From patent specification CH 645 753, a circuit breaker can be used in an electrical high-voltage grid. This circuit breaker has a rotationally symmetrical interrupting chamber which is filled with a dielectrically inert gas, for example with SF6 gas, as quenching and insulating medium. The interrupting chamber has an arcing volume in which the quenching and insulating medium is ionized and heated up by the breaking arc burning between two arcing contact pieces. A part of this heated quenching and insulating medium flows off through an insulating nozzle into an exhaust volume where it is cooled and redirected by means of a cooling device. Mixing the heated quenching and insulating medium with the cold gas existing in the exhaust is possible only to a comparatively small extent since the predominant part of the cold gas is pressed out of the exhaust by the heated quenching and insulating medium before any significant mixing is possible. The flow resistance with which the cooling device opposes the flowing gas is kept as low as possible in this circuit breaker. The cooled and deionized quenching and insulating medium is then available again for further switching processes.
The cooling device has cooling plates which are elaborately shaped to aid the flow and must be elaborately held and, in addition, are manufactured of a metal which is resistant to burn-off loss or wear and is therefore comparatively expensive. Cooling of the heated quenching and insulating medium by mixing it with cold gas only occurs here to a very slight extent.
A circuit breaker has a distinctly increased breaking capacity, the exhaust of which is constructed comparatively simply and inexpensively and which cools the hot gases in a particularly effective manner.
The circuit breaker has in an enclosure filled with an insulating gas at least one interrupting chamber extending along a longitudinal axis. The interrupting chamber can be constructed radially symmetrically, containing an arcing volume and at least two associated arcing contacts. The arcing volume is actively connected to at least one exhaust having an exhaust volume. The exhaust is constructed for cooling hot gases generated during breaking operations and is connected to a volume of the interrupting chamber. In the area of the exhaust, at least one forcibly created recirculation area can be provided which increases the flow resistance of the hot gases.
In one exemplary circuit breaker, the hot gases, during breaking, flow from the arcing volume into an intermediate volume in which at least one baffle plate protruding into the flow of the hot gases is provided. The intermediate volume is attached to a flow tube constructed in the manner of a laval nozzle and having a nozzle constriction, which flow tube leads into the exhaust volume connected to the interrupting chamber volume.
An exemplary embodiment of the circuit breaker is constructed in such a manner that between the entry of the hot gases into the intermediate volume and the baffle plate, a distance L1 is provided, that between the baffle plate and the nozzle constriction, a distance L2 is provided, that between the nozzle constriction and an exit edge of the flow tube a distance L3 is provided, and that between the distances the following relationship applies: L2=0.7*L1 and that the length L3 of the flow tube is within a range of twice to three times the diameter of the nozzle constriction of the flow tube.
In another exemplary embodiment of the circuit breaker, means are provided in the exhaust volume which deflect the flow of the hot gases by up to 180°.
A variant of the circuit breaker suitable for extremely large breaking powers can have openings in the flow tube which provide for an additional entry of gas into the flow tube so that at least one second forcibly created recirculation area is formed in which the hot gases are particularly effectively mixed with colder gas and cooled.
The advantages achieved by the various embodiments can be seen in effect that, due to particularly good cooling of the hot gases, a progressive reduction in volume of these, and thus optimal flow-off of the hot gases out of the arcing volume is ensured so that a distinctly higher breaking capacity of the circuit breaker is achieved, the dimensions of the interrupting chamber remaining approximately the same.
At the same time, reliability on switching-off the circuit breaker is also advantageously increased.
The further advantageous embodiments of the invention are the subject matter of the dependent claims.
The invention, its improvements and the advantages achieved thereby are explained in greater detail by means of exemplary embodiments illustrated in the drawings, wherein:
In all figures, identically acting elements are provided with identical reference symbols. Any elements not required for the direct understanding of the invention are not shown or not described, respectively.
A circuit breaker can have one or more series-connected interrupting chambers filled with an insulating gas, which operate in accordance with one of the conventional switching principles, that is to say, for example, as self-blowing or self-extinguishing chamber, as self-blowing chamber with at least one additional compression piston or puffer arrangement or as simple puffer breaker. The circuit breaker can be constructed as encapsulated circuit breaker and metal or plastic can be chosen as encapsulating material. Thus, the circuit breaker can be constructed, for example, as life-tank or outdoor breaker, as part of metal-encapsulated gas-insulated switchgear or as dead-tank breaker.
This interrupting chamber 1 can be constructed, for example, rotationally symmetrically and extends along a longitudinal axis 2. The interrupting chamber 1 can be enclosed gastight by a concentrically arranged and grounded metal enclosure 3. The electrically insulating holders which fix the interrupting chamber 1 in the metal enclosure 3 are not shown. The interrupting chamber 1 has an arcing volume 4 in which an arc 7 is burning between two rod-shaped arcing contacts 5 and 6 during the switching-off operation. The arcing contact 5 can be constructed as moving contact which moves axially in the direction of an arrow 8 during the switching-off operation whereas the arcing contact 6 is constructed as stationary contact but its mechanical attachment is not shown for the sake of simplicity. However, interrupting chamber variants could also be equipped correspondingly with arcing contacts which can be moved on both sides or arcing contacts which are fixed on both sides. The arcing volume 4 is limited in the radial direction by the inside wall of an insulating nozzle 9. The insulating nozzle 9 opens in the direction of an intermediate volume 10. The insulating nozzle 9 can be constructed to be fixed, but can also be movable together with the arcing contact 5, as has been assumed here.
During the switching-off operation the arc 7 heats up the insulating gas in the arcing volume 4 in familiar manner. The predominant part of this heated, ionized and pressurized gas flows off through the insulating nozzle 9 into the intermediate volume 10. This conical hot-gas stream emerging from the insulating nozzle 9 impinges on a baffle plate 11, which, as a rule, is metallic and is attached to the stationary arcing contact 6. This circular baffle plate 11 causes the hot gas flow to be deflected and prevents the hot gas from flowing directly axially onward into an exhaust volume 12. An arrow 13 indicates the general flow direction of this hot gas from the arcing volume 4 into the exhaust region and through the latter.
The intermediate volume 10 is limited in the radial direction by a metallic wall 14. On the side facing the insulating nozzle 9, a tubular stub 15, which has a smaller diameter than the intermediate volume 10 limited towards the outside by the wall 14, is attached to the wall 14 in the axial direction. In this tubular stub 15, the outside of the insulating nozzle 9 is axially guided. On the side facing away from the tubular stub 15, a constriction 16 is attached to the wall 14 of the intermediate volume 10 and limits the intermediate volume 10 on this side. The transition from the wall 14 to the constriction 16 has a radius R. This radius R supports the deflection of the hot gases in the intermediate volume 10. For breaking currents in the range of 40 kA to 70 kA, a radius R in the range of 25 mm is selected as a result of which an exit angle α of around 30° of the cooled exhaust gases is achieved.
The constriction 16 changes into an axially extending metallic flow tube 17 which is constructed in the manner of a laval nozzle and which has on the side facing the intermediate volume 10 a nozzle constriction 18 and which opens towards the exhaust volume 12. The end of the flow tube 17 in the direction of the exhaust volume 12 is called the exit edge 17a. The flow tube 17, constructed in the manner of a laval nozzle, accordingly connects the intermediate volume 10 to the exhaust volume 12.
The exhaust volume 12 is limited by a metallic exhaust housing 19 which is constructed to promote flow and which deflects the flow of the hot gas by up to 180°. A cylindrically constructed part of the exhaust housing 19 has approximately the same outside diameter as the intermediate volume 10 and surrounds the flow tube 17, a duct 20 with annular cross section remaining for the flowing and already slightly cooled hot gas between the flow tube and the exhaust housing 19. Between the outside wall of the constriction 16 and an end edge 21 of the exhaust housing 19, a cylindrical exit area remains through which the gas, cooled further, flows obliquely into an interrupting chamber volume 22. The insulating gas in the interrupting chamber volume 22 surrounds the active parts, described above, of the interrupting chamber 1 and insulates them against the metal enclosure 3.
The intermediate volume 10 has a length L1 up to the baffle plate 11. From the baffle plate 11 to the nozzle constriction 18, the distance is called L2 and from the nozzle constriction 18 to the exit edge 17a, the flow tube 17 has the length L3. The following ratio of lengths has been found to be particularly advantageous with the cooling performance of the exhaust arrangement: L2=0.7*Ll. If a greater longitudinal extent of the exhaust arrangement is easily possible, values of 70% to 100% of Ll can also be achieved here. The length L3 of the flow tube 17 is advantageously selected in such a manner that it corresponds to three times the diameter of the nozzle constriction 18. However, a satisfactory exhaust capacity is also achieved, if the length L3 of the flow tube 17 is selected in such a manner that it is within the range of twice to three times the diameter of the nozzle constriction 18.
In an optimum exhaust configuration which also comprises the length ratios described above, the area FD, the area of the baffle plate 11 and the area F1, are constructed to be approximately of the same size. The annular area FA around the baffle plate 11 is constructed in such a manner that it has 30% to 80% of the area FD. An optimum exhaust capacity is obtained when the relationship FA=50%*FD is maintained. As a rule, the areas FE and F2 are dimensioned in such a manner that they are within a range of 50% to 70% of FD. The annular area F3 is of approximately the same size as the area FD, as is the exit area F4.
Additional openings 25 can be provided downstream of the nozzle constriction 18 in the flow tube 17. These openings 25 can be of different shapes and connect the interior of the flow tubes 17 with the annular volume outside the flow tube 17. In addition, a deflector 26 constructed to promote flow can be mounted opposite to the opening of the flow tube 17 in the exhaust housing 19, which deflector 26 facilitates the deflection of the hot-gas flow by 180°.
To explain the operation, the figures described above will now be considered in greater detail. The arrow 13 indicates the general flow of the hot gases created by the arc 7 through the exhaust region of the interrupting chamber 1. After the hot gases flow out of the insulating nozzle 9, they impinge on the baffle plate 11 and are slightly deflected. The baffle plate 11 absorbs thermal energy from the hot gases, as does the wall 14. Due to this cooling, the volume of the flowing hot gas is slightly reduced. The hot gas then flows around the baffle plate 11 and impinges on the constriction 16 where it is again deflected and cooled further by delivering energy to the material of the constriction 16 and its volume is thus reduced.
The area of the intermediate volume 10 which is located downstream of the baffle plate 11 is partially used as a recirculation area 29 for the flowing gas. The area of the recirculation area 29 is diagrammatically shown by an arrow 30 shown dashed. In the recirculation area 29, an effective flow is formed which leads to a particularly good intermixing of the hot gases with the cooler insulating gas located in the intermediate volume 10. Due to this intermixing of the hot gases with the cooler insulating gas located in the intermediate volume 10, the major proportion of the heat energy is removed from the hot gas. The turbulences occurring in the edge areas of the intermediate volume 10 do improve the heat transition from the hot gas into the material of the limiting materials but, as a rule, their contribution to the cooling effect of the exhaust is not significant.
This mixed gas which is cooled further then flows into the flow tube 17 where it is first narrowed down by the nozzle constriction 18. Since the flow tube 17 widens out in the manner of a laval nozzle after the nozzle constriction 18, the flow velocity of the gas is increased there so that a negative pressure is produced which additionally sucks the gas through the nozzle constriction 18. This effect advantageously increases the intensity of the mixing of gases in the area of the recirculation area 29 located downstream of the baffle plate 11. The wall of the flow tube 17 also absorbs and removes heat energy from the hot gases.
The hot gases initially flow away from the arcing volume 4 in predominantly an axial direction but after emerging from the flow tube 17, they are deflected by 180° by the exhaust housing 19 and are guided oppositely to the original flow direction outside the flow tube 17. The metallic exhaust housing 19 also absorbs heat energy which it removes from the hot gas. This heat transition is improved by eddies which are mandatorily produced during the deflection of the gas. This complete redirection of the gas flow reduces the constructional length of the exhaust area with the result of an advantageous reduction in size and thus also a reduction of costs of the interrupting chamber 1. Geometric relationships allowing, it is also easily conceivable to install a comparatively large exhaust volume 12 and then to omit this deflection described.
Afterward, the gas, cooled further, flows on in the direction of the interrupting chamber volume 22 between the outside of the flow tube 17 and the exhaust housing 19. As can be seen from
The exemplary embodiments of the interrupting chamber 1 shown in
In another variant, the openings 25 in the flow tube 17 allow the entry of slightly cooler gases from outside in the interior of the flow tube 17 since the gas pressure outside the flow tube 17 is higher than in its interior. As a consequence, a further recirculation area 31, indicated by dashed arrows 32, forms here in the flow tube 17 and in the duct 20. In this recirculation area 31, which is also generated by force, further intensive mixing of hot and cold gas takes place, associated with even better cooling of the hot gases. Afterwards, the flow velocity of the exhaust gases in the flow tube 17 increases again.
The deflector 26 inserted into the exhaust housing 19 advantageously reduces the flow resistance during the deflection of the gas flow into the opposite direction. In addition, the deflector 26 removes further heat energy from the gas flow.
The circular metallic baffle plate 11 with narrow radial notches 27, distributed around a circumference, as shown in
All these measures, individually or also in combination, bring with them an advantageous increase in the breaking capacity of the circuit breaker. If further increase in the capacity of the circuit breaker is to be achieved, the geometric construction of the exhaust region of the moving arcing contact 5 opposite the fixed arcing contact 6 is designed in similar manner as the embodiments already described so that the hot gases removed on the side of the moving arcing contact 5 from the arcing volume 4 in the direction of the interrupting chamber volume 22 are also cooled in a similarly effective manner, which is associated with further advantageous reduction in the volume of the flowing hot gas. A circuit breaker, the interrupting chamber or interrupting chambers of which are provided with this improved cooling of the hot gases on both sides has a distinctly higher breaking capacity than a conventional circuit breaker having the same dimensions.
It is also easily possible to configure an exhaust variant without the baffle plate 11 and without the perforated plate 23. In such an exemplary exhaust variant, only the flow tube 17 is provided with the openings 25 so that the recirculation area 31 forms as a single recirculation area during the breaking or switching-off operation of the circuit breaker and provides for intensive cooling of the hot gases in this area. This exhaust variant can also be configured with or without the gas deflection following the flow tube 17.
It will be appreciated by those of ordinary skill in the art that the exemplary circuit breakers described here can be embodied in various specific forms without departing from the essential characteristics thereof. The presently disclosed embodiments are considered in all respects to be illustrative and not restrictive. The scope of the invention is indicated by the appended claims, rather than the foregoing descriptin, and all changes that come within the meaning and range of equivalence thereof are intended to be embraced.
Number | Date | Country | Kind |
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04405351.0 | Jun 2004 | EP | regional |
This application claims priority under 35 U.S.C. §119 to EP Application 04405351.0 filed in the European Patent Office on 7 Jun. 2004, and as a continuation application under 35 U.S.C. §120 to PCT/CH2005/000295 filed as an International Application on 25 May 2005 designating the U.S., the entire contents of which are hereby incorporated by reference in their entireties.
Number | Date | Country | |
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Parent | PCT/CH05/00295 | May 2005 | US |
Child | 11634076 | Dec 2006 | US |