Preservation method

Abstract

A power plant and method for preserving a power plant, the power plant having a steam turbine with a shaft, further including a condenser mounted downstream of the steam turbine in the direction of flow of the steam, a vacuum pump mounted downstream of the condenser, a compressed steam system with shaft seals, and a compressed steam supply line extending into the shaft seals; a first nitrogen line extends into the condenser, and a second nitrogen line as well as a recirculation line that branches off the vacuum pump extend into the compressed steam supply line.

Claims

1. A power plant comprising: a steam turbine with a shaft, a condenser connected downstream of the steam turbine in the direction of steam flow, a vacuum pump connected downstream of the condenser, a compressed steam system with shaft seals and a compressed steam supply line leading into the shaft seals, a first nitrogen line which leads into the condenser, and a second nitrogen line and a recirculation line branching off from the vacuum pump which lead into the compressed steam supply line.

2. The power plant as claimed in claim 1, wherein the shaft seals comprise sealing steam chambers and exhaust steam chambers, and wherein the compressed steam supply line leads into the sealing steam chambers and the exhaust steam chambers are connected with an exhaust steam fan for drawing off air penetrating into the shaft seals and a sub-stream of the steam from the sealing steam chambers and feeding then to an exhaust steam condenser.

3. The power plant as claimed in claim 1, wherein an electrical superheater is connected into the compressed steam supply line and the first nitrogen line leads into the compressed steam supply line upstream of the electrical superheater.

4. A method for preserving a power plant comprising a steam turbine, a condenser connected downstream of the steam turbine, a vacuum pump connected downstream of the condenser and a compressed steam system, the method comprising: on shutdown of the steam turbine into a preserved state, feeding nitrogen into the compressed steam system and into the condenser, and bringing the steam turbine and the condenser to nitrogen overpressure and switching off the vacuum pump, and on start-up of the steam turbine, bringing the vacuum pump back into operation and branching off nitrogen at least for a time at the exhaust air of the vacuum pump and feeding the nitrogen to the compressed steam system.

5. The method as claimed in claim 4, wherein the nitrogen is fed into a compressed steam supply line of the compressed steam system upstream of an electrical superheater.

6. The method as claimed in claim 4, wherein on shutdown of the power plant the nitrogen is fed jointly with steam into the compressed steam supply line as soon as it is possible to break the vacuum.

7. The method as claimed in claim 4, wherein, after shutdown of the steam turbine, once a nitrogen overpressure has been reached in the steam turbine and in the condenser, the nitrogen supply of the compressed steam system is taken out of operation during the preserved state.

8. The method as claimed in claim 4, wherein a nitrogen pressure is increased in the steam turbine or in the condenser prior to an expected temperature change in the steam turbine or in the condenser.

9. The method as claimed in claim 4, wherein, on start-up of the power plant, as long as sufficient compressed steam is not present, the nitrogen is backfed continuously via the compressed steam system.

10. The method as claimed in claim 4, wherein the nitrogen from the condenser is recirculated into the compressed steam system for start-up of the power plant, once air in a recirculation line from the condenser to the compressed steam system has been expelled and once a sufficiently reduced pressure has been achieved in the condenser to allow steam diverting stations to be opened.

11. The method as claimed in claim 4, wherein heating or keeping warm of the steam turbine is assisted by heating of the nitrogen via an electrical superheater arranged in the compressed steam supply line.

12. The method as claimed in claim 4, wherein nitrogen-enriched exhaust air from exhaust steam chambers is compressed and made available as input air to a nitrogen generator.

13. The method as claimed in claim 4, wherein a comparatively small, first quantity of high purity nitrogen is provided for preservation during the shutdown for the steam turbine and while it is out of service and a comparatively larger, second quantity of less pure nitrogen is provided per unit time for start-up.

14. The method as claimed in claim 4, wherein an exhaust steam system is in operation at least for a time during deliberate filling of the condenser and the steam turbine with nitrogen.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The invention is explained in greater detail by way of example with reference to the drawings, in which, schematically and not to scale:

(2) FIG. 1 shows a power plant according to the invention and

(3) FIG. 2 shows the operational sequence of a method for preserving a power plant.

DETAILED DESCRIPTION OF INVENTION

(4) FIG. 1 is a schematic diagram which shows by way of example a power plant 1 comprising a steam turbine 2 with a shaft 3, a condenser 4 connected downstream of the steam turbine 2 in the direction of steam flow and a vacuum pump 5 connected downstream of the condenser 4. To seal off the shaft 3, use is conventionally made of a compressed steam system 6 with a compressed steam supply line 8 leading into the shaft seals 7. The shaft seals 7 comprise sealing steam chambers 12 and exhaust steam chambers 13. The compressed steam supply line 8 coming from the auxiliary steam generator 19 leads into the sealing steam chambers 12. To superheat the auxiliary steam or compressed steam, an electrical superheater 16 is connected into the compressed steam supply line 8. Within an exhaust steam system 18, the exhaust steam chambers 13 are connected with an exhaust steam fan 14, for drawing off air penetrating into the shaft seals 7 and a sub-stream of the steam from the sealing steam chambers 12. The drawn off exhaust steam is fed to an exhaust steam condenser 15.

(5) According to the invention, a first nitrogen line 9 leads into the condenser 4. A second nitrogen line 10 leads upstream of the electrical superheater 16 into the compressed steam supply line 8. In addition, a recirculation line 11 branching off from the vacuum pump 5 leads into the compressed steam supply line 8. The recirculated quantity of nitrogen may be adjusted via a valve 40 in the recirculation line 11. Pressure control of the vacuum pump 5 may also proceed via valve 41 or via the two valves 40 and 41 combined. In the exemplary embodiment of FIG. 1, nitrogen supply proceeds via a nitrogen generator and a nitrogen reservoir 20. Since, with regard to the delivered volumetric flow rate, the vacuum pump 5 is not expected to be designed for the recirculation of nitrogen for the purposes of preservation and tends to be oversized for this purpose, FIG. 1 shows two further measures with which operation with the vacuum pump 5 is nonetheless sensibly possible. On the one hand, excess pumped nitrogen may be returned to the inlet of the vacuum pump 5 via the return line 42 with valve 43, and on the other hand nitrogen may be delivered directly into the nitrogen reservoir 20 via line 44 with compressor 45.

(6) In the method according to the invention for preserving a power plant 1, according to FIG. 2 on shutdown of the steam turbine 2 into a preserved state nitrogen is introduced 21 upstream of an electrical superheater 16 into the compressed steam supply line 8 of the compressed steam system 6 and into the condenser 4. While the steam turbine 2 is still synchronized with the grid, the condenser pressure may only be raised to a limited degree by the supply of nitrogen, in order to avoid ventilation problems at the steam turbine 2. In the event both of shutdown and start-up of the steam turbine 2, nitrogen may for a time be fed 22 jointly with steam into the compressed steam supply line 8, but in particular only when the vacuum can be broken. Only after separation from the grid and achievement of the turning speed is the vacuum pump 5 switched off 23. A corresponding condenser-side shut-off at the condenser air extraction is closed. The vacuum breaker is not used (it may optionally be wholly dispensed with if it is replaced by a sufficiently large nitrogen feed-in at the condenser). The pressure in the condenser 4/steam turbine 2 is then raised to overpressure 24 via nitrogen supply.

(7) In the compressed steam system an overpressure is always maintained 25 (either by nitrogen feed-in, conventional compressed steam supply from the boiler or a combination of the two) during the nitrogen filling operation (this may begin slowly as early as during shutdown of the power plant, i.e. steam turbo set still synchronized with the grid), such that no ambient air can penetrate via this path. It may thus be ensured that from a chemical standpoint the plant is already ready for a rapid start (no waiting for steam purity) and corrosion is stopped in the region of steam turbine and condenser even in the event of a full condensate collection tank.

(8) After complete shutdown of the steam turbine 2 and once a nitrogen overpressure has been achieved in the steam turbine 2 and in the condenser 4, the nitrogen supply of the compressed steam system 6 is taken out of operation 26 during the preservation phase. The exhaust steam system 18 is in operation at least for a time during deliberate filling of the condenser and the steam turbine with nitrogen.

(9) Nitrogen-enriched exhaust air from the exhaust steam chambers 13 may be compressed and made available 28 as input air to a nitrogen generator 17. For preservation during the shutdown procedure for the steam turbine 2 and while it is out of service, a comparatively small, first quantity of high purity nitrogen is needed 29.

(10) Heating or keeping warm of the steam turbine 2 is assisted 30 by heating of the nitrogen via an electrical superheater 16 arranged in the compressed steam supply line 8.

(11) Prior to an expected temperature change in the steam turbine 2 or in the condenser 4, a nitrogen pressure in the steam turbine 2 or in the condenser 4 is increased 31.

(12) On start-up of the power plant 1, in particular during condenser evacuation, nitrogen is backfed 32 continuously via the compressed steam system 6 to seal the steam turbine shaft seal, as long as sufficient compressed steam is not present.

(13) On start-up of the steam turbine 2, the vacuum pump 5 is brought back into operation 33. In particular, a vacuum sufficient for opening the steam diverting stations or enabling start of the gas turbine is generated via the vacuum pumps. Nitrogen is discharged 34 overhead via a corresponding exhaust air line at the vacuum pumps or, in the case of on-site nitrogen production (e.g. by means of pressure swing adsorption), is fed to a special feed air area in a compressed air generation plant for nitrogen production 35. It is thus sensible to recompress the heavily nitrogen-containing exhaust gas from the exhaust steam system 18 or the exhaust air from the vacuum pump 5 and make it available to the nitrogen generator 17 as compressed input air. In this way, the nitrogen production plant and the compressed air quantity needed therefor may be much smaller.

(14) The nitrogen required may either proceed via an externally fillable receiver (for example set of cylinders) or nitrogen is produced on-site (for example by means of pressure swing adsorption) and optionally kept ready in a receiver. The size of the receiver and/or of the nitrogen production plant must be sufficient to ensure at least filling of the steam turbine/condenser and subsequent pressure maintenance. Furthermore, the renewed start-up system must also be taken into consideration, i.e. it is necessary to consider from when nitrogen backfeed may be replaced again by conventional compressed steam. If nitrogen production does not take place on-site, delivery logistics must be taken into consideration when determining the size of the receiver.

(15) To limit nitrogen requirements, during start-up nitrogen is branched off at least for a time at the exhaust air of the vacuum pump 5 and fed 36 to the compressed steam system 6. The nitrogen is naturally not recirculated into the compressed steam system 6 immediately, but rather only after a given operating time, specifically once air in a recirculation line 11 from the condenser 4 to the compressed steam system 6 has been expelled and once a sufficiently reduced pressure has been achieved in the condenser 4 which enables opening of steam diverting stations. This is ensured by corresponding shut-off devices.

(16) In the case of nitrogen production on-site, the capacity of a given nitrogen plant may be varied by varying the degree of nitrogen purity. As has already been described above, the provision of a smaller but high purity nitrogen quantity is necessary for preservation.

(17) This is required during the shutdown procedure and the out-of-service period and results from the comparatively low nitrogen losses via the exhaust steam system, since the nitrogen overpressure in steam turbine/condenser is kept very low for preservation purposes. Nitrogen production could then be changed over for start-up from high purity in the case of preservation such that a comparatively larger, second quantity of less pure nitrogen is provided 37. The provision of a larger quantity of less pure nitrogen for start-up is necessary in relation to quantity and sufficient with regard to purity. Nitrogen has namely to be provided with a higher pressure in the compressed steam system 6, whereby the nitrogen losses via the exhaust steam system 18 increase. On the other hand, the increased impurity is not a problem due to the start-up operation being short, and furthermore high purity nitrogen is also recirculated via the vacuum pump 5.

(18) With regard to operational safety, it should be noted that the exhaust steam system 18 (in particular the extraction fans) remains in operation for the entire time (even during the optionally extended out-of-service preservation) and the nitrogen, otherwise escaping into the power house via the shaft seals 7, is removed overhead via a corresponding pipe or fed to a particular (correspondingly well shielded) feed air region in an optionally additional compressed air generation plant intended merely to compress the nitrogen-containing exhaust air. The power house ventilation present ensures, as a further safety measure, that any nitrogen accumulations (e.g. in the event of malfunctioning of the extractor fans at the exhaust steam system 18), which could stop sufficient oxygen supply for people, cannot arise in the first place. As a further safety measure, corresponding alarm installations, which indicate that the exhaust steam system 18 and/or the building ventilation have failed, and moreover corresponding gas detectors may be applied, which detect and accordingly clearly indicate either a high nitrogen concentration or a low oxygen concentration. To this end, stationary gas detectors or indeed those worn by individual employees may be used. Thus, any problems arising in relation to personal safety may be very well managed. Overall, it should also be noted that the molecular nitrogen given off in gaseous form is non-toxic in itself and, as the main constituent of air, also not an environmentally relevant emission.