This application is the US National Stage of International Application No. PCT/EP2018/056199 filed Mar. 13, 2018, and claims the benefit thereof. The International Application claims the benefit of German Application No. DE 10 2017 205 382.8 filed Mar. 30, 2017. All of the applications are incorporated by reference herein in their entirety.
The invention relates to a method for starting up a vertical forced-flow steam generator in a waste-heat steam generator, and to a device for starting up a vertical forced-flow steam generator in a waste-heat steam generator.
Waste-heat steam generators with a forced-flow evaporator are known as so-called horizontal BENSON waste-heat steam generators (with a horizontal flue gas path) and vertical BENSON waste-heat steam generators (with a vertical flue gas path). The embodiment with a vertical flue gas path has cost advantages in comparison with the horizontal design. On the other hand, there are operational disadvantages of the vertical BENSON waste-heat steam generator in the form of considerably higher water consumption, caused by a considerably greater expulsion of water (blowdown) during startup.
It is therefore an object of the invention to specify a method for starting up a vertical forced-flow steam generator, that is to say with a vertical flue gas path, in a waste-heat steam generator, in which the water consumption is reduced in comparison with the prior art. A further object of the invention is to specify a corresponding device for starting up a vertical forced-flow steam generator in a waste-heat steam generator.
The invention achieves the object directed toward a method for starting up a vertical forced-flow steam generator in a waste-heat steam generator in that it provides that, for such a method for starting up a vertical forced-flow steam generator in a waste-heat steam generator, wherein feed water is supplied as working fluid to the forced-flow steam generator, and there flows firstly through a feed water preheater and then through an evaporator and in the process at least partially evaporates, the partially evaporated working fluid being supplied to a water separation system in which non-evaporated working fluid is separated beyond evaporated working fluid and is collected, at least a portion of the non-evaporated working fluid collected in the water separation system is supplied geodetically to the evaporator and, beyond a specific quantity of accumulating non-evaporated working fluid, a remaining portion is automatically discharged from the water separation system.
Owing to the return of the non-evaporated working fluid, the water consumption of the gas and steam turbine installation is reduced considerably. The systems required for the disposal of the accumulating waste water may be designed to be smaller (and thus at a lower cost). The systems required for the refeeding of the required deionate may likewise be designed to be smaller (and thus at a lower cost).
Owing to the geodetic return, the use of pumps is no longer necessary. This has a positive effect both with the investments and with the fail-safety of the installation.
It is expedient here if the water separation system comprises a separator and a bottle and the non-evaporated working fluid is returned from the separator, since this keeps the outlay for a geodetic return low in comparison with an embodiment without separation of separator and bottle.
It is very particularly advantageous if, for returning the non-evaporated working fluid to the evaporator from the water separation system, merely a shut-off fitting is opened and the quantity of returned working fluid is regulated solely by the geometry of the water separation system.
The object directed toward a device for starting up a vertical forced-flow steam generator in a waste-heat steam generator is achieved by a device with a feed water preheater which, by means of a feed water pump, can be supplied with feed water as working fluid via a feed water supply line, with an evaporator which is arranged downstream of the feed water preheater in the direction of flow of the working fluid and which can be flowed through by the working fluid and can at least partially evaporate said working fluid, with a water separation system at the outlet of the evaporator, which is able to separate non-evaporated working fluid from evaporated working fluid, wherein the water separation system comprises a separator and a bottle, which are designed as separate containers, wherein a return line from the separator opens into a point of connection of the evaporator and a working-medium outlet for the return line in the separator is situated so far above the point of connection that a geodetic return of the non-evaporated working fluid into the evaporator via the return line is possible, wherein furthermore, a drain line branches off from the separator and opens into the bottle and is arranged in the water separation system such that it is arranged, at least in part, above the return line.
If more water arrives at the separator than can flow back into the evaporator, the fill level in the separator will rise up to a point defined by the arrangement of the drain line and then automatically flow off into the bottle. This water which flows off into the water bottle is discharged in the hitherto known manner.
In one advantageous embodiment, a shut-off fitting is arranged in the return line, with the result that, upon ending of the water expulsion, the return line to the evaporator can be closed.
It is furthermore advantageous for a check valve to be arranged in the return line, with the result that the flow of the non-evaporated working fluid is also possible only in one direction, specifically from the water separation system to the evaporator.
In one advantageous embodiment, the drain line comprises a pipe which projects into the separator through the bottom of the separator.
It is furthermore advantageous for a first evacuation line to be arranged at a lower end of the separator, and to open into the bottle, such that it is possible for the separator to be evacuated as completely as possible.
It may also be advantageous if one part of the drain line between the separator and the bottle is formed in a siphon-like manner and, at its lowest point, is provided with a second evacuation line, which opens into the bottle.
The stated embodiments all have the advantage that return and drainage are realized automatically and result from the geometry of the water separation system, and no active regulation is necessary, such as for example in the case of a solution in which, in the return line, there is arranged a valve arrangement with the function of a three-way valve, from which one line branches off into the bottle.
The invention will be discussed in more detail by way of example on the basis of the drawings. In the drawings, in each case schematically and not to scale:
In the embodiment in
As soon as, during startup, the water expelled from the evaporator 2 arrives in the separator 4 and is separated out, this water can flow back into the evaporator 2. The efficiency of this measure increases if the evaporator 2 is not completely filled for the startup. If more water arrives at the separator 4 than can flow back into the evaporator 2, the fill level in the separator 4 will rise up to the overflow 21 into the water bottle 5. This water which overflows into the water bottle 5 from the separator 4 via a drain line 12 is discharged in the hitherto known manner. If the water expulsion has ended (pressure rise in the system), the shut-off fitting 6 in the return line 9 to the evaporator 2 is closed. A second first evacuation line 16, of smallest possible design, from the separator 4 to the water bottle 5 serves exclusively to evacuate the separator 4 as completely as possible during operation and while the installation is at a standstill.
The embodiment in
The embodiment in
Number | Date | Country | Kind |
---|---|---|---|
10 2017 205 382.8 | Mar 2017 | DE | national |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/EP2018/056199 | 3/13/2018 | WO |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2018/177738 | 10/4/2018 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
3532453 | Zipay | Oct 1970 | A |
4129140 | Carlin | Dec 1978 | A |
4520762 | Martin | Jun 1985 | A |
5588400 | Stefan et al. | Dec 1996 | A |
5839396 | Franke | Nov 1998 | A |
6173679 | Bruckner | Jan 2001 | B1 |
20140014189 | Brodesser et al. | Jan 2014 | A1 |
Number | Date | Country |
---|---|---|
103459926 | Dec 2013 | CN |
3236979 | Apr 1984 | DE |
4303613 | Aug 1994 | DE |
19702133 | Dec 1997 | DE |
0544615 | Jun 1993 | EP |
0812407 | Dec 1997 | EP |
S4818082 | Mar 1973 | JP |
S59209628 | Nov 1984 | JP |
S59209628 | Nov 1984 | JP |
S61228201 | Oct 1986 | JP |
S61228201 | Oct 1986 | JP |
2007315726 | Dec 2007 | JP |
2007315726 | Dec 2007 | JP |
2008151503 | Jul 2008 | JP |
9709565 | Mar 1997 | WO |
9730312 | Aug 1997 | WO |
Entry |
---|
English Translation of JP-2007315726-A, dated Mar. 15, 2022 (Year: 2022). |
English Translation of JPS61228201A, dated Mar. 15, 2022 (Year: 2022). |
English Translation of JPS59209628A, dated Mar. 15, 2022 (Year: 2022). |
Weiss, T.: “Das dynamische Verhalten eines Abhitzedampferzeugers mit Zwangsdurchlauf”: Dusseldorf: VDI Verlag 2003 (Reihe 6); pp. 10, 12, 15-17; ISBN 3-18-349806; The dynamic behavior of a forced heat recovery steam generator; ENGLISH Machine translation attached. |
PCT International Search Report and Written Opinion of International Search Authority dated Jul. 23, 2018 corresponding to PCT International Application No. PCT /E P201 8/056199 filed Mar. 13, 2018. |
Number | Date | Country | |
---|---|---|---|
20210131312 A1 | May 2021 | US |