 900° C und einer Feldstärke von ca. 4 kV/mm wurde nach 50 Stunden Betriebsdauer eine Emissionsstromdichte von 110 A/cm2 gemessen (Elektronenstromrichtung gemäß den Pfeilen 10 und 11). Es ergaben sich bereits bei diesen labormäßig hergestellten Proben erheblich bessere Werte als mit bisher bekannten Kathodenelementen erreicht wurden. Bei 965°C wurden Lebensdauern von mehr als 3000 Stunden problemlos erreicht.3, an
Bei der Ausführung nach Fig. 2 sind Sc203-Kerne 12 und BaO-Kerne 13 (oder auch CaO-Kerne) mit W-Schichten 14a bzw. 14b umhüllt. Auf den zu den Porenräumen 15 gerichteten W-Flächen der zweischichtigen Partikel werden emittierende Schichten aus Ba-Sc-O gebildet. Für den in Richtung der Pfeile 16,17 fließenden Elektronenstrom wurden Stromdichten von 95 A/cm2 bei 850° C und Feldstärken von ca. 4kV/mm gemessen. Bei bekannten pulvermetallurgisch hergestellten Kathodenelementen, welche also keine offenporige Struktur aufweisen, konnte unter vergleichbaren Bedingungen höchstens 80 A/cm2 erreicht werden. Dabei ist zu bedenken, daß die mit der Erfindung erreichten günstigen Werte an nicht optimierten labormäßig hergestellten Proben gemessen wurden. Die bei der Erfindung erforderliche Offenporigkeit konnte mit Niederschlagsverfahren wie insbesondere PCVD erreicht werden. Sinterverfahren erwiesen sich als wenig geeignet.2, Sc 2 0 3
Fig. 4 zeigt ein mäanderförmig folienartiges Effusionskathodenelement 20, mit einer Struktur nach Fig. 2, welches auf einem vorzugsweise aus W, Ni oder Ti bestehenden Tragblech 21 angeordnet ist. Das Tragblech 21 kann gleichzeitig Substrat für die Herstellung der Schicht des Effusionskathodenelements 20 sein.FIG. 4 shows a meandering foil-like
Wegen der metallischen Leitfähigkeit erfindungsgemäßer Effusionskathodenelemente und der nanostrukturierten homogenen Struktur läßt sich das mäanderförmige Effusionskathodenelement 20 auch ohne Tragblech 21 direkt heizen. Bei einem hindurchgeleiteten Heizstrom (Pfeil 18), kann ein Elektronenstrom in Richtung des Pfeils 19 erzeugt werden.Because of the metallic conductivity of effusion cathode elements according to the invention and the nanostructured homogeneous structure, the meandering
Man kann natürlich auch eine indirekte Heizung vorsehen. Beispielsweise können gemäß Fig. 2 strukturierte Effusionskathodenelemente auf einem Widerstandsheizleiter angeordnet sein.Indirect heating can of course also be provided. For example, structured effusion cathode elements can be arranged on a resistance heating conductor according to FIG. 2.
Claims (10)
- A cathode including a porous cathode element which comprises a high melting point metal between two facing surfaces, characterized in that the cathode element (1) comprises particles (5,7) of a high melting point metal, in that less than 10% of the particles (5,7) have a diameter in excess of 500 nm, and in that the cathode element (1) has pores which are accessible from one or both surfaces.
- A cathode including a porous cathode element comprising a high melting point metal between two facing surfaces, characterized in that the cathode element (1) comprises particles (5) of a high melting point metal as well as particles of metal oxides (7), in that less than 10% of the particles (5,7) have a diameter in excess of 500 nm, and in that the cathode element (1) has pores which are accessible from one or both surfaces.
- A cathode as claimed in Claim 2, characterized in that the porous cathode element (1) is provided with heating means.
- A cathode including a porous cathode body (3) which is provided with an impregnant (4) and with an emissive surface, characterized in that the cathode comprises a porous cathode element (1) on its emissive surface, which element comprises a high melting point metal between two facing surfaces, the cathode element (1) comprising particles (5) of a high melting point metal as well as particles of metal oxides (7), in that less than 10% of the particles (5,7) have a diameter in excess of 500 nm, and in that the cathode element (1) has pores which extend between the two surfaces.
- A cathode including a porous cathode element comprising at least a high melting point metal as well as nano-structured particles having an average diameter of < 1000 nm, characterized in that the cathode element (1) completely consists of particles (5, 7) whose average diameter is smaller than 1000 nm and which in a homogeneous distribution are connected to each other, in that 5 to 90% of the overall volume of the cathode element (1) consists of unfilled pores (6, 15) which are open to their surroundings, the free distances, constituted by the pores (6, 15), between neighbouring particles (5, 7, 14a, 14b) being smaller than 1000 nm.
- A cathode as claimed in Claim 5, characterized in that the porous cathode element comprises particles of high melting point metals (5), as well as particles of metal oxides (7), which are provided on a heatable substrate.
- A cathode as claimed in Claim 5, characterized in that the porous cathode element exclusively comprises particles of a high melting point metal (5) or particles of metal oxides (7) and in that the cathode element (1) is provided on an I cathode element (2).
- A cathode as claimed in Claim 5 or 6, characterized in that the porous cathode element comprises particles of a high melting point metal and particles of metal oxides and particles of alkaline earth metal oxides.
- A cathode as claimed in any one of Claims 5 to 8, characterized in that the metal fraction (5, 14a, 14b) amounts to a volume fraction of > 30% of all the solid-state particles.
- A cathode as claimed in any one of Claims 5 to 9, characterized in that the porous cathode element (1) is composed of particles (5, 7, 14a, 14b) of which at least 30% has a diameter in the range from 5 to 1,000 nm, preferably from 30 to 500 nm.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4206909 | 1992-03-05 | ||
| DE4206909A DE4206909A1 (en) | 1992-03-05 | 1992-03-05 | THERMIONIC EMITTING CATHODE ELEMENT |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0559283A1 EP0559283A1 (en) | 1993-09-08 |
| EP0559283B1 true EP0559283B1 (en) | 1996-11-13 |
Family
ID=6453269
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP93200563A Expired - Lifetime EP0559283B1 (en) | 1992-03-05 | 1993-03-01 | Cathode with porous cathode element |
Country Status (3)
| Country | Link |
|---|---|
| EP (1) | EP0559283B1 (en) |
| JP (1) | JPH065198A (en) |
| DE (2) | DE4206909A1 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4400353A1 (en) * | 1994-01-08 | 1995-07-13 | Philips Patentverwaltung | Controllable thermionic electron emitter |
| DE19652822A1 (en) | 1996-12-18 | 1998-06-25 | Patent Treuhand Ges Fuer Elektrische Gluehlampen Mbh | Sintered electrode |
| DE19855670A1 (en) * | 1998-12-02 | 1999-12-09 | Siemens Ag | Steam generator operating method |
| DE102006024437B4 (en) * | 2006-05-24 | 2012-08-09 | Siemens Ag | X-ray |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL266639A (en) * | 1960-07-05 | |||
| FR1410641A (en) * | 1963-10-04 | 1965-09-10 | Philips Nv | Porous metal body and its manufacturing process |
| JPS58154131A (en) * | 1982-03-10 | 1983-09-13 | Hitachi Ltd | Impregnation type cathode |
| US4986788A (en) * | 1989-11-02 | 1991-01-22 | Samsung Electron Devices Co., Ltd. | Process of forming an impregnated cathode |
| KR920001335B1 (en) * | 1989-11-10 | 1992-02-10 | 삼성전관 주식회사 | Dispenser cathode |
-
1992
- 1992-03-05 DE DE4206909A patent/DE4206909A1/en not_active Withdrawn
-
1993
- 1993-03-01 EP EP93200563A patent/EP0559283B1/en not_active Expired - Lifetime
- 1993-03-01 DE DE59304447T patent/DE59304447D1/en not_active Expired - Fee Related
- 1993-03-03 JP JP4276893A patent/JPH065198A/en active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| DE4206909A1 (en) | 1993-09-09 |
| DE59304447D1 (en) | 1996-12-19 |
| JPH065198A (en) | 1994-01-14 |
| EP0559283A1 (en) | 1993-09-08 |
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