EP1805785B1 - Incandescent lamp having an illuminant that contains a high-temperature resistant metal compound - Google Patents
Incandescent lamp having an illuminant that contains a high-temperature resistant metal compound Download PDFInfo
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- EP1805785B1 EP1805785B1 EP05803936A EP05803936A EP1805785B1 EP 1805785 B1 EP1805785 B1 EP 1805785B1 EP 05803936 A EP05803936 A EP 05803936A EP 05803936 A EP05803936 A EP 05803936A EP 1805785 B1 EP1805785 B1 EP 1805785B1
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- carbon
- sink
- hydrogen
- illuminant
- incandescent lamp
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01K—ELECTRIC INCANDESCENT LAMPS
- H01K1/00—Details
- H01K1/52—Means for obtaining or maintaining the desired pressure within the vessel
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- the invention relates to an incandescent lamp with a luminous body containing a high-temperature-resistant metal compound, according to the preamble of claim 1. It is in particular bulbs with a carbide-containing filament, in particular the invention relates to halogen incandescent lamps having a luminous body of TaC, or whose luminous body TaC contains as a component or coating.
- a common method of solving the problem of preventing vaporization of filament material is by using circular processes.
- the filling gas a further chemical substance is added, which reacts in colder areas with the evaporated material to a relatively volatile compound, which does not deposit on the bulb wall.
- This compound is transported in the build-up concentration gradient - namely high concentration near the bulb wall, low concentration near the filament - in the direction of the filament.
- the material of the filament is attached to this again.
- the tungsten evaporating from the filament combines at lower temperatures near the bulb wall to tungsten halides, which are volatile at temperatures above about 200 ° C and do not deposit on the bulb wall. This prevents a tungsten failure on the bulb wall.
- the tungsten halide compounds are transported back by diffusion and possibly also convection to the hot filament, where they decompose. The freed tungsten is again attached to the filament. However, the tungsten i.allg. not transported back to the same site from which it has evaporated, but deposited at a location of different temperature, i. the cycle is not regenerative. An exception is the fluorine cycle.
- the gaseous carbon formed upon decomposition of the TaC is transported towards the bulb wall, where it reacts with hydrogen to form hydrocarbons such as methane. These hydrocarbons are transported back to the hot filament, where they decompose again. The carbon is released again and can attach to the filament. However, at low temperatures, the hydrocarbons decompose below 1000 K, so that the return of carbon is not targeted to the hottest spots of the filament.
- the evaporation from the luminous element is relatively strong and the compound carrying the cyclic process is stable only at very low temperatures, such as the hydrocarbons in the last example, the luminous body will be rapidly destroyed, because it will rapidly attack the evaporating material like carbon impoverished in the last example.
- the carbon is relatively fast from the hottest points of the filament to the colder places of the filament or the outlets transported to the luminous body, which can also cause problems, for example by Windungs gleich. Only a very small proportion of the transported back carbon reaches the hottest point of the helix (very low degree of regeneration).
- the back reaction of the carbon with the hydrogen to hydrocarbons proceeds in any case only with a relatively large excess of hydrogen sufficiently fast, so that a blackening of the piston is avoided.
- WO-A 03/075315 described the regeneration of the filament out of a depot out. From the depot continuously evaporates a chemical substance, which supplies the luminous body that substance to which it is depleted again.
- a chemical substance which supplies the luminous body that substance to which it is depleted again.
- the gas phase is permanently supplied with a chemical compound, which also contains carbon; In this case, carbon is provided continuously, which can replace the evaporated by the filament carbon again.
- the disadvantage here is that changes the composition of the gas phase and the luminous body continuously by the permanently supplied chemical compound; a lamp operation in stable conditions is hardly possible.
- the concentration of carbon in the gas phase is constantly increased, which eventually leads to the deposition of carbon in inappropriate places such as the ends of the luminous element or finally the bulb wall.
- An enrichment of carbon in the luminous body is not desirable because it changes the properties of the filament continuously.
- An enrichment of hydrogen in the gas phase leads by increasing the heat conduction to an increasing cooling of the filament.
- high temperature resistant metal compound means compounds whose melting point is near the melting point of tungsten, sometimes even higher.
- the material of the luminous body is preferably TaC or Ta 2 C.
- carbides of Hf, Nb or Zr and, moreover, alloys of these carbides are suitable.
- nitrides or borides of such metals Common to these compounds is the property that a luminous body made of this material depletes in operation on at least one element.
- the principle described below is equally applicable to filaments of metals.
- metal compound used below is therefore not to be understood as limiting, but by way of example. The statements made therein are analogously applicable to metals.
- a lamp If a lamp is operated at high temperatures, it comes - depending on the nature of the material of the filament - to evaporate material or components of the material.
- the evaporated material or its constituents are replaced by e.g. Convection, diffusion or thermal diffusion removed and deposit elsewhere in the lamp, e.g. on the bulb wall or frames.
- the evaporation of the material or its components leads to a rapid destruction of the filament. Due to the material which separates on the bulb wall, the transmission of the light is greatly reduced.
- the task is to minimize by appropriate measures evaporation from the lamp or to undo.
- the adjustment of the required concentration over the luminous element is to be realized by a continuous transport of a substance containing the component in question from a source into a sink.
- the continuous deposition of the material supplied from the source avoids a change in the composition of the gas phase and enables operation of the luminous element under constant conditions.
- the source of a solid, or liquid, hydrocarbon which is introduced into the lamp so that builds up on the source material, a certain vapor pressure of gaseous hydrocarbon.
- This hydrocarbon is transported by diffusion or convection into the interior of the lamp, where it decomposes at higher temperatures near the filament.
- the luminous body is thus in a carbon-enriched atmosphere; a decomposition of the filament is thereby prevented.
- the filament does not emit carbon to the environment, nor is carbon enriched in it. In other words, a balance between carbon deposition and carbon evaporation sets in the luminous body. At lower temperatures near the bulb wall, the carbon reacts again Back to hydrogen hydrocarbons.
- the hydrocarbon decomposes with deposition of solid carbon (soot).
- This process corresponds approximately to the cracking of hydrocarbons in suitable catalysts known from the technical chemistry, in which case - in contrast to the reaction regime in plants of the chemical industry - the deposition of carbon on the catalyst is desired.
- carbon continuously exits from one source and is re-deposited in a sink.
- the filament of the lamp is thus neither enriched in carbon, nor depleted of carbon;
- the carbon concentration in the gas phase is kept constant.
- the hydrogen can preferably be used analogously.
- the permeable quartz piston wall acts at high temperatures.
- the resulting hydrogen can be trapped by iodine (reaction to hydrogen iodide, the resulting hydrogen iodide is not critical to its effect on the maintenance of the lamp, because it does not interfere with the chemistry of the metal carbide nor the physical properties of the filler gas (especially the thermal conductivity)
- Another way of attaching the released hydrogen ie, a sink of hydrogen
- metals such as zirconium or hafnium or niobium or tantalum, which "getter" hydrogen at appropriate temperatures.
- transport processes described in the last paragraphs can still be superimposed by one or more cycle processes.
- a TaC lamp to superimpose a carbon cycle process on the described permanent transport of carbon from a source into a sink, for example a CH, C-halogen, CS or CN cycle process as in the application DE-Az 103 56 651.1 described.
- the sinking metals may be e.g. in the form of wires or plates welded to the frame or the power supply, or wound as a coating coil directly around the power supply, or e.g. in the form of wires to be squeezed directly. It is essential in particular when using catalytically active metals as sinks that the surface of these metals is sufficiently large, since the surface is continuously covered with carbon ("poisoning" of the catalyst) in order to obtain the effectiveness of the catalyst. Also, the coating of Wendelabêtn or power supplies with serving as a sink metals is another embodiment.
- elemental carbon is used as the source of carbon.
- This may be present, for example, in the form of carbon compacts, graphite fibers or carbon black deposited on a substrate, diamond in the form of DLC or graphite.
- the carbon is maintained at a "medium" temperature, which must be just enough so that the resulting vapor pressure of the carbon at the location of the hot filament results in a carbon partial pressure which is approximately equal to the carbon equilibrium vapor pressure above the tantalum carbide.
- the carbon If the carbon reaches colder areas near the bulb wall, it reacts with hydrogen or halogens to (possibly halogenated) hydrocarbons; This prevents the deposition of carbon on the piston wall.
- the decomposition of the hydrocarbon then takes place on a catalyst, in which case the carbon deposits on the surface of the catalyst and the hydrogen is liberated again.
- you do not need a sink for the hydrogen or possibly the halogen which indeed prevent only the deposition of the carbon on the piston wall and transport the bonded in the form of hydrocarbon carbon to the catalyst.
- the hydrogen or optionally the halogen thus serves only as a means of transport to transport the carbon and is not consumed.
- carbon is transported from the carbon source (carbon compact, graphite fibers, diamond such as DLC, graphite layers, carbon black, etc.) to the carbon sink (eg, nickel, iron, molybdenum wire) where it deposits again.
- carbon source carbon compact, graphite fibers, diamond such as DLC, graphite layers, carbon black, etc.
- carbon sink eg, nickel, iron, molybdenum wire
- the carbon is deposited on a few turns of the filament metal carbide filament.
- the carbon deposition takes place on the outer turns of the coil at lower temperatures than in the middle of the filament. Since the vapor pressure over pure carbon is greater than the carbon vapor pressure over tantalum carbide, the source of pure carbon is attached at lower temperatures than the hot coil center. As a result, as far as possible the carbon equilibrium vapor pressure over the middle of the hot coil should be set and achieved that no carbon-transporting gradient of the carbon partial pressure is produced via the luminous body.
- the last described approach is also useful for circumventing problems related to the relatively low impact strength of the tantalum carbide during transport of the lamps to the customer.
- One option for circumventing this problem is to complete the carburization only after the lamps have been transported to the customer during the firing process and initially to leave at least one tantalum core in the TaC luminous element.
- the reaction with the hydrocarbon is not complete, the large amounts of carbon released that must be held in the gas phase also present a problem.
- This problem can be overcome in the manner described by leaving the incompletely fully carburized luminescent body is located in a continuous stream of carbon from a source of carbon.
- the non-carburizing carbon reacts with hydrogen to form hydrocarbons, thereby preventing the deposition of carbon on the piston wall.
- the hydrocarbon eventually decomposes back to a catalyst, depositing the unneeded carbon and liberating the hydrogen. It comes with a relatively small amount of hydrogen, because it is not consumed, but only serves to transport the carbon to the carbon sink. In particular, the amount of hydrogen remains constant and does not increase permanently during carburization.
- the hydrogen can be replaced by the hydrogen Use of iodine near the piston wall to be intercepted and stabilized as hydrogen iodide.
- Another way to realize a carbon source is to use a tantalum carbide coated carbon fiber.
- the carbon diffuses through the tantalum carbide layer; a depletion of the Tantalkarbid für of carbon is thus avoided.
- the carbon released thereby into the gas space leads to a rapid blackening of the piston wall, if no countermeasures are taken.
- blackening of the bulb can be prevented if the bulb temperatures are not too high.
- very large amounts of hydrogen are needed to "catch" the carbon as completely as possible before its deposition on the bulb wall. This can be avoided by decomposing the hydrocarbon at a catalyst maintained at a suitable temperature, eg a wire of nickel, iron, etc.
- the carbon is deposited on the nickel wire, while the hydrogen is released again and is available for reaction with more carbon available.
- the hydrogen serves only as a "vehicle” to intercept carbon transported by the luminous body by the formation of hydrocarbon and to transport it to the carbon sink (eg wire made of nickel, molybdenum, etc.).
- the carbon sink eg wire made of nickel, molybdenum, etc.
- no hydrogen is consumed in this transport mechanism, ie it comes with a relatively small amount of hydrogen.
- one would alternatively implement a cyclic process one would have to use very large amounts of hydrogen in order to trap the transported in large concentration by the filament carbon by formation of hydrocarbons or build such a high concentration of hydrocarbons near the bulb wall that the return of carbon to the Luminous body exactly compensates for the removal.
- a source it makes sense to coat the filament with the material to which it is depleted and which is to be supplied from a source again, and then again a layer of the actual filament material from the outside on this layer applied.
- a luminous element eg consists of a metal carbide such as tantalum carbide or hafnium carbide
- a layer of carbon is deposited on the surface of the filament of metal carbide.
- a layer of a metal carbide is then applied again.
- the operation is quite similar to that of a metal carbide coated carbon fiber.
- the application of the carbon coating is carried out, for example, according to a CVD method in the stud lamp, for example by decomposition of methane (1 bar pressure) at a temperature of about 2,500 K on the filament.
- the application of the metal carbide outer layer is carried out in the CVD method, for example, by simultaneous thermal decomposition of metal halides such as tantalum halide and methane; Of course, it is also possible to use other metal compounds or hydrocarbons as precursor.
- the metal carbide can then be deposited directly on the surface of the luminous element, eg according to TaCl 5 + CH 4 + x H 2 -> TaC + 5 HCl + (x - 1 ⁇ 2) H 2 .
- the hydrogen serves here to avoid the deposition of soot. It is also possible to deposit only the metal on the carbon surface of the filament and then to react (ie carburize) in an atmosphere containing, for example, methane, carburizing from the outer carbon-containing atmosphere and from the inside from the carbon layer starts.
- a disadvantage of this method is that the volume change occurring in the transformation of the metal into metal carbide causes relatively large layer stresses. Therefore, a simultaneous deposition of the metal and the carbon in the stoichiometric ratio is advantageous.
- the materials of the inner material (e.g., wire) of metal carbide and the outer layer of metal carbide need not necessarily be identical.
- the inner wire may be tantalum carbide
- the outer layer applied to the carbon layer may be hafnium carbide or HfC-4TaC alloy.
- HfC or the alloy HfC-4TaC has lower vapor pressures than pure tantalum carbide.
- hafnium is significantly more expensive than tantalum, the amount of hafnium used can be significantly reduced in this way.
- sintered materials with carbon come into consideration, such as in US 3,405,328 described. It describes how metal carbides such as tantalum carbide with dissolved carbon can be produced by sintering processes at high temperatures and high pressures in autoclaves. These materials, which are to serve as the filament material, then contain significantly more carbon than is to be expected according to the stoichiometry of the TaC. The patent also describes the use of mixtures of various carbides in order to increase the impact strength of the filament.
- carbon sinks are metals such as tungsten, tantalum, zirconium, etc., which form carbides at suitable temperatures.
- the operating temperature of these metals depends in particular on the flow of carbon coming from the luminous element; Common temperatures are in the range between 1800 ° C and 2500 ° C.
- Hydrogen is preferably used in the use of these metals in order to prevent the carbon from being deposited on the bulb wall and to form carbon. Sink to transport. If one were to forego the hydrogen, then the carbon transported by the luminous body would - if it does not accidentally strike the carbide-forming metal on its way from the luminous body - deposit on the bulb wall. With additional use of hydrogen, the carbon first reacts with the hydrogen to form a hydrocarbon, such as methane, which then decomposes back to the carbide-forming metal to transfer the carbon to the carbide-forming metal and release the hydrogen.
- a hydrocarbon such as methane
- catalysts for the decomposition of hydrocarbons are aluminum, molybdenum or magnesium silicates.
- tantalum carbide or other carbides. If, for example, a rod of tantalum carbide not flowed through by the current is brought to a temperature corresponding to the luminous element, then the suitable equilibrium vapor pressure of carbon is established above the tantalum carbide, in which vaporization or deposition of carbon no longer takes place on the luminous element.
- the rod must be at virtually the same temperature as the adjacent turns. It must under no circumstances be significantly colder than the adjacent windings, ie the heat dissipation along the rod must be limited - for example, by choosing a sufficiently small diameter.
- the advantage of using a TaC rod on the helix axis whose temperature profile corresponds as closely as possible to that of the helix is that the carbon equilibrium pressures, which prevent decomposition of the luminous body, are then automatically adjusted at the individual turns of the TaC helix.
- carbon and fluorine-containing polymers can be used, as they arise, for example, in the polymerization of tetrafluoroethylene C 2 F 4 (eg polytetrafluoroethylene PTFE, brand name "Teflon" at the company DUPONT).
- C 2 F 4 eg polytetrafluoroethylene PTFE, brand name "Teflon” at the company DUPONT.
- gas phase compounds such as CF 4 , C 2 F 4 , etc. which decompose only at very high temperatures near the filament and thereby release carbon and fluorine.
- the advantage here is that the carbon is released especially or practically exclusively at high temperature sites. The carbon is thus transported specifically to locations of high luminous body temperature.
- the liberated fluorine reacts on the wall to form gaseous SiF 4 , which then scarcely intervenes in the reaction process and also does not have a negative effect on the efficiency of the lamp, such as hydrogen, because of increased heat conduction.
- the released carbon can again - unless it is used up in the wall reaction with CO formation - first bound by a transport partner such as chlorine in colder areas and then decomposed on a hot metal wire, the carbon is deposited again and the chlorine is released (carbon sink). Since in the wall reaction two F atoms release an O atom and in polytetrafluoroethylene in about two F atoms a C atom comes, the carbon is largely reacted with the liberated in the wall reaction oxygen to CO.
- the present invention is particularly suitable for low-voltage lamps with a voltage of at most 50 V, because the necessary filament can be made relatively solid and for the wires preferably a diameter between 50 microns and 300 microns, especially at most 150 microns for general lighting purposes with maximum power of 100 W, exhibit. Thick wires up to 300 ⁇ m are used in particular for photo-optical applications up to a power of 1000 W.
- the invention is used for one-sided squeezed lamps, since the luminous body can be kept relatively short, which also reduces the susceptibility to breakage. But the application to double-sided squeezed lamps and lamps for mains voltage operation is possible.
- rod means a means formed as a solid rod or, in particular, a thin wire.
- the described concept can be applied in a variety of ways to special chemical transport systems.
- it is used for a design of a carbon-sulfur cycle.
- CS decomposes only at temperatures well above 3000 K, the degree of dissociation of CS increases strongly with increasing temperature.
- the CS cycle process is suitable for transporting the carbon back to the hottest point along the helix, thus slowing down or preventing the formation of "hot spots”.
- the sulfur atoms liberated in this temperature range then react with the carbon to CS; a decarburization of the metal carbide filament is avoided. Over the life of this carbon coating is used up slowly.
- carbon is released and deposited at lower temperatures below about 2200 K in the disproportionation of the CS.
- the CS system thus transports the carbon from places of higher temperature with T> 2200K to places of lower temperature with T ⁇ 2200 K. Without the reservoir of carbon for T> 2200 K (source) or the deposition of carbon at T ⁇ 2200 K (sink), it is difficult to achieve stationary operating conditions.
- the regenerative effect of the fluorine cycle process is based on the fact that tungsten fluorides decompose only at temperatures above about 2500 K, with the tungsten is preferably deposited again at the hottest points.
- An essential difficulty in the use of fluorine is that fluorine reacts on the bulb wall to Silliciumtetrafluorid SiF 4 , where in addition still oxygen is released. The fluorine bound in the SiF 4 is no longer available for further reaction in the halogen cycle. Therefore, several possibilities for passivating the bulb wall are mentioned in the literature, cf. eg Schröder, PHILIPS Techn. Rundschau 1963/64, p. 359 on the use of Al 2 O 3 .
- tungsten is deliberately transported back to the hottest places of the filament.
- fluorine reacts to form SiF 4 and is therefore not available for further participation in chemical transport reactions.
- the wall reaction also releases oxygen. Since in the polytetrafluoroethylene on two fluorine atoms, a carbon atom and in the wall reaction each release two fluorine atoms an oxygen atom, stoichiometrically, the released in the wall reaction oxygen can be completely gegettert by the carbon to CO. Since liberated carbon is usually otherwise bound, for example in the form of carbides, the gettering of the oxygen by the carbon is usually not complete.
- the tungsten fluorides formed at the tungsten reservoir do not become convective or diffuse completely transported in the direction of the luminous element or not fully implemented there; a part is transported in the direction of the piston wall. There, the tungsten fluorides decompose at least in part, releasing fluorine, which reacts with the wall in the manner described, and tungsten. In order to avoid blackening of the lamp bulb, the simultaneous use of bromine is recommended. As a result, tungsten (oxy) bromides can be formed and the bulb wall is kept clean.
- the tungsten oxybromides decompose at temperatures far below those of the filament. That is, the tungsten bound in them is mainly deposited on the frame or the Wendelab réellen., This superimposed W-Br (-O) cycle process is thus not regenerative, it serves only to keep the lamp bulb clear.
- the continuous transport of hydrogen from a source to a sink is treated.
- the source of hydrogen may be hydrogen stored in the luminous element (metal carbide), hydrogen taken up in the supply lines or getter (possibly bound as metal hydride, eg tantalum hydride).
- metal hydride eg tantalum hydride
- carburizing hydrogen can be enriched in the vertical lamp via the hydrogen partial pressure and the temperature distribution in the lamp and the supply lines. In lamp operation other temperature distributions prevail than when carburizing.
- the lamp temperature in lamp operation is about 3300 K - 3600 K higher than when carburizing (2800 K - 3100 K);
- carburizing higher hydrogen partial pressures can be used.
- tantalum or niobium can absorb hydrogen. Later in lamp operation, these rack parts are at a higher temperature in an atmosphere that is less Contains hydrogen, and therefore give off hydrogen (source). Parts of the frame located at a significantly lower temperature absorb this hydrogen (sink). For example, with lamps with TaC luminaires with integral filament outlets (similar to in FIG. 1 ) the helical outlets are not carburized during carburizing; Thus, tantalum is available in a wide range of temperatures, so that in any case places occur that can act as a source or sink.
- quartz glass can serve as a source of hydrogen, which is possible via the setting of a suitable content of OH groups in the glass (via the vacuum annealing of the quartz glass).
- the filling gas introduced later must take this material rearrangement into account.
- other compounds or metals which are used as hydrogen storage such as zirconium, can be used as sources of hydrogen.
- the second example merely facilitating the understanding of the invention relates to the use of sulfur in a lamp with metal carbide filament and an integral design of helix and Wendelabêtn, ie helical and Wendelab réelle are integrally made of a tantalum wire and then the filament carburized.
- helix and Wendelabêtn ie helical and Wendelab réelle are integrally made of a tantalum wire and then the filament carburized.
- helical outlets are not completely mitcarburiert, ie here you will find tantalum or Tantalsubcarbid Ta2C.
- sulfur in the lamp is converted to the very stable compound tantalum sulfide and the sulfur is thus removed from the gas phase (sink).
- the gas withdrawn from the gas phase must be constantly replenished (source) in order to maintain a CS cycle process.
- FIG. 1 shows an incandescent incandescent lamp 1 with a piston made of quartz glass 2, a pinch 3, and inner power supply lines 10, the films 4 in the pinch with a filament 7 connect.
- the filament 7 is a simple coiled, axially arranged wire of TaC, the ends 14 are uncoiled and projecting transversely to the lamp axis.
- the outer leads 5 are attached to the outside of the foils 4.
- the design described here can also be applied, for example, to lamps with luminous bodies of other metal carbides, e.g. Hafnium carbide, zirconium carbide, niobium carbide, transferred.
- metal carbides e.g. Hafnium carbide, zirconium carbide, niobium carbide
- alloys of different carbides is possible.
- borides or nitrides in particular of rhenium nitride or osmium boride, is possible.
- the lamp preferably uses a filament of tantalum carbide, which preferably consists of a single-coiled wire.
- a filament of tantalum carbide which preferably consists of a single-coiled wire.
- Zirconium carbide, hafnium carbide, or an alloy of various carbides, such as, for example, are also suitable as the filament material, which is preferably a coiled wire US-A 3 405 328 described.
- the piston is typically made of quartz glass or hard glass with a piston diameter between 5 mm and 35 mm, preferably between 8 mm and 15 mm.
- the filling is mainly inert gas, in particular noble gas such as Ar, Kr or Xe, possibly with the addition of small amounts (up to 15 mol%) of nitrogen.
- This is typically a hydrocarbon, hydrogen and a halogen additive.
- halogen is useful regardless of possible carbon-halogen cycle processes or transport processes to prevent vaporized metals from the filament of metal carbide deposition on the piston wall and possible to transport back to the filament.
- This is a metal-halogen cyclic process such as in the application DE-Az 103 56 651.1 described.
- the following circumstance is important: The more the evaporation of carbon from the luminous body can be pushed back, the lower the evaporation of the metallic component, see eg JA Coffmann, GM Kibler, TR Riethof, AA Watts: WADD-TR-60-646 Part I (1960s ).
- aliphatic hydrocarbons are usually due to the otherwise low melting point only high molecular weight compounds in question (eg, the melting point of C 56 H 114 only just below 100 ° C, which is too little for most applications, unless the use of liquid compounds is possible). More suitable are aromatic hydrocarbons such as anthracene (melting point 216 ° C), naphthacene (melting point 355 ° C), corons (melting point 440 ° C), which also have the advantage that significantly less hydrogen is introduced into the lamp per carbon atom , For example, the vapor pressure of anthracene is just below the melting point by 50 mbar, at 145 ° C just above 1 mbar.
- a suitable vapor pressure By locating the source in a range of suitable temperatures, one can set a suitable vapor pressure.
- the vapor pressure of the hydrocarbon has to be adjusted approximately in such a way that the molar concentration of carbon atoms that occurs after its complete decomposition on the TaC luminous body is of the order of the equilibrium concentration of C atoms above the luminous body; the exact value depends on details (eg distance of the C source to the filament and to the sink, rate of decomposition of the hydrocarbons at the sink, etc.).
- the appropriate temperature for the source is in the range between 120 ° C and 150 ° C, when the distance between the filament located at eg 3400 K and the source is about 3 cm and the deposition of the carbon after decomposition of the hydrocarbons takes place at a about 400 ° C - 800 ° C hot nickel wire.
- the cold filling pressure in such a lamp is in the range around 1 bar; the inert gas (eg argon, krypton) preferably contains 2 mbar - 20 mbar hydrogen H 2 , 0.5 mbar CH 2 Br 2 and 2 mbar - 20 mbar iodine.
- FIG. 1 shows schematically an example of a possible design of the source and sink for a single-pinch lamp.
- the source 6 uses as source material a solid hydrocarbon 8 deposited on the end of a wire rod 9, often called a middle holder, of tungsten.
- the rod 9 is supported by being connected to an additional sheet 11 in the center of the pinch seal 3. This can for ease of insertion have an outer wire approach 12, which typically consists of molybdenum.
- the sink 13 is realized by coating coils 15 on one or both power supply lines 10. These coils consist for example of nickel wire. This can be located in the inner volume, near the pinch, or even protrude into the pinch, as shown on the right helix 15.
- both source and sink must be operated at relatively low temperatures, typically below about 500 ° C, as found near the piston wall.
- relatively low temperatures typically below about 500 ° C, as found near the piston wall.
- the use of the power supply leads 10 near the pinch 3 is the simplest.
- the source could be attached to one power supply 10 and the drain to the other power supply 10.
- the end of the middle holder 9 is coated here with the serving as source material hydrocarbon.
- this embodiment is easy to manufacture, one has to accept that the transport from the source into the sink takes place mainly at the luminous body 7.
- the catalyst which is formed here by the sink of nickel wire, in the steady state in the entire gas phase, even outside the direct path from the source to the sink, an increased concentration at hydrocarbon or carbon.
- An advantage for the operation is therefore the use of an arrangement as in FIG. 2 where the source 16 consists of a holder 18 made of tungsten crushed in the pump tip 17, at whose end facing the filament 7 the source material 19 is seated, namely a hydrocarbon which has been deposited as a solid.
- the sink is realized here by the lower part 21 of the power supply leads 22 close to the pinch.
- This part 21 consists of molybdenum, which serves as a catalyst in the decomposition of the hydrocarbons.
- the upper part 20 of the power supply is integrally formed by the carbide of the filament. The lower parts 21 protrude into the pinch.
- the luminous body 7 is located in the material flow, which forms from the source 16 to the sink 21.
- the lower part of the inner power supply 22 is made of molybdenum, referred to as Catalyst in the decomposition of hydrocarbons and thus acts as a sink.
- the consisting of TaC filament 23, see FIG. 3 is operated at a temperature between 3300 K and 3600 K.
- the carbon source 24 is maintained in the temperature range between 2700 K and 3000 K.
- Hydrogen is added to the inert gas (krypton, argon) in such a way that the partial pressure of the hydrogen in the range is preferably between 2 mbar H 2 and 20 mbar H 2 to avoid the deposition of the carbon on the piston wall and the transport of the carbon to the sink , In this case, no hydrogen is released from the source, so that no sink for hydrogen is needed.
- the carbon source is at such a high temperature that there is no direct reaction with the hydrogen.
- As a sink for decomposition of the hydrocarbon is, for example, again at 400 ° C - 800 ° C operated wires or plates made of nickel or iron or molybdenum, or at temperatures around 500 ° C operated aluminosilicate.
- FIG. 3 shows a possible geometry for such a lamp.
- C deposits in the "upper" region of the power supply lines 25 act near the transition region to the coil 23, where comparatively high temperatures already exist.
- carbon deposition on the outer turns of the luminescent body may also be expedient.
- the power supply is here an integral departure from the helix 23.
- C deposits C-fibers can be wound around the outlet.
- the sink 26 is here a coating coil made of iron, which is coated with platinum. It is near the pinch, so it is appropriate at much lower temperatures.
- FIG. 4 An example of a source disposed on the axis of the luminous element is in FIG FIG. 4 shown.
- the rod 27 has approximately the same temperature profile in the region of the helix 28 as the helix itself.
- the helix is wound to such an extent that the rod 27 fits into its axis without contact.
- the sink is again formed by coating helices 26, as in FIG FIG. 3 , They are made of molybdenum.
- the rod 27 is similar to a middle holder 9 as in FIG. 1 supported. He may in particular extend into a pump seats 29, see dashed embodiment. As a result, he is better locked.
- FIG. 5 shows a possible arrangement for a two-sided pinch lamp 30.
- the bruises are designated 39.
- the source 31 is a carbon deposit (soot) or a carbon fiber wound around the power supply 34.
- the sink 32 is the part of a power supply, which is made of molybdenum and is arranged away from the luminous body 33. This part is connected via a weld point 35 to the outlet 36 of the luminous body made of TaC.
- the entire temperature spectrum is available here on both sides of the luminous element 33 in the axial direction, so that, for example, the C source is arranged at relatively high temperatures in the vicinity of the luminous element and the drain at lower temperatures farther away from the luminous element on the other side can.
- the molybdenum outlet acts as a sink.
- a metal or a metal compound is suitable, whose melting point is in the vicinity of the melting point of tungsten, preferably at least 3000 ° C and more preferably above that of tungsten.
- tungsten, rhenium, osmium and tantalum are particularly suitable.
Abstract
Description
Die Erfindung geht aus von einer Glühlampe mit einem Leuchtkörper, der eine hochtemperaturbeständige Metallverbindung enthält, gemäß dem Oberbegriff des Anspruchs 1. Es handelt sich dabei insbesondere um Glühlampen mit einem carbidhaltigen Leuchtkörper, insbesondere betrifft die Erfindung Halogenglühlampen, die einen Leuchtkörper aus TaC aufweisen, oder dessen Leuchtkörper TaC als Bestandteil oder Beschichtung enthält.The invention relates to an incandescent lamp with a luminous body containing a high-temperature-resistant metal compound, according to the preamble of claim 1. It is in particular bulbs with a carbide-containing filament, in particular the invention relates to halogen incandescent lamps having a luminous body of TaC, or whose luminous body TaC contains as a component or coating.
Aus vielen Schriften ist eine Glühlampe mit einem Leuchtkörper, der eine hochtemperaturbeständige Metallverbindung enthält bekannt. Ein bisher noch ungelöstes Problem ist die stark einschränkte Lebensdauer. Eine in
Eine weit verbreitete Methode zur Lösung des Problems, ein Abdampfen von Material des Leuchtkörpers zu verhindern, besteht in der Verwendung von Kreisprozessen. Dabei wird dem Füllgas eine weitere chemische Substanz zugefügt, welche in kälteren Bereichen mit dem abgedampften Material zu einer relativ leicht flüchtigen Verbindung reagiert, welche sich nicht an der Kolbenwand abscheidet. Diese Verbindung wird im sich aufbauenden Konzentrationsgradienten - nämlich hohe Konzentration nahe der Kolbenwand, niedrige Konzentration nahe des Leuchtkörpers - in Richtung des Leuchtkörpers transportiert. Bei den hohen Temperaturen nahe des Leuchtkörpers zersetzt sie sich unter Zerfall in das Material des Leuchtkörpers und der zugegebenen chemischen Substanz; das Material des Leuchtkörpers wird wieder an diesen angelagert.A common method of solving the problem of preventing vaporization of filament material is by using circular processes. In this case, the filling gas, a further chemical substance is added, which reacts in colder areas with the evaporated material to a relatively volatile compound, which does not deposit on the bulb wall. This compound is transported in the build-up concentration gradient - namely high concentration near the bulb wall, low concentration near the filament - in the direction of the filament. At the high temperatures near the filament, it decomposes to decompose into the material of the filament and the added chemical substance; the material of the filament is attached to this again.
Das vom Leuchtkörper abdampfende Wolfram verbindet sich bei niedrigeren Temperaturen nahe der Kolbenwand zu Wolframhalogeniden, welche bei Temperaturen oberhalb ca. 200°C flüchtig sind und sich nicht an der Kolbenwand abscheiden. Dadurch wird ein Ausfall von Wolfram an der Kolbenwand verhindert. Die Wolframhalogenidverbindungen werden durch Diffusion und ggf. auch Konvektion zum heißen Leuchtkörper zurücktransportiert, wo sie sich zersetzen. Das dabei frei gewordene Wolfram wird wieder an den Leuchtkörper angelagert. Allerdings wird das Wolfram i.allg. nicht an dieselbe Stelle zurücktransportiert, von der es abgedampft ist, sondern an einer Stelle anderer Temperatur abgelagert, d.h. der Kreisprozess ist nicht regenerativ. Eine Ausnahme ist der Fluor-Kreisprozess.The tungsten evaporating from the filament combines at lower temperatures near the bulb wall to tungsten halides, which are volatile at temperatures above about 200 ° C and do not deposit on the bulb wall. This prevents a tungsten failure on the bulb wall. The tungsten halide compounds are transported back by diffusion and possibly also convection to the hot filament, where they decompose. The freed tungsten is again attached to the filament. However, the tungsten i.allg. not transported back to the same site from which it has evaporated, but deposited at a location of different temperature, i. the cycle is not regenerative. An exception is the fluorine cycle.
Der bei Zersetzung des TaC entstehende gasförmige Kohlenstoff wird in Richtung der Kolbenwand transportiert, wo er mit Wasserstoff zu Kohlenwasserstoffen wie Methan reagiert. Diese Kohlenwasserstoffe werden zum heißen Leuchtkörper zurück transportiert, wo sie sich wieder zersetzen. Der Kohlenstoff wird dabei wieder freigesetzt und kann sich an den Leuchtkörper anlagern. Allerdings zersetzen sich die Kohlenwasserstoffe bei niedrigen Temperaturen bereits unter 1000 K, so dass die Rückführung von Kohlenstoff nicht gezielt zu den heißesten Stellen des Leuchtkörpers erfolgt.The gaseous carbon formed upon decomposition of the TaC is transported towards the bulb wall, where it reacts with hydrogen to form hydrocarbons such as methane. These hydrocarbons are transported back to the hot filament, where they decompose again. The carbon is released again and can attach to the filament. However, at low temperatures, the hydrocarbons decompose below 1000 K, so that the return of carbon is not targeted to the hottest spots of the filament.
Wenn wie im zuletzt beschriebenen Beispiel die Abdampfung vom Leuchtkörper relativ stark ist und die den Kreisprozess tragende Verbindung nur bei sehr niedrigen Temperaturen stabil ist wie die Kohlenwasserstoffe im letzten Beispiel, so kommt es zu einer raschen Zerstörung des Leuchtkörpers, weil dieser schnell an dem abdampfenden Material wie Kohlenstoff im letzten Beispiel verarmt. Insgesamt wird der Kohlenstoff relativ schnell von den heißesten Stellen des Leuchtkörpers zu den kälteren Stellen des Leuchtkörpers bzw. den Abgängen zum Leuchtkörper transportiert, was ebenfalls z.B. durch Windungsschluss Probleme bereiten kann. Nur ein sehr geringer Anteil des zurücktransportierten Kohlenstoffs erreicht noch die heißeste Stelle der Wendel (sehr geringer Regenerationsgrad). Zudem verläuft die Rückreaktion des Kohlenstoffs mit dem Wasserstoff zu Kohlenwasserstoffen ohnehin nur bei einem relativ großen Wasserstoffüberschuss hinreichend schnell, so dass eine Schwärzung des Kolbens vermieden wird.If, as in the last-described example, the evaporation from the luminous element is relatively strong and the compound carrying the cyclic process is stable only at very low temperatures, such as the hydrocarbons in the last example, the luminous body will be rapidly destroyed, because it will rapidly attack the evaporating material like carbon impoverished in the last example. Overall, the carbon is relatively fast from the hottest points of the filament to the colder places of the filament or the outlets transported to the luminous body, which can also cause problems, for example by Windungsschluss. Only a very small proportion of the transported back carbon reaches the hottest point of the helix (very low degree of regeneration). In addition, the back reaction of the carbon with the hydrogen to hydrocarbons proceeds in any case only with a relatively large excess of hydrogen sufficiently fast, so that a blackening of the piston is avoided.
Zusammenfassend ist in solchen Fällen wie bei der TaC Lampe der Gebrauch eines Kreisprozesses, bei dem:
- (a) erstens das Material vom Leuchtkörper relativ schnell abdampft bzw. abtransportiert wird,
und - (b) zweitens das abgedampfte Material nur bei sehr niedrigen Temperaturen eine chemische Verbindung eingeht,
für viele Anwendungsfälle nicht ausreichend, weil wegen der nur sehr geringen Rückführung von Material zur den Stellen, von denen es abtransportiert wurde, der Leuchtkörper schnell zerstört wird.
- (a) firstly the material evaporates or is removed relatively quickly from the luminous element,
and - (b) second, that the evaporated material forms a chemical compound only at very low temperatures,
not sufficient for many applications, because because of the very low return of material to the bodies from which it was removed, the luminous body is destroyed quickly.
Als Möglichkeit zur Lösung des Problems wird in
Zusammenfassend ist ein stabiler Betrieb einer Lampe mit einem fortlaufend aus einem Depot ausdampfenden chemischen Verbindung nicht möglich, weil sich die Zusammensetzung der Gasphase und ggf. auch des Leuchtkörpers selber kontinuierlich ändern.In summary, a stable operation of a lamp with a continuously evaporating from a depot chemical compound is not possible because the composition of the gas phase and possibly also the filament itself change continuously.
Als weitere Möglichkeit wird im
Es ist Aufgabe der vorliegenden Erfindung, eine Glühlampe mit einem Leuchtkörper, der eine hochtemperaturbeständige Metallverbindung, und insbesondere einen carbidhaltigem Leuchtkörper, oder auch ein Metall enthält, gemäß dem Oberbegriff des Anspruchs 1 bereitzustellen, die eine lange Lebensdauer ermöglicht und das Problem der Verarmung des Leuchtkörpers an einer abdampfenden Komponente überwindet.It is an object of the present invention to provide an incandescent lamp with a luminous body, which contains a high-temperature-resistant metal compound, and in particular a carbide-containing luminous body, or even a metal, according to the preamble of claim 1, which allows a long life and the problem overcomes the depletion of the filament on a evaporating component.
Diese Aufgaben werden durch die kennzeichnenden Merkmale des Anspruchs 1 gelöst. Besonders vorteilhafte Ausgestaltungen finden sich in den abhängigen Ansprüchen.These objects are achieved by the characterizing features of claim 1. Particularly advantageous embodiments can be found in the dependent claims.
Der Begriff hochtemperaturbeständige Metallverbindung meint Verbindungen, deren Schmelzpunkt in der Nähe des Schmelzpunkts von Wolfram liegt, teilweise sogar darüber. Bevorzugt ist das Material des Leuchtkörpers TaC oder Ta2C. Aber auch Carbide des Hf, Nb oder Zr und überdies Legierungen dieser Carbide sind geeignet. Des weiteren Nitride oder Boride von derartigen Metallen. Diesen Verbindungen gemeinsam ist die Eigenschaft, dass ein Leuchtkörper aus diesem Material im Betrieb an mindestens einem Element verarmt. Das im folgenden beschriebene Prinzip ist aber genauso auch auf Leuchtkörper aus Metallen anwendbar. Der im folgenden verwendete Begriff Metallverbindung ist daher nicht einschränkend zu verstehen, sondern beispielhaft. Die darin getroffenen Aussagen sind analog auch auf Metalle anwendbar.The term high temperature resistant metal compound means compounds whose melting point is near the melting point of tungsten, sometimes even higher. The material of the luminous body is preferably TaC or Ta 2 C. However, carbides of Hf, Nb or Zr and, moreover, alloys of these carbides are suitable. Further, nitrides or borides of such metals. Common to these compounds is the property that a luminous body made of this material depletes in operation on at least one element. However, the principle described below is equally applicable to filaments of metals. The term metal compound used below is therefore not to be understood as limiting, but by way of example. The statements made therein are analogously applicable to metals.
Wird ein Leuchtkörper bei hohen Temperaturen betrieben, so kommt es - je nach der Beschaffenheit des Materials des Leuchtkörpers - zu einem Abdampfen von Material bzw. von Bestandteilen des Materials. Das abgedampfte Material bzw. seine Bestandteile werden durch z.B. Konvektion, Diffusion oder Thermodiffusion abtransportiert und scheiden sich an anderer Stelle in der Lampe ab, z.B. an der Kolbenwand oder Gestelltellen. Durch die Abdampfung des Materials bzw. seiner Bestandteile kommt es zu einer raschen Zerstörung des Leuchtkörpers. Durch das sich an der Kolbenwand abscheidende Material wird die Transmission des Lichtes stark reduziert.If a lamp is operated at high temperatures, it comes - depending on the nature of the material of the filament - to evaporate material or components of the material. The evaporated material or its constituents are replaced by e.g. Convection, diffusion or thermal diffusion removed and deposit elsewhere in the lamp, e.g. on the bulb wall or frames. The evaporation of the material or its components leads to a rapid destruction of the filament. Due to the material which separates on the bulb wall, the transmission of the light is greatly reduced.
- (a) Das von einer Glühwendel aus Wolfram abdampfende Wolfram wird bei einer konventionellen Glühlampe zur Kolbenwand transportiert und scheidet sich dort ab.(a) The tungsten evaporating from a tungsten filament is transported to the bulb wall in a conventional incandescent lamp and deposits there.
- (b) Ein bei hohen Temperaturen betriebener Tantalcarbidleuchtkörper zersetzt sich unter Entstehung des spröden, gegenüber TaC bei niedrigeren Temperaturen schmelzenden Subcarbids Ta2C und von gasförmigem Kohlenstoff, welcher zur Kolbenwand transportiert wird und sich dort abscheidet.(b) A tantalum carbide flare operated at high temperatures decomposes to form the brittle Ta 2 C subcarbide melting at lower temperatures relative to TaC and gaseous carbon which is transported to and settles to the flask wall.
Die Aufgabenstellung besteht darin, durch geeignete Maßnahmen ein Abdampfen vom Leuchtkörper zu minimieren bzw. rückgängig zu machen.The task is to minimize by appropriate measures evaporation from the lamp or to undo.
Um eine Verarmung des Leuchtkörpers an der abdampfenden Komponente zu vermeiden, wird von außen eine solche Konzentration der abdampfenden Komponente eingestellt, dass im Idealfall sich Abdampfung und Sublimation das Gleichgewicht halten und der Leuchtkörper somit an der fraglichen Komponente weder verarmt noch angereichert wird. Die Einstellung der benötigten Konzentration über dem Leuchtkörper soll durch einen kontinuierlichen Transport eines die fragliche Komponente enthaltenden Stoffes von einer Quelle in eine Senke realisiert werden. Durch die fortlaufende Abscheidung des aus der Quelle nachgelieferten Stoffes wird eine Veränderung der Zusammensetzung der Gasphase vermieden und ein Betrieb des Leuchtkörpers bei konstanten Bedingungen ermöglicht.In order to avoid a depletion of the filament on the evaporating component, such a concentration of the evaporating component is adjusted from the outside, that in the ideal case, evaporation and sublimation keep the balance and the filament is thus neither depleted nor enriched in the component in question. The adjustment of the required concentration over the luminous element is to be realized by a continuous transport of a substance containing the component in question from a source into a sink. The continuous deposition of the material supplied from the source avoids a change in the composition of the gas phase and enables operation of the luminous element under constant conditions.
Bei einer möglichen Auslegungsform einer Lampe mit TaC Leuchtkörper besteht die Quelle aus einem festen, oder auch flüssigen, Kohlenwasserstoff, welcher so in die Lampe eingebracht wird, dass sich über dem Quellenmaterial ein bestimmter Dampfdruck an gasförmigem Kohlenwasserstoff aufbaut. Dieser Kohlenwasserstoff wird durch Diffusion bzw. Konvektion in das Lampeninnere transportiert, wo er sich bei höheren Temperaturen nahe des Leuchtkörpers zersetzt. Der Leuchtkörper befindet sich somit in einer mit Kohlenstoff angereicherten Atmosphäre; eine Zersetzung des Leuchtkörpers wird dadurch verhindert. Im Idealfall gibt der Leuchtkörper dabei weder Kohlenstoff an die Umgebung ab, noch wird Kohlenstoff in ihm angereichert. Anders ausgedrückt stellt sich am Leuchtkörper ein Gleichgewicht zwischen Kohlenstoffabscheidung und Kohlenstoffverdampfung ein. Bei niedrigeren Temperaturen nahe der Kolbenwand reagiert der Kohlenstoff wieder mit Wasserstoff zu Kohlenwasserstoffen zurück. An einem bei geeigneter Temperatur angebrachten Draht z.B. aus einem der Materialien Eisen, Nickel, Kobalt, Platin oder Molybdän hinreichend großer Oberfläche zersetzt sich der Kohlenwasserstoff unter Abscheidung von festem Kohlenstoff (Ruß). Dieser Vorgang entspricht etwa dem aus der Technischen Chemie bekannten Cracken von Kohlenwasserstoffen an geeigneten Katalysatoren, wobei in diesem Fall - im Gegensatz zur Reaktionsführung in Anlagen der chemischen Industrie - die Abscheidung von Kohlenstoff am Katalysator erwünscht ist. Insgesamt tritt somit fortlaufend Kohlenstoff aus einer Quelle aus und wird in einer Senke wieder abgeschieden. Der Leuchtkörper der Lampe wird somit weder an Kohlenstoff angereichert, noch verarmt er an Kohlenstoff; außerdem wird die Kohlenstoffkonzentration in der Gasphase konstant gehalten.In one possible design of a lamp with TaC filament, the source of a solid, or liquid, hydrocarbon, which is introduced into the lamp so that builds up on the source material, a certain vapor pressure of gaseous hydrocarbon. This hydrocarbon is transported by diffusion or convection into the interior of the lamp, where it decomposes at higher temperatures near the filament. The luminous body is thus in a carbon-enriched atmosphere; a decomposition of the filament is thereby prevented. Ideally, the filament does not emit carbon to the environment, nor is carbon enriched in it. In other words, a balance between carbon deposition and carbon evaporation sets in the luminous body. At lower temperatures near the bulb wall, the carbon reacts again Back to hydrogen hydrocarbons. At a suitable temperature attached wire, for example, from one of the materials iron, nickel, cobalt, platinum or molybdenum sufficiently large surface, the hydrocarbon decomposes with deposition of solid carbon (soot). This process corresponds approximately to the cracking of hydrocarbons in suitable catalysts known from the technical chemistry, in which case - in contrast to the reaction regime in plants of the chemical industry - the deposition of carbon on the catalyst is desired. Overall, therefore, carbon continuously exits from one source and is re-deposited in a sink. The filament of the lamp is thus neither enriched in carbon, nor depleted of carbon; In addition, the carbon concentration in the gas phase is kept constant.
Mit dem Wasserstoff kann bevorzugt analog verfahren werden. Als Wasserstoffsenke wirkt die permeable Quarzkolbenwand bei hohen Temperaturen. Bei niedrigeren Temperaturen kann der entstehende Wasserstoff durch Jod abgefangen werden (Reaktion zu Jodwasserstoff; der dabei entstehende Jodwasserstoff ist hinsichtlich seiner Auswirkung auf die Maintenance der Lampe unkritisch, weil er weder in die Chemie des Metallkarbids eingreift noch die physikalischen Eigenschaften des Füllgases (insbesondere die Wärmeleitfähigkeit) ändert. Eine weitere Möglichkeit zur Bindung des freigesetzten Wasserstoffs (d.h. einer Senke für Wasserstoff) besteht im Gebrauch von Metallen wie z.B. Zirkonium oder Hafnium oder Niob oder Tantal, welche bei geeigneten Temperaturen Wasserstoff "gettern".The hydrogen can preferably be used analogously. As a hydrogen sink, the permeable quartz piston wall acts at high temperatures. At lower temperatures, the resulting hydrogen can be trapped by iodine (reaction to hydrogen iodide, the resulting hydrogen iodide is not critical to its effect on the maintenance of the lamp, because it does not interfere with the chemistry of the metal carbide nor the physical properties of the filler gas (especially the thermal conductivity Another way of attaching the released hydrogen (ie, a sink of hydrogen) is to use metals such as zirconium or hafnium or niobium or tantalum, which "getter" hydrogen at appropriate temperatures.
Es soll noch einmal darauf hingewiesen werden, dass die Existenz einer Senke für die Funktionsfähigkeit der Lampe wichtig ist. Beim Fehlen von Senken für Kohlenstoff und Wasserstoff würde sich entweder die Gasphase oder der Leuchtkörper an dem jeweiligen Element anreichern; die Folge davon wäre eine Veränderung der Betriebsdaten der Lampe.It should be pointed out again that the existence of a sink is important to the functionality of the lamp. In the absence of sinks for carbon and hydrogen, either the gas phase or the luminous body would accumulate on the respective element; the consequence of this would be a change in the operating data of the lamp.
Insbesondere können die in den letzten Absätzen beschriebenen Transportprozesse noch von einem oder mehreren Kreisprozessen überlagert werden.In particular, the transport processes described in the last paragraphs can still be superimposed by one or more cycle processes.
Wenn z.B. in einer Lampe mit einem Leuchtkörper aus TaC ständig Kohlenstoff - zum Teil in Form von Kohlenwasserstoffen - von einer Quelle zu einer Senke transportiert wird, so kann diesem Transportprozess durch Zusatz einer halogenhaltigen Verbindung ein Tantal-Halogen-Kreisprozess überlagert werden, welcher das vom Leuchtkörper abgedampfte Tantal an der Abscheidung an der Kolbenwand hindert und zumindest teilweise zum Leuchtkörper zurück transportiert, wie z.B. in der noch unveröffentlichten Anmeldung
Die als Senken dienenden Metalle können z.B. in Form von Drähten oder Plättchen an das Gestell bzw. die Stromzuführung angeschweißt werden, oder als Überzugswendel direkt um die Stromzuführung gewickelt werden, oder z.B. in Form von Drähten direkt mit eingequetscht werden. Wesentlich ist insbesondere bei der Verwendung von katalytisch wirkenden Metallen als Senken, dass die Oberfläche dieser Metalle hinreichend groß ist, da ja die Oberfläche fortlaufend mit Kohlenstoff belegt wird ("Vergiftung" des Katalysators), um die Wirksamkeit des Katalysators zu erhalten. Auch die Beschichtung von Wendelabgängen bzw. Stromzuführungen mit als Senke dienenden Metallen ist eine weitere Ausführungsform.The sinking metals may be e.g. in the form of wires or plates welded to the frame or the power supply, or wound as a coating coil directly around the power supply, or e.g. in the form of wires to be squeezed directly. It is essential in particular when using catalytically active metals as sinks that the surface of these metals is sufficiently large, since the surface is continuously covered with carbon ("poisoning" of the catalyst) in order to obtain the effectiveness of the catalyst. Also, the coating of Wendelabgängen or power supplies with serving as a sink metals is another embodiment.
In einer weiteren Ausführungsform wird als Quelle für Kohlenstoff elementarer Kohlenstoff verwandt. Dieser kann z.B. in Form von Kohlenstoffpresslingen, von Graphitfasern oder auf einem Substrat abgeschiedenem Russ, Diamant in Form von DLC oder Graphit vorliegen. Der Kohlenstoff wird auf einer "mittleren" Temperatur gehalten, die genau so groß sein muss, dass der resultierende Dampfdruck des Kohlenstoffs am Ort des heißen Leuchtkörpers zu einem Kohlenstoff-Partialdruck führt, welcher in etwa dem Kohlenstoff-Gleichgewichtsdampfdruck über dem Tantalkarbid entspricht. Damit halten sich am Leuchtkörper aus Tantalkarbid Kohlenstoffabscheidung und Kohlenstoffverdampfung das Gleichgewicht; eine Dekarburierung des Leuchtkörpers wird so vermieden. Gelangt der Kohlenstoff in kältere Bereiche nahe der Kolbenwand, so reagiert er mit Wasserstoff oder auch Halogenen zu (ggf. halogenierten) Kohlenwasserstoffen; dadurch wird die Abscheidung des Kohlenstoffs an der Kolbenwand verhindert. An einem Katalysator erfolgt dann die Zersetzung des Kohlenwasserstoffs, dabei scheidet sich der Kohlenstoff an der Oberfläche des Katalysators ab und der Wasserstoff wird wieder freigesetzt. In diesem Fall benötigt man keine Senke für den Wasserstoff bzw. ggf. das Halogen, welche ja nur die Abscheidung des Kohlenstoffs an der Kolbenwand verhindern und den in Form von Kohlenwasserstoff gebundenen Kohlenstoff zum Katalysator transportieren. Der Wasserstoff bzw. ggf. das Halogen dient somit hier lediglich als Transportmittel, um den Kohlenstoff zu transportieren und wird nicht verbraucht. Insgesamt wird in diesem Fall Kohlenstoff von der Kohlenstoffquelle (Kohlenstoffpressling, Graphitfasern, Diamant wie DLC, Graphitschichten, Ruß, etc.) zur Kohlenstoffsenke (z.B. Draht aus Nickel, Eisen, Molybdän) transportiert, wo er sich wieder abscheidet.In another embodiment, elemental carbon is used as the source of carbon. This may be present, for example, in the form of carbon compacts, graphite fibers or carbon black deposited on a substrate, diamond in the form of DLC or graphite. The carbon is maintained at a "medium" temperature, which must be just enough so that the resulting vapor pressure of the carbon at the location of the hot filament results in a carbon partial pressure which is approximately equal to the carbon equilibrium vapor pressure above the tantalum carbide. Thus keep the luminous body of tantalum carbide carbon deposition and carbon evaporation equilibrium; a Dekarburierung the filament is avoided. If the carbon reaches colder areas near the bulb wall, it reacts with hydrogen or halogens to (possibly halogenated) hydrocarbons; This prevents the deposition of carbon on the piston wall. The decomposition of the hydrocarbon then takes place on a catalyst, in which case the carbon deposits on the surface of the catalyst and the hydrogen is liberated again. In this case, you do not need a sink for the hydrogen or possibly the halogen, which indeed prevent only the deposition of the carbon on the piston wall and transport the bonded in the form of hydrocarbon carbon to the catalyst. The hydrogen or optionally the halogen thus serves only as a means of transport to transport the carbon and is not consumed. Overall, in this case, carbon is transported from the carbon source (carbon compact, graphite fibers, diamond such as DLC, graphite layers, carbon black, etc.) to the carbon sink (eg, nickel, iron, molybdenum wire) where it deposits again.
In einer Ausführungsform der Kohlenstoffquelle wird der Kohlenstoff auf einigen Windungen des als Wendel ausgeführten Leuchtkörpers aus Metallcarbid abgeschieden. Bevorzugt erfolgt die Kohlenstoffabscheidung auf den äußeren Windungen der Wendel bei niedrigeren Temperaturen als in der Mitte des Leuchtkörpers. Da der Dampfdruck über reinem Kohlenstoff größer ist als der Kohlenstoff-Dampfdruck über Tantalcarbid, wird die Quelle aus reinem Kohlenstoff bei niedrigeren Temperaturen als in der heißen Wendelmitte angebracht. Dadurch soll möglichst der Kohlenstoff-Gleichgewichtsdampfdruck über der Mitte der heißen Wendel eingestellt werden und erreicht werden, dass über den Leuchtkörper keine den Kohlenstoff-Transport treibenden Gradienten des Kohlenstoff-Partialdrucks entstehen.In one embodiment of the carbon source, the carbon is deposited on a few turns of the filament metal carbide filament. Preferably, the carbon deposition takes place on the outer turns of the coil at lower temperatures than in the middle of the filament. Since the vapor pressure over pure carbon is greater than the carbon vapor pressure over tantalum carbide, the source of pure carbon is attached at lower temperatures than the hot coil center. As a result, as far as possible the carbon equilibrium vapor pressure over the middle of the hot coil should be set and achieved that no carbon-transporting gradient of the carbon partial pressure is produced via the luminous body.
Die zuletzt beschriebene Vorgehensweise ist auch von Nutzen zur Umgehung von Problemen hinsichtlich der relativ geringen Stossfestigkeit des Tantalkarbids beim Transport der Lampen zum Kunden. Eine Option zur Umgehung dieses Problems besteht darin, die Karburierung erst nach dem Transport der Lampen zum Kunden beim Einbrennen abzuschließen und zunächst noch wenigstens einen Tantalkern im Leuchtkörper aus TaC zu belassen. Um die Karburierung beim Kunden dann abzuschließen, muss man beim Einbrennen der Lampe dem noch nicht vollständig durchkarburierten Leuchtkörper große Mengen an Kohlenstoff zuführen. Speichert man diese große Mengen Kohlenstoff in Form von gasförmigen Kohlenwasserstoffen in der Gasatmosphäre oder in Form von kontinuierlich verdampfenden festen Kohlenwasserstoffen, so werden bei der Karburierungsreaktion sehr große Mengen Wasserstoff freigesetzt, welche sich dann wegen der Erhöhung der Wärmeleitfähigkeit negativ auf die Effizienz der Lampe auswirken. Da die Reaktion mit dem Kohlenwasserstoff auch nicht vollständig verläuft, stellen die großen Mengen an freigesetztem Kohlenstoff, die in der Gasphase gehalten werden müssen, ebenfalls ein Problem dar. Dieses Problem lässt sich in der beschriebenen Weise umgehen, indem der noch nicht vollständig durchkarburierte Leuchtkörper sich in einem kontinuierlichen Strom eines von einer Kohlenstoffquelle ausgehenden Stroms von Kohlenstoff befindet. Der nicht zur Karburierung verwandte Kohlenstoff reagiert mit Wasserstoff zu Kohlenwasserstoffen, wodurch die Abscheidung des Kohlenstoffs an der Kolbenwand verhindert wird. Der Kohlenwasserstoff zersetzt sich schließlich wieder an einem Katalysator, wobei der nicht benötigte Kohlenstoff abgeschieden wird und der Wasserstoff freigesetzt wird. Dabei kommt man mit einer relativ geringen Menge Wasserstoff aus, weil dieser nicht verbraucht wird, sondern nur zum Transport des Kohlenstoffs zur Kohlenstoffsenke dient. Insbesondere bleibt die Menge an Wasserstoff dabei konstant und steigt nicht permanent während der Karburierung an. Ist bei hoher Kolbentemperatur, insbesondere bei einem Kolben aus Quarzglas, die Permeabilität des Wasserstoffs nicht mehr vernachlässigbar, kann der Wasserstoff durch den Gebrauch von Jod nahe der Kolbenwand wieder als Jodwasserstoff abgefangen und stabilisiert werden.The last described approach is also useful for circumventing problems related to the relatively low impact strength of the tantalum carbide during transport of the lamps to the customer. One option for circumventing this problem is to complete the carburization only after the lamps have been transported to the customer during the firing process and initially to leave at least one tantalum core in the TaC luminous element. In order to complete the carburization at the customer then, you have to perform the burning of the lamp not yet completely durchkarburierten luminous body large amounts of carbon. If you store these large amounts of carbon in the form of gaseous hydrocarbons in the gas atmosphere or in the form of continuously evaporating solid hydrocarbons, the carburization reaction very large amounts of hydrogen are released, which then have a negative effect on the efficiency of the lamp because of the increase in thermal conductivity. Also, because the reaction with the hydrocarbon is not complete, the large amounts of carbon released that must be held in the gas phase also present a problem. This problem can be overcome in the manner described by leaving the incompletely fully carburized luminescent body is located in a continuous stream of carbon from a source of carbon. The non-carburizing carbon reacts with hydrogen to form hydrocarbons, thereby preventing the deposition of carbon on the piston wall. The hydrocarbon eventually decomposes back to a catalyst, depositing the unneeded carbon and liberating the hydrogen. It comes with a relatively small amount of hydrogen, because it is not consumed, but only serves to transport the carbon to the carbon sink. In particular, the amount of hydrogen remains constant and does not increase permanently during carburization. If the permeability of the hydrogen can no longer be neglected at high piston temperature, in particular in the case of a quartz glass flask, then the hydrogen can be replaced by the hydrogen Use of iodine near the piston wall to be intercepted and stabilized as hydrogen iodide.
Eine weitere Möglichkeit zur Realisierung einer Kohlenstoffquelle besteht in der Verwendung einer mit Tantalkarbid beschichteten Kohlenstofffaser. Bei den hohen Betriebstemperaturen diffundiert der Kohlenstoff durch die Tantalkarbidschicht hindurch; eine Verarmung der Tantalkarbidschicht an Kohlenstoff wird damit vermieden. Der dadurch in den Gasraum freigesetzte Kohlenstoff führt jedoch zu einer raschen Schwärzung der Kolbenwand, wenn keine Gegenmaßnahmen ergriffen werden. Durch Abfangen des Kohlenstoffs mit Wasserstoff lässt sich bei nicht zu hohen Kolbentemperaturen eine Schwärzung des Kolbens verhindern. Allerdings werden sehr große Mengen an Wasserstoff benötigt, um den Kohlenstoff möglichst vollständig vor seiner Abscheidung auf der Kolbenwand "abzufangen". Dies lässt sich dadurch vermeiden, dass man den Kohlenwasserstoff an einem auf geeigneter Temperatur gehaltenen Katalysator, z.B. einem Draht aus Nickel, Eisen, usw. zersetzt. Dabei scheidet sich der Kohlenstoff am Nickeldraht ab, während der Wasserstoff wieder freigesetzt wird und zur Reaktion mit weiterem Kohlenstoff zur Verfügung steht. Der Wasserstoff dient somit lediglich als "Vehikel", um vom Leuchtkörper herantransportierten Kohlenstoff durch Bildung von Kohlenwasserstoff abzufangen und zur Kohlenstoffsenke (z.B. Draht aus Nickel, Molybdän, ...) zu transportieren. Insgesamt wird bei diesem Transportmechanismus kein Wasserstoff verbraucht, d.h. man kommt mit einer relativ geringen Menge an Wasserstoff aus. Würde man alternativ einen Kreisprozess implementieren, so müsste man sehr große Mengen an Wasserstoff verwenden, um den in großer Konzentration vom Leuchtkörper herantransportierten Kohlenstoff durch Bildung von Kohlenwasserstoffen abzufangen bzw. eine solch hohe Konzentration an Kohlenwasserstoffen nahe der Kolbenwand aufzubauen, dass der Rücktransport von Kohlenstoff zum Leuchtkörper den Abtransport genau ausgleicht. Bei Verwendung von so großen Mengen an Wasserstoff würde die Effizienz der Lampe stark zurückgehen. Als weitere Möglichkeit der Ausgestaltung einer Quelle bietet es sich an, den Leuchtkörper mit dem Material, an welchem er verarmt und das aus einer Quelle wieder zugeführt werden soll, zu beschichten und dann noch einmal eine Schicht des eigentlichen Leuchtkörper-Materials von außen auf diese Schicht aufzubringen. Besteht ein Leuchtkörper z.B. aus einem Metallcarbid wie Tantalcarbid oder Hafniumcarbid, so wird eine Schicht aus Kohlenstoff auf der Oberfläche des Leuchtkörpers aus Metallcarbid abgeschieden. Auf dieser Schicht aus Kohlenstoff wird dann noch einmal eine Schicht eines Metallcarbids aufgebracht. Verdampft im Lampenbetrieb Kohlenstoff von der äußeren Metallcarbid - Schicht, so diffundiert sofort Kohlenstoff von innen von der umschlossenen Kohlenstoff-Schicht nach und verhindert eine Verarmung der äußeren Metallcarbid-Schicht an Kohlenstoff. In dieser Hinsicht ist die Funktionsweise derjenigen einer mit Metallcarbid beschichteten Kohlenstoff-Faser recht ähnlich. Bei dieser Vorgehensweise ist jedoch von Vorteil, dass bei der Herstellung des Leuchtkörpers weitgehend auf im Halogenlampenbau etablierte Verfahrenstechnologie zurückgegriffen werden kann. Das Aufbringen der Kohlenstoff-Beschichtung erfolgt zum Beispiel gemäß einem CVD-Verfahren in der Stängellampe, z.B. durch Zersetzung von Methan (1 bar Druck) bei einer Temperatur von ca. 2.500 K am Leuchtkörper. Die Aufbringung der aus Metallcarbid bestehenden äußeren Schicht erfolgt beim CVD-Verfahren z.B. durch gleichzeitige thermische Zersetzung von Metallhalogeniden wie Tantalhalogenid und Methan; es ist natürlich auch die Verwendung von anderen Metallverbindungen bzw. Kohlenwasserstoffen als Precursor möglich. Durch Einstellung geeigneter stöchiometrischer Verhältnisse der Ausgangsverbindungen lässt sich dann das Metallcarbid direkt auf der Oberfläche des Leuchtkörpers abscheiden, z.B. gemäß TaCl5 + CH4 + x H2 -> TaC + 5 HCl + (x - ½) H2. Der Wasserstoff dient hier einer Vermeidung der Abscheidung von Ruß. Man kann auch nur das Metall auf der aus Kohlenstoff bestehenden Oberfläche des Leuchtkörpers abscheiden und dann erst in einer z.B. Methan enthaltenden Atmosphäre zur Reaktion (d.h. Carburierung) bringen, wobei von der äußeren Kohlenstoff enthaltenden Atmosphäre und von Innen von der Kohlenstoffschicht her die Carburierung einsetzt. Nachteilig bei diesem Verfahren ist jedoch, dass die bei der Umwandlung des Metalls in Metallcarbid auftretende Volumenänderung relativ große Schichtspannungen verursacht. Daher ist eine gleichzeitige Abscheidung des Metalls und des Kohlenstoffs im stöchiometrischen Verhältnis vorteilhaft.Another way to realize a carbon source is to use a tantalum carbide coated carbon fiber. At high operating temperatures, the carbon diffuses through the tantalum carbide layer; a depletion of the Tantalkarbidschicht of carbon is thus avoided. However, the carbon released thereby into the gas space leads to a rapid blackening of the piston wall, if no countermeasures are taken. By trapping the carbon with hydrogen, blackening of the bulb can be prevented if the bulb temperatures are not too high. However, very large amounts of hydrogen are needed to "catch" the carbon as completely as possible before its deposition on the bulb wall. This can be avoided by decomposing the hydrocarbon at a catalyst maintained at a suitable temperature, eg a wire of nickel, iron, etc. Here, the carbon is deposited on the nickel wire, while the hydrogen is released again and is available for reaction with more carbon available. Thus, the hydrogen serves only as a "vehicle" to intercept carbon transported by the luminous body by the formation of hydrocarbon and to transport it to the carbon sink (eg wire made of nickel, molybdenum, etc.). Overall, no hydrogen is consumed in this transport mechanism, ie it comes with a relatively small amount of hydrogen. If one would alternatively implement a cyclic process, one would have to use very large amounts of hydrogen in order to trap the transported in large concentration by the filament carbon by formation of hydrocarbons or build such a high concentration of hydrocarbons near the bulb wall that the return of carbon to the Luminous body exactly compensates for the removal. Using such large amounts of hydrogen would greatly reduce the efficiency of the lamp. As a further possibility of the embodiment of a source, it makes sense to coat the filament with the material to which it is depleted and which is to be supplied from a source again, and then again a layer of the actual filament material from the outside on this layer applied. If a luminous element eg consists of a metal carbide such as tantalum carbide or hafnium carbide, a layer of carbon is deposited on the surface of the filament of metal carbide. On this layer of carbon, a layer of a metal carbide is then applied again. When carbon from the outer metal carbide layer evaporates during lamp operation, carbon immediately diffuses from the inside of the enclosed carbon layer and prevents depletion of the outer metal carbide layer of carbon. In this regard, the operation is quite similar to that of a metal carbide coated carbon fiber. In this approach, however, is of advantage that in the manufacture of the luminous body can be used largely established in halogen lamp process technology. The application of the carbon coating is carried out, for example, according to a CVD method in the stud lamp, for example by decomposition of methane (1 bar pressure) at a temperature of about 2,500 K on the filament. The application of the metal carbide outer layer is carried out in the CVD method, for example, by simultaneous thermal decomposition of metal halides such as tantalum halide and methane; Of course, it is also possible to use other metal compounds or hydrocarbons as precursor. By setting suitable stoichiometric ratios of the starting compounds, the metal carbide can then be deposited directly on the surface of the luminous element, eg according to TaCl 5 + CH 4 + x H 2 -> TaC + 5 HCl + (x - ½) H 2 . The hydrogen serves here to avoid the deposition of soot. It is also possible to deposit only the metal on the carbon surface of the filament and then to react (ie carburize) in an atmosphere containing, for example, methane, carburizing from the outer carbon-containing atmosphere and from the inside from the carbon layer starts. A disadvantage of this method, however, is that the volume change occurring in the transformation of the metal into metal carbide causes relatively large layer stresses. Therefore, a simultaneous deposition of the metal and the carbon in the stoichiometric ratio is advantageous.
Im zuletzt genannten Ausführungsbeispiel müssen die Materialien des inneren Materials (z.B. Drahtes) aus Metallcarbid sowie der äußeren Schicht aus Metallcarbid nicht unbedingt identisch sein. Z.B. kann der innere Draht aus Tantalcarbid bestehen, während die äußere auf die Kohlenstoff-Schicht aufgebrachte Schicht aus Hafniumcarbid oder der Legierung HfC-4TaC besteht. Über HfC bzw. der Legierung HfC-4TaC herrschen geringere Dampfdrücke als etwa über reinem Tantalcarbid. Da jedoch Hafnium deutlich teurer ist als Tantal, lässt sich auf diese Weise die Menge des eingesetzten Hafniums deutlich reduzieren.In the latter embodiment, the materials of the inner material (e.g., wire) of metal carbide and the outer layer of metal carbide need not necessarily be identical. For example, For example, the inner wire may be tantalum carbide, while the outer layer applied to the carbon layer may be hafnium carbide or HfC-4TaC alloy. HfC or the alloy HfC-4TaC has lower vapor pressures than pure tantalum carbide. However, since hafnium is significantly more expensive than tantalum, the amount of hafnium used can be significantly reduced in this way.
Als eine weitere Quelle für Kohlenstoff kommen Sinterwerkstoffe mit Kohlenstoff in Betracht, wie z.B. in
Als weitere Optionen für Kohlenstoff- Senken kommen Metalle wie z.B. Wolfram, Tantal, Zirkonium etc. in Betracht, welche bei geeigneten Temperaturen Karbide bilden. Die Betriebstemperatur dieser Metalle richtet sich insbesondere nach dem vom Leuchtkörper kommenden Fluss an Kohlenstoff; üblich sind Temperaturen im Bereich zwischen 1800°C und 2500 °C. Bevorzugt wird beim Gebrauch dieser Metalle Wasserstoff eingesetzt, um den Kohlenstoff an einer Abscheidung an der Kolbenwand zu hindern und zur Kohlenstoff- Senke zu transportieren. Würde man auf den Wasserstoff verzichten, so würde vom Leuchtkörper herantransportierter Kohlenstoff sich - wenn er nicht auf seinem Weg vom Leuchtkörper zufällig auf das karbidbildende Metall trifft - auf der Kolbenwand abscheiden. Bei zusätzlichem Gebrauch von Wasserstoff reagiert der Kohlenstoff zunächst mit dem Wasserstoff zu einem Kohlenwasserstoff wie z.B. Methan, welches sich dann am karbidbildenden Metall wieder unter Übergang des Kohlenstoffs auf das karbidbildende Metall und Freisetzung des Wasserstoffs zersetzt .Further options for carbon sinks are metals such as tungsten, tantalum, zirconium, etc., which form carbides at suitable temperatures. The operating temperature of these metals depends in particular on the flow of carbon coming from the luminous element; Common temperatures are in the range between 1800 ° C and 2500 ° C. Hydrogen is preferably used in the use of these metals in order to prevent the carbon from being deposited on the bulb wall and to form carbon. Sink to transport. If one were to forego the hydrogen, then the carbon transported by the luminous body would - if it does not accidentally strike the carbide-forming metal on its way from the luminous body - deposit on the bulb wall. With additional use of hydrogen, the carbon first reacts with the hydrogen to form a hydrocarbon, such as methane, which then decomposes back to the carbide-forming metal to transfer the carbon to the carbide-forming metal and release the hydrogen.
Weitere mögliche Katalysatoren für die Zersetzung von Kohlenwasserstoffen sind Aluminium-, Molybdän- oder Magnesiumsilicate.Other possible catalysts for the decomposition of hydrocarbons are aluminum, molybdenum or magnesium silicates.
Als eine weitere Möglichkeit zur Verwendung als Kohlenstoffquelle kommt auch die Verwendung von Tantalkarbid bzw. anderer Karbide in Betracht. Bringt man etwa einen nicht vom Strom durchflossenen Stab aus Tantalkarbid auf eine dem Leuchtkörper entsprechende Temperatur, so stellt sich über dem Tantalkarbid gerade der geeignete Gleichgewichts-Dampfdruck an Kohlenstoff ein, bei dem am Leuchtkörper keine Verdampfung oder Abscheidung von Kohlenstoff mehr erfolgt. Dies lässt sich z.B. realisieren, indem man einen Stab / Draht aus Tantalkarbid im Inneren auf der Achse einer Wendel aus Tantalkarbid einbringt (analog einer Wendel mit Innenrückführung, wie sie für IRC- Lampen verwandt wird, wobei bei den Metallkarbid- Lampen aber der Draht auf der Wendelachse nicht vom Strom durchflossen wird), wobei die Windungen der stromführenden aus TaC Draht bestehenden Wendel den nicht stromführenden Stab aus TaC nicht berühren dürfen, um einen Kurzschluss zu vermeiden. Der Stab muss sich auf praktisch derselben Temperatur befinden wie die benachbarten Windungen. Er darf auf keinen Fall deutlich kälter sein als die benachbarten Windungen, d.h. die Wärmeableitung längs des Stabs muss - z.B. durch Wahl eines hinreichend kleinen Durchmessers - begrenzt werden. Über dem Stab stellt sich ein Gleichgewichtsdampfdruck an Kohlenstoff ein. Der Kohlenstoff wird im radial nach außen gerichteten Konzentrationsgradienten an den stromführenden TaC Wendeln vorbei zur Kolbenwand transportiert. Die einzelnen Windungen der TaC- Wendel befinden sich damit in einem ständigen Strom aus Kohlenstoff, wobei der Kohlenstoff-Partialdruck dem Gleichgewichtsdruck über den Wendeln entspricht. Der nach außen transportierte Kohlenstoff reagiert nahe der Kolbenwand wieder mit Wasserstoff zu Kohlenwasserstoffen, welche sich dann an einem geeigneten Katalysator wie oben beschrieben unter Abscheidung von Kohlenstoff und Freisetzung von Wasserstoff zersetzen. Insgesamt wird somit Kohlenstoff vom auf der Achse der Wendel befindlichen Stab aus TaC an den Windungen der TaC Wendel vorbei zur Kohlenstoff-Senke transportiert, wobei der Kohlenstoff-Partialdruck etwa dem Kohlenstoff-Gleichgewichtsdruck an den einzelnen Windungen entspricht und die aus TaC bestehenden Windungen somit stabilisiert werden. Anders ausgedrückt wird der von den einzelnen Windungen der TaC Wendel abdampfende und nach außen transportierte Kohlenstoff von innen her durch von dem vom TaC- Stab abdampfenden Kohlenstoff ersetzt. Der Vorteil einer Verwendung eines Stabes aus TaC gegenüber der Verwendung eines Stabes z.B. aus reinem Kohlenstoff liegt darin, dass bei derselben Temperatur der Kohlenstoff-Dampfdruck über reinem Kohlenstoff um Größenordnungen höher liegt als derjenige über Tantalkarbid, somit würde man in diesem Fall eine unnötig starken Kohlenstofftransport erzeugen und zum Teil sogar Kohlenstoff an der TaC Wendel abscheiden. Der Vorteil der Verwendung eines TaC Stabes auf der Wendelachse, dessen Temperaturprofil möglichst genau demjenigen der Wendel entspricht, besteht darin, dass sich dann an den einzelnen Windungen der TaC Wendel automatisch die Kohlenstoff- Gleichgewichtsdrücke, welche eine Zersetzung des Leuchtkörpers verhindern, einstellen.Another possibility for use as carbon source is the use of tantalum carbide or other carbides. If, for example, a rod of tantalum carbide not flowed through by the current is brought to a temperature corresponding to the luminous element, then the suitable equilibrium vapor pressure of carbon is established above the tantalum carbide, in which vaporization or deposition of carbon no longer takes place on the luminous element. This can be achieved, for example, by introducing a rod / wire made of tantalum carbide inside on the axis of a spiral of tantalum carbide (analogous to a coil with internal feedback, as it is used for IRC lamps, in the case of the metal carbide but the wire on the coil axis is not traversed by the current), wherein the turns of the current-carrying TaC wire coil must not touch the non-current rod made of TaC to avoid a short circuit. The rod must be at virtually the same temperature as the adjacent turns. It must under no circumstances be significantly colder than the adjacent windings, ie the heat dissipation along the rod must be limited - for example, by choosing a sufficiently small diameter. Above the rod, an equilibrium vapor pressure of carbon is established. The carbon becomes in the radially outward concentration gradient at the current carrying TaC Wendeln transported over to the piston wall. The individual turns of the TaC helix are therefore in a constant stream of carbon, with the carbon partial pressure corresponding to the equilibrium pressure across the helices. The carbon transported to the outside reacts again with hydrogen near the bulb wall to form hydrocarbons, which then decompose on a suitable catalyst as described above, with deposition of carbon and liberation of hydrogen. Overall, therefore, carbon is transported from the rod of TaC on the axis of the helix past the turns of the TaC helix to the carbon sink, the carbon partial pressure approximately corresponding to the carbon equilibrium pressure at the individual windings and thus stabilizing the turns made of TaC become. In other words, the carbon which evaporates from the individual turns of the TaC helix and is transported outwards is replaced from the inside by the carbon which evaporates from the TaC rod. The advantage of using a rod of TaC over the use of a rod of pure carbon, for example, is that at the same temperature the carbon vapor pressure over pure carbon is orders of magnitude higher than that over tantalum carbide, thus unnecessarily high carbon transport would be required produce and sometimes even deposit carbon on the TaC helix. The advantage of using a TaC rod on the helix axis whose temperature profile corresponds as closely as possible to that of the helix is that the carbon equilibrium pressures, which prevent decomposition of the luminous body, are then automatically adjusted at the individual turns of the TaC helix.
Als Quelle für Kohlenstoff kommen neben dem Kohlenstoff selber und Kohlenstoff-Wasserstoff Verbindungen auch Verbindungen des Kohlenstoffs mit anderen Elementen in Betracht.As a source of carbon in addition to the carbon itself and carbon-hydrogen compounds and compounds of carbon with other elements into consideration.
Vorteilhaft können z.B. Kohlenstoff und Fluor enthaltende Polymere verwandt werden, wie sie z.B. bei der Polymerisation von Tetrafluorethylen C2F4 entstehen (z.B. Polytetrafluorethylen PTFE, Markenname "Teflon" bei der Fa. DUPONT). Bei der Zersetzung dieser Verbindungen entstehen in der Gasphase Verbindungen wie z.B. CF4, C2F4, usw. welche sich erst bei höchsten Temperaturen nahe des Leuchtkörpers zersetzen und dabei Kohlenstoff und Fluor freisetzen. Von Vorteil ist dabei, dass der Kohlenstoff besonders bzw. praktisch ausschließlich an Stellen hoher Temperatur freigesetzt wird. Der Kohlenstoff wird somit gezielt zu Stellen hoher Leuchtkörpertemperatur transportiert. Wegen des gezielten Rückflusses zu Stellen höherer Temperatur kann hier mit relativ geringen Flüssen an Kohlenstoff bzw. relativ geringen Partialdrücken an gasförmigen C-F-Verbindungen gearbeitet werden. Das freigesetzte Fluor reagiert an der Wand zu gasförmigem SiF4, welches dann aber kaum noch in das Reaktionsgeschehen eingreift und sich auch nicht - wie etwa Wasserstoff - wegen erhöhter Wärmeleitung negativ auf die Effizienz der Lampe auswirkt. Der dabei freigesetzte Kohlenstoff kann wieder - sofern er nicht in der Wandreaktion unter CO-Bildung aufgebraucht wird - mittels eines Transportpartners wie z.B. Chlor in kälteren Bereichen zunächst gebunden und dann an einem heißen Metalldraht wieder zersetzt werden, wobei der Kohlenstoff sich wieder abscheidet und das Chlor freigesetzt wird (Kohlenstoff-Senke). Da in der Wandreaktion zwei F-Atome ein O-Atom freisetzen und im Polytetrafluorethylen in etwa auf zwei F-Atome ein C-Atom kommt, wird der Kohlenstoff weitgehend mit dem in der Wandreaktion freigesetzten Sauerstoff zu CO umgesetzt.Advantageously, for example, carbon and fluorine-containing polymers can be used, as they arise, for example, in the polymerization of tetrafluoroethylene C 2 F 4 (eg polytetrafluoroethylene PTFE, brand name "Teflon" at the company DUPONT). In the decomposition of these compounds are formed in the gas phase compounds such as CF 4 , C 2 F 4 , etc. which decompose only at very high temperatures near the filament and thereby release carbon and fluorine. The advantage here is that the carbon is released especially or practically exclusively at high temperature sites. The carbon is thus transported specifically to locations of high luminous body temperature. Because of the targeted reflux to higher temperature sites can be used here with relatively low flows of carbon or relatively low partial pressures of gaseous CF compounds. The liberated fluorine reacts on the wall to form gaseous SiF 4 , which then scarcely intervenes in the reaction process and also does not have a negative effect on the efficiency of the lamp, such as hydrogen, because of increased heat conduction. The released carbon can again - unless it is used up in the wall reaction with CO formation - first bound by a transport partner such as chlorine in colder areas and then decomposed on a hot metal wire, the carbon is deposited again and the chlorine is released (carbon sink). Since in the wall reaction two F atoms release an O atom and in polytetrafluoroethylene in about two F atoms a C atom comes, the carbon is largely reacted with the liberated in the wall reaction oxygen to CO.
Die vorliegende Erfindung eignet sich insbesondere für Niedervoltlampen mit einer Spannung von höchstens 50 V, weil die dafür notwendigen Leuchtkörper relativ massiv ausgeführt sein können und dafür die Drähte bevorzugt einen Durchmesser zwischen 50 µm und 300 µm, insbesondere höchstens 150 µm für Allgemeinbeleuchtungszwecke mit maximaler Leistung von 100 W, aufweisen. Dicke Drähte bis 300 µm werden insbesondere bei fotooptischen Anwendungen bis zu einer Leistung von 1000 W gebraucht. Besonders bevorzugt wird die Erfindung für einseitig gequetschte Lampen verwendet, da hier der Leuchtkörper relativ kurz gehalten werden kann, was die Bruchanfälligkeit ebenfalls reduziert. Aber auch die Anwendung auf zweiseitig gequetschte Lampen und Lampen für Netzspannungsbetrieb ist möglich.The present invention is particularly suitable for low-voltage lamps with a voltage of at most 50 V, because the necessary filament can be made relatively solid and for the wires preferably a diameter between 50 microns and 300 microns, especially at most 150 microns for general lighting purposes with maximum power of 100 W, exhibit. Thick wires up to 300 μm are used in particular for photo-optical applications up to a power of 1000 W. Particularly preferably, the invention is used for one-sided squeezed lamps, since the luminous body can be kept relatively short, which also reduces the susceptibility to breakage. But the application to double-sided squeezed lamps and lamps for mains voltage operation is possible.
Der Begriff Stab, wie er hier verwendet wird, meint ein Mittel, das als massiver Stab oder insbesondere als ein dünner Draht ausgebildet ist.The term rod as used herein means a means formed as a solid rod or, in particular, a thin wire.
Das beschriebene Konzept lässt sich in vielfältiger Weise auf spezielle chemische Transportsysteme anwenden. In einer speziellen Ausführungsform wird es für eine Auslegung eines Kohlenstoff-Schwefel-Kreisprozesses benutzt. Wie in DE Az 10358262.2 beschrieben zerfällt CS erst bei Temperaturen deutlich oberhalb 3000 K, wobei der Dissoziationsgrad des CS mit steigender Temperatur stark zunimmt. Damit eignet sich der C-S-Kreisprozess dazu, den Kohlenstoff zur heißesten Stelle längs der Wendel zurück zu transportieren und damit die Ausbildung von "Hot-Spots" zu verlangsamen bzw. zu verhindern. Bei Verwendung dieses C-S-Systems ist nun zu berücksichtigen, dass die den Kohlenstoff im Hochtemperaturbereich transportierende Verbindung CS bei Temperaturen ca. unterhalb 2200 K disproportioniert gemäß 2 CS -> CS2 + C, wobei Kohlenstoff am Gestell bzw. an den Wendelabgängen abgeschieden wird. Wird andererseits CS2 durch Diffusion bzw. durch die Strömung wieder zu Orten höherer Temperatur hin transportiert, so zersetzt es sich bei T > 2200 K in CS und Schwefel, wobei der Schwefel decarburierend auf den Metallcarbid-Leuchtkörper einwirkt. Daher ist es vorteilhaft, den Leuchtkörper bzw. dessen Abgänge im Bereich oberhalb 2200 K mit einer Kohlenstoff-Schicht zu überziehen. Die in diesem Temperaturbereich freiwerdenden Schwefel-Atome reagieren dann mit dem Kohlenstoff zu CS; eine Decarburierung des Metallcarbid-Leuchtkörpers wird vermieden. Im Laufe der Lebensdauer wird diese Kohlenstoff-Beschichtung langsam aufgebraucht. Andererseits wird bei niedrigeren Temperaturen unterhalb ca. 2200 K bei der Disproportionierung des CS Kohlenstoff freigesetzt und abgeschieden. Zusammenfassend wird somit durch das CS-System der Kohlenstoff von Orten höherer Temperatur mit T > 2200K zu Orten niederer Temperatur mit T < 2200 K transportiert. Ohne das Reservoir an Kohlenstoff für T > 2200 K (Quelle) bzw. die Abscheidung von Kohlenstoff bei T < 2200 K (Senke) lassen sich nur schwer stationäre Betriebsbedingungen erreichen.The described concept can be applied in a variety of ways to special chemical transport systems. In a specific embodiment, it is used for a design of a carbon-sulfur cycle. As described in DE Az 10358262.2 CS decomposes only at temperatures well above 3000 K, the degree of dissociation of CS increases strongly with increasing temperature. Thus, the CS cycle process is suitable for transporting the carbon back to the hottest point along the helix, thus slowing down or preventing the formation of "hot spots". When using this CS system, it should now be taken into consideration that the compound CS transporting the carbon in the high-temperature region is disproportionated at temperatures below about 2200 K according to 2 CS -> CS 2 + C, whereby carbon is deposited on the frame or on the helical outlets. If, on the other hand, CS 2 is transported back to higher temperature sites by diffusion or through the flow, it decomposes into CS and sulfur at T> 2200 K, the sulfur acting in a decarburizing manner on the metal carbide luminous body. Therefore, it is advantageous to coat the filament or its outlets in the range above 2200 K with a carbon layer. The sulfur atoms liberated in this temperature range then react with the carbon to CS; a decarburization of the metal carbide filament is avoided. Over the life of this carbon coating is used up slowly. On the other hand, carbon is released and deposited at lower temperatures below about 2200 K in the disproportionation of the CS. In summary, the CS system thus transports the carbon from places of higher temperature with T> 2200K to places of lower temperature with T <2200 K. Without the reservoir of carbon for T> 2200 K (source) or the deposition of carbon at T <2200 K (sink), it is difficult to achieve stationary operating conditions.
Die hier beschriebene Methodik lässt sich auch auf Glühkörper aus anderen Materialien als Metallcarbide, -boride oder-nitride anwenden. Als Beispiel wird im folgenden eine Anwendung auf reine Metalle wie Wolfram beschrieben. Zur Erzeugung eines die Lebensdauer verlängernden regenerativen Kreisprozesses, bei dem "Hot-Spots" am Leuchtkörper ausgeheilt werden, wird in der Literatur der Fluor-Kreisprozess beschrieben, vgl. z.B. (a)
Das hier beschriebene Grundprinzip - der kontinuierliche Transport eines Stoffes von einer Quelle in eine Senke - lässt sich in zwei weiteren Ausführungsbeispielen, die nicht Teil der Erfindung sind, sondern Beispiele, die lediglich das Verständnis der Erfindung erleichtern sollen, auch auf das Transportmittel anwenden, welches zum Klarhalten des Kolbens sowie der Rückführung von Material zum Leuchtkörper benutzt wird. Hier kann die Situation eintreten, dass entweder laufend das Transportmittel durch Reaktion oder Absorption mit Teilen des Gestells oder der Kolbenwand der Gasphase entzogen wird (Senke), oder dass es laufend durch Desorption oder chemische Reaktion in die Gasphase eingebracht wird (Quelle). Um stationäre Verhältnisse in der Gasphase zu erreichen, empfiehlt es sich daher in einem solchen Fall; beim Auftreten einer Senke zusätzlich eine Quelle und beim Auftreten einer Quelle zusätzlich eine Senke in die Lampe einzubringen.The basic principle described here - the continuous transport of a substance from a source into a sink - can be applied in two other embodiments, which are not part of the invention, but also examples, which are only to facilitate the understanding of the invention, on the means of transport is used to keep the piston clear as well as the return of material to the filament. Here, the situation may arise that either the transport means is continuously removed by reaction or absorption with parts of the frame or the piston wall of the gas phase (sink), or that it is continuously introduced by desorption or chemical reaction in the gas phase (source). In order to achieve stationary conditions in the gas phase, it is therefore recommended in such a case; in addition, when a sink occurs, a source and, in the event of a source, an additional sink in the lamp.
Als erstes lediglich das Verständnis der Erfindung erleichterndes Beispiel wird der kontinuierliche Transport von Wasserstoff von einer Quelle in eine Senke behandelt. Als Quelle für Wasserstoff können dienen im Leuchtkörper (Metallcarbid) eingelagerter Wasserstoff, in den Zuleitungen oder Getter aufgenommener Wasserstoff (evtl. gebunden als Metallhydrid wie z.B. Tantalhydrid). Bei der Aufkohlung kann über den Wasserstoff-Partialdruck und die Temperaturverteilung im Leuchtkörper und den Zuleitungen gezielt Wasserstoff in der Stängellampe angereichert werden. Im Lampenbetrieb herrschen andere Temperaturverteilungen als beim Aufkohlen. Typischerweise ist die Leuchtkörpertemperatur im Lampenbetrieb mit ca. 3300 K - 3600 K höher als beim Aufkohlen (2800 K - 3100 K); außerdem können beim Aufkohlen höhere Wasserstoff-Partialdrücke eingesetzt werden. Daher können beim Aufkohlen auf geeigneter Temperatur sich befindende Teile des Gestells z.B. aus Tantal oder Niob Wasserstoff aufnehmen. Später im Lampenbetrieb befinden sich diese Gestellteile auf höherer Temperatur in einer Atmosphäre, die weniger Wasserstoff enthält, und geben daher Wasserstoff ab (Quelle). Auf deutlich niedrigerer Temperatur sich befindende Teile des Gestells nehmen diesen Wasserstoff auf (Senke). Z.B. bei Lampen mit TaC-Leuchtkörper mit integralen Wendelabgängen (ähnlich wie in
Das zweite lediglich das Verständnis der Erfindung erleichternde Beispiel bezieht sich auf den Einsatz von Schwefel in einer Lampe mit Metallcarbid-Leuchtkörper sowie einer integralen Auslegung von Wendel und Wendelabgängen, d.h. Wendel und Wendelabgänge werden integral aus einem Tantaldraht gefertigt und dann der Leuchtkörper carburiert. Bei der Carburierung werden die Wendelabgänge nicht komplett mitcarburiert, d.h. hier findet man Tantal bzw. Tantalsubcarbid Ta2C. In diesem Bereich niedrigerer Temperaturen wird in der Lampe befindlicher Schwefel zu der sehr stabilen Verbindung Tantalsulfid umgesetzt und der Schwefel somit der Gasphase entzogen (Senke). Der der Gasphase entzogene Schwefel muss ständig nachgeliefert werden (Quelle), um einen C-S-Kreisprozess aufrecht zu erhalten. Dies kann z.B. durch permanente Ausdampfung von CH3CSCH3 aus einem damit getränktem (z.B. aus Gummi bestehenden) Reservoir geschehen. Bei Lampen mit extrem niedrigen Kolbentemperaturen unter ca. 100°C kann elementarer Schwefel als Quelle dienen, der bereits bei niederen Temperaturen einen beträchtlichen Dampfdruck aufweist und etwas oberhalb 100°C schmilzt. Auch der Einsatz von höher schmelzenden hochmolekularen Mercaptanen als Schwefel-Quelle ist möglich.The second example merely facilitating the understanding of the invention relates to the use of sulfur in a lamp with metal carbide filament and an integral design of helix and Wendelabgängen, ie helical and Wendelabgänge are integrally made of a tantalum wire and then the filament carburized. When carburizing the helical outlets are not completely mitcarburiert, ie here you will find tantalum or Tantalsubcarbid Ta2C. In this range of lower temperatures, sulfur in the lamp is converted to the very stable compound tantalum sulfide and the sulfur is thus removed from the gas phase (sink). The gas withdrawn from the gas phase must be constantly replenished (source) in order to maintain a CS cycle process. This can be done, for example, by permanent evaporation of CH3CSCH3 from a reservoir impregnated therewith (eg made of rubber). For lamps with extremely low bulb temperatures below about 100 ° C elemental sulfur can serve as a source, which already at low temperatures has a considerable vapor pressure and melts slightly above 100 ° C. The use of higher melting high molecular weight mercaptans as a sulfur source is also possible.
Im folgenden soll die Erfindung anhand mehrerer Ausführungsbeispiele näher erläutert werden. Es zeigen:
- Figur 1
- eine Glühlampe mit Carbid-Leuchtkörper gemäß einem Ausführungs- beispiel;
Figur 2- eine Glühlampe mit Carbid-Leuchtkörper gemäß einem zweiten Aus- führungsbeispiel;
Figur 3bis 5- eine Glühlampe mit Carbid-Leuchtkörper gemäß weiteren Ausfüh- rungsbeispielen.
- FIG. 1
- an incandescent lamp with carbide filament according to an embodiment;
- FIG. 2
- an incandescent lamp with carbide filament according to a second embodiment;
- FIGS. 3 to 5
- an incandescent lamp with carbide filament according to further embodiments.
Die hier beschriebene Bauform lässt sich beispielsweise auch auf Lampen mit Leuchtkörpern anderer Metallkarbide, z.B. Hafniumkarbid, Zirkoniumkarbid, Niobkarbid, übertragen. Auch die Verwendung von Legierungen verschiedener Carbide ist möglich. Außerdem ist die Verwendung von Boriden oder Nitriden, insbesondere von Rheniumnitrid oder Osmiumborid, möglich.The design described here can also be applied, for example, to lamps with luminous bodies of other metal carbides, e.g. Hafnium carbide, zirconium carbide, niobium carbide, transferred. The use of alloys of different carbides is possible. In addition, the use of borides or nitrides, in particular of rhenium nitride or osmium boride, is possible.
Im allgemeinen verwendet die Lampe bevorzugt einen Leuchtkörper aus Tantalcarbid, der bevorzugt aus einem einfach gewendelten Draht besteht. Als Leuchtkörpermaterial, der bevorzugt ein gewendelter Draht ist, eignet sich bevorzugt auch Zirkoniumkarbid, Hafniumkarbid, oder eine Legierung verschiedener Karbide wie z.B. in
Der Kolben ist typisch aus Quarzglas oder Hartglas mit einem Kolbendurchmesser zwischen 5 mm und 35 mm, bevorzugt zwischen 8 mm und 15 mm, gefertigt.The piston is typically made of quartz glass or hard glass with a piston diameter between 5 mm and 35 mm, preferably between 8 mm and 15 mm.
Die Füllung ist hauptsächlich Inertgas, insbesondere Edelgas wie Ar, Kr oder Xe, ggf. unter Beimengung geringer Mengen (bis 15 mol-%) Stickstoff. Dazu kommt typisch ein Kohlenwasserstoff, Wasserstoff und ein Halogenzusatz.The filling is mainly inert gas, in particular noble gas such as Ar, Kr or Xe, possibly with the addition of small amounts (up to 15 mol%) of nitrogen. This is typically a hydrocarbon, hydrogen and a halogen additive.
Ein Halogenzusatz ist unabhängig von möglichen Kohlenstoff-Halogen-Kreisprozessen bzw. Transportprozessen zweckmäßig, um vom Leuchtkörper aus Metallkarbid abgedampfte Metalle an der Abscheidung an der Kolbenwand zu hindern und möglichst zum Leuchtkörper zurück zu transportieren. Hier handelt es sich um einen Metall-Halogen-Kreisprozess wie z.B. in der Anmeldung
Konkrete Ausführungsbeispiele, die das Wesen der Erfindung näher erläutern, werden im folgenden dargelegt.Concrete embodiments that illustrate the essence of the invention are set forth below.
Von den aliphatischen Kohlenwasserstoffen kommen in der Regel wegen des sonst zu niedrigen Schmelzpunktes nur hochmolekulare Verbindungen in Frage (z.B. liegt der Schmelzpunkt von C56H114 nur bei knapp unter 100°C, was für die meisten Anwendungen zu wenig ist; es sei denn, der Einsatz von flüssigen Verbindungen ist möglich). Geeigneter sind aromatische Kohlenwasserstoffe wie z.B. Anthracen (Schmelzpunkt 216°C), Naphthacen (Schmelzpunkt 355°C), Coronen (Schmelzpunkt 440°C), die zudem noch den Vorteil haben, dass pro C-Atom erheblich weniger Wasserstoff in die Lampe eingetragen wird. Z.B. liegt der Dampfdruck von Anthracen knapp unterhalb des Schmelzpunktes um 50 mbar, bei 145 °C etwas oberhalb 1 mbar. Durch Lokalisierung der Quelle in einem Bereich geeigneter Temperatur kann man einen geeigneten Dampfdruck einstellen. Der Dampfdruck des Kohlenwasserstoffs muss etwa so eingestellt werden, dass die sich nach seinem vollständigen Zerfall einstellende molare Konzentration an C-Atomen am TaC Leuchtkörper in der Größenordnung der Gleichgewichtskonzentration an C-Atomen über dem Leuchtkörper liegt; der genaue Wert hängt von Details ab (z.B. Abstand der C-Quelle zum Leuchtkörper und zur Senke, Zerfallsgeschwindigkeit der Kohlenwasserstoffe an der Senke, usw.). Bei Verwendung von Anthracen als Quelle für Kohlenstoff liegt die geeignete Temperatur für die Quelle im Bereich zwischen 120°C und 150°C, wenn der Abstand zwischen dem auf z.B. 3400 K befindlichen Leuchtkörper und der Quelle ca. 3 cm beträgt und die Abscheidung des Kohlenstoffs nach Zersetzung der Kohlenwasserstoffe an einem bei etwa 400°C - 800°C heißen Nickeldraht erfolgt. Der Kaltfülldruck in einer solchen Lampe liegt im Bereich um 1 bar; das Inertgas (z.B. Argon, Krypton) enthält bevorzugt 2 mbar - 20 mbar Wasserstoff H2, 0,5 mbar CH2Br2 und 2 mbar - 20 mbar Jod. Durch das Brom soll die Abscheidung von Tantal am Kolben verhindert werden (siehe DE-Az 103 56 651.1), und durch das Jod soll der im Laufe der Verdampfung und Zersetzung des Anthracens freiwerdende Wasserstoff in Form von HJ gebunden werden. HJ stellt hier eine Senke für den freiwerdenden Wasserstoff dar.Of the aliphatic hydrocarbons are usually due to the otherwise low melting point only high molecular weight compounds in question (eg, the melting point of C 56 H 114 only just below 100 ° C, which is too little for most applications, unless the use of liquid compounds is possible). More suitable are aromatic hydrocarbons such as anthracene (melting point 216 ° C), naphthacene (melting point 355 ° C), corons (melting point 440 ° C), which also have the advantage that significantly less hydrogen is introduced into the lamp per carbon atom , For example, the vapor pressure of anthracene is just below the melting point by 50 mbar, at 145 ° C just above 1 mbar. By locating the source in a range of suitable temperatures, one can set a suitable vapor pressure. The vapor pressure of the hydrocarbon has to be adjusted approximately in such a way that the molar concentration of carbon atoms that occurs after its complete decomposition on the TaC luminous body is of the order of the equilibrium concentration of C atoms above the luminous body; the exact value depends on details (eg distance of the C source to the filament and to the sink, rate of decomposition of the hydrocarbons at the sink, etc.). When using anthracene as the source of carbon, the appropriate temperature for the source is in the range between 120 ° C and 150 ° C, when the distance between the filament located at eg 3400 K and the source is about 3 cm and the deposition of the carbon after decomposition of the hydrocarbons takes place at a about 400 ° C - 800 ° C hot nickel wire. The cold filling pressure in such a lamp is in the range around 1 bar; the inert gas (eg argon, krypton) preferably contains 2 mbar - 20 mbar hydrogen H 2 , 0.5 mbar CH 2 Br 2 and 2 mbar - 20 mbar iodine. By the bromine, the deposition of tantalum is to be prevented on the piston (see DE-Az 103 56 651.1), and by the iodine to be released during the evaporation and decomposition of the anthracene released hydrogen in the form of HJ. HJ here represents a sink for the released hydrogen.
Die Senke 13 ist durch Überzugswendeln 15 auf einer oder beiden Stromzuführungen 10 realisiert. Diese Wendeln bestehen beispielsweise aus Nickeldraht. Dieser kann im Innenvolumen angebracht sein, und zwar in der Nähe der Quetschung, oder sogar bis in die Quetschung hineinragen, wie an der rechten Wendel 15 gezeigt.The
In diesem Ausführungsbeispiel müssen sowohl Quelle als auch Senke bei relativ niedrigen Temperaturen, normalerweise unterhalb ca. 500°C, betrieben werden, wie man sie nahe der Kolbenwand findet. Hinsichtlich der Einbringung ist die Verwendung der Stromzuführungen 10 nahe der Quetschung 3 am einfachsten. Alternativ könnte auch die Quelle an der einen Stromzuführung 10 und die Senke an der anderen Stromzuführung 10 befestigt sein.In this embodiment, both source and sink must be operated at relatively low temperatures, typically below about 500 ° C, as found near the piston wall. With regard to introduction, the use of the power supply leads 10 near the
Das Ende des Mittelhalters 9 ist hier mit dem als Quellenmaterial dienenden Kohlenwasserstoff beschichtet. Zwar ist diese Ausführungsform einfach herzustellen, man muss aber dabei in Kauf nehmen, dass der Transport von der Quelle in die Senke hauptsächlich am Leuchtkörper 7 vorbei erfolgt. Da jedoch für die Zersetzung des Kohlenwasserstoffs am Katalysator, der hier von der Senke aus Nickeldraht gebildet ist, eine bestimmte Zeit benötigt wird, stellt sich im stationären Zustand in der gesamten Gasphase, auch außerhalb des direkten Weges von der Quelle zur Senke, eine erhöhte Konzentration an Kohlenwasserstoff bzw. Kohlenstoff ein.The end of the
Von Vorteil für die Funktionsweise ist daher die Verwendung einer Anordnung wie in
Die Senke ist hier durch den unteren, quetschungsnahen Teil 21 der Stromzuführungen 22 realisiert. Dieser Teil 21 besteht aus Molybdän, der als Katalysator bei der Zersetzung der Kohlenwasserstoffe dient. Der obere Teil 20 der Stromzuführung ist integral vom Karbid des Leuchtkörpers gebildet. Die unteren Teile 21 ragen bis in die Quetschung hinein.The sink is realized here by the
Bei dieser geometrische Anordnung befindet sich der Leuchtkörper 7 im Materialstrom, der sich von der Quelle 16 zur Senke 21 ausbildet. In
Der aus TaC bestehende Leuchtkörper 23, siehe
Ein Beispiel einer Quelle, die auf der Achse des Leuchtkörpers angeordnet ist, ist in
Die Quelle 31 ist eine Kohlenstoffabscheidung (Ruß) oder eine um die Stromzuführung 34 gewickelte Kohlenstoff-Faser. Die Senke 32 ist der Teil einer Stromzuführung, der aus Molybdän gefertigt ist und vom Leuchtkörper 33 abgewandt angeordnet ist. Dieser Teil ist über einen Schweißpunkt 35 mit dem Abgang 36 des Leuchtkörpers aus TaC verbunden.The
Vorteilhaft steht hier auf beiden Seiten des Leuchtkörpers 33 in axialer Richtung das gesamte Temperaturspektrum zur Verfügung, so dass z.B. die C-Quelle bei relativ hohen Temperaturen in der Nähe des Leuchtkörpers und die Senke bei niedrigeren Temperaturen weiter weg vom Leuchtkörper auf der anderen Seite angeordnet werden kann. In dem in
Als Leuchtkörpermaterial ist ein Metall oder eine Metallverbindung geeignet, dessen Schmelzpunkt in der Nähe des Schmelzpunkts von Wolfram, bevorzugt bei mindestens 3000 °C und besonders bevorzugt oberhalb dem von Wolfram, liegt. Neben Wolfram kommt dabei insbesondere Rhenium, Osmium und Tantal in Frage.As the filament material, a metal or a metal compound is suitable, whose melting point is in the vicinity of the melting point of tungsten, preferably at least 3000 ° C and more preferably above that of tungsten. Besides tungsten, rhenium, osmium and tantalum are particularly suitable.
Claims (24)
- Incandescent lamp having an illuminant which contains a high-temperature resistant metal compound (7) and having electrodes (10) which hold the illuminant (7), the illuminant being introduced vacuum-tightly together with a filling in a bulb (2), the material of the illuminant comprising a metal or a metal compound, in particular a metal carbide, whose melting point lies close to the melting point of tungsten, preferably at least at 3000°C and particularly preferably above that of tungsten, the illuminant containing a material which becomes depleted of at least one chemical element owing to chemical decomposition and/or evaporation during operation, and a source for this element being fitted in the bulb, the source delivering the element of which the illuminant is depleted, characterized in that a sink for this chemical element is also fitted in the bulb, the element which the illuminant emits progressively during the lifetime being deposited on the sink with the aid of a transport medium comprising hydrogen and/or a halogen, so that overall there is a continuous flux of the described element from the source to the sink, the concentration of the relevant element being essentially steady at any position in the lamp, apart from startup processes, the illuminant in steady-state operation being in equilibrium with the partial atmosphere of the element constantly transported past it, imposed from the outside by the interaction of the source and sink, so that the illuminant is prevented from being depleted of the element in question.
- Incandescent lamp according to Claim 1, characterized in that the illuminant is enclosed by a bulb of glass, in particular quartz glass or hard glass, or ceramic, in particular Al2O3.
- Incandescent lamp according to Claim 1, characterized in that at least one base gas in the form of an inert gas, in particular noble gas and/or nitrogen, is used as the filling.
- Incandescent lamp according to Claim 1, characterized in that the metal compound is a metal carbide, for example tantalum carbide, zirconium carbide or hafnium carbide or alloys of different metal carbides.
- Incandescent lamp according to Claim 4, characterized in that the source consists of a solid or liquid hydrocarbon or halogenated hydrocarbon which is operated in the temperature range of between 100°C and 400°C, and which releases carbon during decomposition.
- Incandescent lamp according to Claim 4, characterized in that the source consists of hydrogen, in particular carbon black or graphite fibers or of fabric or carbon moldings, the carbon being transported to the sink by material additionally introduced as a constituent of the filling, from the group hydrogen and/or halogen, this material reacting in cooler regions with the carbon to form hydrocarbons or halogenated hydrocarbons, this hydrocarbon decomposing again at the sink while depositing carbon and releasing the transport medium.
- Incandescent lamp according to Claim 4, characterized in that the source consists of a graphite body, in particular graphite fibers, coated with the corresponding metal carbide, the carbon being transported to the sink by material additionally introduced as a constituent of the filling, from the group hydrogen and/or halogen, this material reacting in cooler regions with the carbon to form hydrocarbons or halogenated hydrocarbons, this hydrocarbon decomposing again at the sink while depositing carbon and releasing the transport medium.
- Incandescent lamp according to Claim 4, characterized in that the source consists of a sintered material containing carbon, the carbon being transported to the sink by material additionally introduced as a constituent of the filling, from the group hydrogen and/or halogen, this material reacting in cooler regions with the carbon to form hydrocarbons or halogenated hydrocarbons, this hydrocarbon decomposing again at the sink while depositing carbon and releasing the transport medium.
- Incandescent lamp according to Claim 4, characterized in that a rod fastened in the vicinity of the illuminant, in particular an axially arranged rod, made of the same metal carbide as the illuminant is used as the source for the carbon, the longitudinal temperature profile of which corresponds to that of the illuminant consisting of the same metal carbide, and hydrogen and optionally halogen are used as a medium for transporting the carbon to the sink.
- Incandescent lamp according to Claim 4, characterized in that a rod fastened in the vicinity of the axis of the illuminant, made of a second metal carbide is used as the source for the carbon, the vapor pressure of which at a given temperature is greater than that of the metal carbide of the illuminant wire, in order to compensate for the losses by thermal conduction along the wire fastened in the axis of the filament, and hydrogen and optionally halogen are used as a medium for transporting the carbon to the sink.
- Incandescent lamp according to one of Claims 5 to 10, characterized in that the sink for the carbon consists of a catalytically active metal, in particular nickel or iron or molybdenum or cobalt or platinum, on which the optionally halogenated hydrocarbons decompose while depositing carbon and releasing hydrogen and optionally halogen.
- Incandescent lamp according to one of Claims 5 to 10, characterized in that the sink for the carbon consists of a carbide-forming metal, in particular of nickel or iron or molybdenum or cobalt or platinum, on which the optionally halogenated hydrocarbons decompose while forming metal carbides and releasing hydrogen and optionally halogen.
- Incandescent lamp according to one of Claims 5 to 10, characterized in that the sink for the carbon consists of aluminium, magnesium or molybdenum silicates.
- Incandescent lamp according to one of Claims 11 to 13, characterized in that the filling contains iodine, the released hydrogen being bound by reaction with iodine to form hydrogen iodide so that the iodine has the function of a gaseous sink for the hydrogen.
- Incandescent lamp according to one of Claims 11 to 13, characterized in that the released hydrogen escapes through the hot quartz bulb wall, so that the sink for the hydrogen is provided by the permeation of the hot bulb wall.
- Incandescent lamp according to one of Claims 11 to 13, characterized in that a hydrogen-affine metal is introduced into the bulb, the released hydrogen being bound or "gettered" by the hydrogen-affine metal, in particular zirconium or hafnium or niobium or tantalum.
- Incandescent lamp according to Claim 4, characterized in that a fluorinated, in particular perfluorinated hydrocarbon, in particular PTFE, which delivers perfluorinated carbon compounds as decomposition products at high temperatures, it is used as the source.
- Incandescent lamp according to Claim 17, characterized in that the carbon is transported by means of halogen, preferably chlorine to the sink which consists of a catalytically active metal or a carbide-forming metal, in particular nickel, iron, molybdenum, cobalt, platinum, tungsten or tantalum.
- Incandescent lamp according to one of the preceding claims, characterized in that the filling gas additionally contains a halogen compound and optionally hydrogen, sulfur or a cyanide compound, in order to prevent the metal and optionally the carbon from depositing on the bulb wall and to transport it back as much as possible to the illuminant.
- Incandescent lamp according to Claim 4, characterized in that the illuminant is coated with the material of which it is depleted and which is intended to be fed back to a source, and forms a first layer, and then a second layer of the illuminant material per se is applied from the outside onto this first layer.
- Incandescent lamp according to Claim 4, characterized in that the source consists of a body made of the same or another metal carbide, coated first with carbon in a first layer and then with metal carbide in a second layer, the carbon being transported to the sink by material additionally introduced as a constituent of the filling, from the group hydrogen and/or halogen, this material reacting in cooler regions with the carbon to form hydrocarbons or halogenated hydrocarbons, this hydrocarbon decomposing again at the sink while depositing carbon and releasing the transport medium.
- Incandescent lamp according to Claim 21, characterized in that the outer second layer is an alloy of different metal carbides, in particular an alloy of tantalum carbide and hafnium carbide.
- Incandescent lamp according to Claims 1 to 3, wherein the illuminant consists of a metal.
- Incandescent lamp according to Claim 23, characterized in that the illuminant consists of tungsten and in that a high molecular weight carbon and fluorine compound slowly decomposes over the lifetime of the lamp, fluorine being released which reacts to form tungsten fluorides at a tungsten reservoir applied in the temperature range between 1600 K and 2400 K and therefore having the function of a source which transports tungsten back preferentially to the hottest position on the illuminant, and the fluorine from the tungsten fluorides not converted at the illuminant reacting on the bulb wall to form gaseous SiF4, or the tungsten being accumulated by a superimposed boron cycle process at cooler positions of the framework and thus having the function of a sink for tungsten and fluorine.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102004052044A DE102004052044A1 (en) | 2004-10-26 | 2004-10-26 | Incandescent lamp with a luminous body containing a high temperature resistant metal compound |
PCT/DE2005/001857 WO2006045273A2 (en) | 2004-10-26 | 2005-10-18 | Incandescent lamp having an illuminant that contains a high-temperature resistant metal compound |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1805785A2 EP1805785A2 (en) | 2007-07-11 |
EP1805785B1 true EP1805785B1 (en) | 2010-12-01 |
Family
ID=35733985
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP05803936A Not-in-force EP1805785B1 (en) | 2004-10-26 | 2005-10-18 | Incandescent lamp having an illuminant that contains a high-temperature resistant metal compound |
Country Status (8)
Country | Link |
---|---|
US (1) | US7911121B2 (en) |
EP (1) | EP1805785B1 (en) |
JP (1) | JP4571981B2 (en) |
CN (1) | CN101048850B (en) |
AT (1) | ATE490547T1 (en) |
CA (1) | CA2584458A1 (en) |
DE (2) | DE102004052044A1 (en) |
WO (1) | WO2006045273A2 (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8044567B2 (en) | 2006-03-31 | 2011-10-25 | General Electric Company | Light source incorporating a high temperature ceramic composite and gas phase for selective emission |
US7722421B2 (en) | 2006-03-31 | 2010-05-25 | General Electric Company | High temperature ceramic composite for selective emission |
US7851985B2 (en) | 2006-03-31 | 2010-12-14 | General Electric Company | Article incorporating a high temperature ceramic composite for selective emission |
CN102171795A (en) * | 2008-10-03 | 2011-08-31 | 维易科加工设备股份有限公司 | Vapor phase epitaxy system |
US7965026B2 (en) * | 2009-06-25 | 2011-06-21 | General Electric Company | Lamp with IR suppressing composite |
DE202009013860U1 (en) | 2009-10-13 | 2010-11-25 | Osram Gesellschaft mit beschränkter Haftung | halogen bulb |
KR20130007589A (en) * | 2010-02-26 | 2013-01-18 | 엘리언스 포 서스터너블 에너지, 엘엘씨 | Hot wire chemical vapor deposition with carbide filaments |
JP5989984B2 (en) | 2011-10-27 | 2016-09-07 | スタンレー電気株式会社 | Incandescent light bulb |
JP5975816B2 (en) * | 2012-09-21 | 2016-08-23 | スタンレー電気株式会社 | Incandescent light bulb, manufacturing method thereof, and filament |
ITUB20152829A1 (en) * | 2015-08-04 | 2017-02-04 | Getters Spa | Hydrogen dosing in LED lighting bulbs |
Citations (2)
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US3277330A (en) * | 1960-07-15 | 1966-10-04 | Polaroid Corp | Incandescent lamp with tac filament and cyanide-radical producing and halogen atmosphere |
US3405328A (en) * | 1966-03-02 | 1968-10-08 | Westinghouse Electric Corp | Incandescent lamp with a refractory metal carbide filament |
Family Cites Families (11)
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GB190908283A (en) * | 1908-04-06 | 1909-08-26 | Ernst August Krueger | An Improved Method for Regenerating Blackened Carbon Filament Electric Lamps. |
US3237284A (en) * | 1962-02-05 | 1966-03-01 | Polaroid Corp | Method of forming carbide coated coiled filaments for lamps |
GB1047302A (en) * | 1963-03-28 | |||
US3717784A (en) * | 1970-06-25 | 1973-02-20 | Sylvania Electric Prod | Tungsten halogen lamp with tungsten mesh deflector |
JPS5281975A (en) * | 1975-12-29 | 1977-07-08 | Iwasaki Electric Co Ltd | High-melting point carbide filament |
US4450381A (en) * | 1982-04-05 | 1984-05-22 | Gte Products Corporation | Tungsten-halogen lamp with preferential tungsten deposition site |
JPH08273633A (en) * | 1995-03-31 | 1996-10-18 | Toshiba Lighting & Technol Corp | Tungsten halogen lamp and reflection type tungsten halogen lamp and lighting system |
BR0013489A (en) | 1999-08-22 | 2002-05-14 | Ip2H Ag | Light source |
AU2003210146A1 (en) | 2002-03-04 | 2003-09-16 | Ip2H Ag | Source of light and method for regenerating a source of light |
DE10356651A1 (en) | 2003-12-01 | 2005-06-23 | Patent-Treuhand-Gesellschaft für elektrische Glühlampen mbH | Incandescent lamp using a carbon cycle comprises a luminescent element which is inserted in a vacuum-tight manner in a bulb along with a filler |
DE10358262A1 (en) * | 2003-12-01 | 2005-09-01 | Patent-Treuhand-Gesellschaft für elektrische Glühlampen mbH | Light bulb with carbon cycle process |
-
2004
- 2004-10-26 DE DE102004052044A patent/DE102004052044A1/en not_active Withdrawn
-
2005
- 2005-10-18 DE DE502005010636T patent/DE502005010636D1/en active Active
- 2005-10-18 JP JP2007538259A patent/JP4571981B2/en not_active Expired - Fee Related
- 2005-10-18 WO PCT/DE2005/001857 patent/WO2006045273A2/en active Application Filing
- 2005-10-18 EP EP05803936A patent/EP1805785B1/en not_active Not-in-force
- 2005-10-18 CN CN2005800364666A patent/CN101048850B/en not_active Expired - Fee Related
- 2005-10-18 CA CA002584458A patent/CA2584458A1/en not_active Abandoned
- 2005-10-18 US US11/665,158 patent/US7911121B2/en not_active Expired - Fee Related
- 2005-10-18 AT AT05803936T patent/ATE490547T1/en active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3277330A (en) * | 1960-07-15 | 1966-10-04 | Polaroid Corp | Incandescent lamp with tac filament and cyanide-radical producing and halogen atmosphere |
US3405328A (en) * | 1966-03-02 | 1968-10-08 | Westinghouse Electric Corp | Incandescent lamp with a refractory metal carbide filament |
Also Published As
Publication number | Publication date |
---|---|
EP1805785A2 (en) | 2007-07-11 |
WO2006045273A2 (en) | 2006-05-04 |
US20090045742A1 (en) | 2009-02-19 |
WO2006045273A3 (en) | 2006-10-26 |
DE102004052044A1 (en) | 2006-04-27 |
CA2584458A1 (en) | 2006-05-04 |
JP4571981B2 (en) | 2010-10-27 |
DE502005010636D1 (en) | 2011-01-13 |
CN101048850A (en) | 2007-10-03 |
US7911121B2 (en) | 2011-03-22 |
CN101048850B (en) | 2011-03-09 |
JP2008518409A (en) | 2008-05-29 |
ATE490547T1 (en) | 2010-12-15 |
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