The present invention refers to a method for the start up and management of a combined cycle thermal plant for energy production according to the preamble of claim 1.
Within the range of the present invention, expressions like “functional group” and similar expressions indicate a precisely set sequence of successive operations automatically operated and linked between them; substantially said expressions are used to indicate a macroinstruction formed by a plurality of minor instructions linked between them both functionally and temporally.
Furthermore, within the range of the present invention the term “bottling” when referred to a recovery steam generator is used to indicate a series of activities as a whole destined to insulate the steam generator itself and its thermal cycle as much as possible from the outer environment and further components with a view to keep all the accumulated heat inside. The bottling operation is carried out by appropriately operating on the insulating systems of the plant (valves, dampers, etc.).
Plants for the production of electric energy of the above specified type, are also known as combined cycle plants since they have a recovery steam cycle subordinate to a first thermal cycle through which they generate electric energy by exploiting one or more gas and generator turbine groups. These plant are widespread nowadays thanks to their high flexibility of use allowing to change within a very large percentage range and in a reasonable lapse of time the quantity of energy produced, while maintaining a good total efficiency when the plant has reached substantial operating conditions.
Furthermore, it is pointed out that combined cycle thermal plants for the production of electric energy can be stopped and started up again within a reduced lapse of time.
A very critical state for combined cycle plants for the production of electric energy is the so called transient state, i.e. the phases where the plant changes its operational status. Transient states during the plant functioning may be:
It is almost unnecessary to remark that aforementioned transient states during the plant functioning are critical from the point of view of:
Moreover, the transient states are critical even when considering the total efficiency of the plant, namely during the start-up phases.
Furthermore, it must be underlined how the greater part of pollution emissions are freed during the transient state of the plant starting from an off-state.
From the above said it highlights the need to operate the plant with start-up and stop sequences which:
Nowadays, said concerted implementation of the correct sequence of functional groups depends on the technicians' experience who follow and implement a written sequence of functional groups conceived on purpose for a specific plant. To this respect it is useful to underline that, even when formally correct as for the linkage, the functional groups sequence is carried out according to the timing decided step by step by the plant technician who, judging from his personal experience, and evaluating from time to time the specific physical and operational parameters detected in the plant, decides on the basis of his personal experience which are the operations to switch on the different components involved in the start-up.
This procedure is not satisfactory both because it requires the attendance of a plant technician having a long experience with the specific plant to be started/stopped and because, it goes without saying, different technicians will implement different start-up timings which, even though correct, do not always allow optimizing the procedure and, at the same time, satisfying said need.
The problem at the basis of the present invention is that of devising and developing a method to optimize the start up and/or stopping sequences, partially or totally, of combined cycle thermal plants for the production of electric energy once the functional groups known, i.e. the specific operations to be carried out to operate the start up or the stopping of the specific components of the plant. This problem is solved by a method for the start up and management of a combined cycle thermal plant for energy production according to claim 1.
According to a further aspect, said problem is also solved by a combined cycle thermal plant for energy production according to claim 7, being suitable to implement the following method.
Further features and advantages of the method according to this invention and of the plant according to this invention will enhance from the description hereinafter detailed of some preferred example embodiments thereof, given for indicating and not limiting purposes, with reference to
According to the above stated, the thermal plant for energy production comprises:
According to this invention the plant also comprises valve means and similar means opening or closing which it is possible to change the working conditions of the plant. Said valve means are not illustrated in the figure scheme and are not detailed hereinafter since they are components well known to a technician of the sector.
Furthermore, according to this invention the plant comprises detection and check means to monitor and detect a plurality of parameters connected to the correct functioning and/or malfunctioning of said plant, particularly of the first and second gas turbine and generator groups TG1 and TG2, of the first and second steam generators GRV1 and GRV2 and of the steam turbine TV.
Advantageously, according to this invention the plant comprises a control and processing unit DCS (not illustrated for the sake of simplicity of representation) where to memorize:
Advantageously, said control and processing unit is connected to said detection and check means in order to:
As above detailed, in the plant control and processing unit in addition to the functional groups it is possible to memorize also the sequences of functional groups, i.e. more functional groups linked between them according to an optimal and set sequence, corresponding to the different start up or stop procedures, both total or partial, of the plant according to the invention. At the same time, in said plant control and processing unit it is also possible to memorize the specific and different local conditions in the different plant components and in the remaining parts of the plant itself to be detected to give the green light for execution of the functional groups still to be executed. This is possible thanks to the fact that the plant control and processing unit continuously detects the specific and different local conditions of the plant components and in the remaining parts of the plant itself while comparing the detected values with the reference values (i.e. suitable to give the green light) and by finding a value correspondence allows the automatic starting of the following functional groups of the specific start/stop sequence required. Substantially, the plant control and processing unit allows the automatic and linked execution of the different functional groups that compose the required sequence thanks to a systematic and automatic control suitable to give the green light to the execution of a specific functional group as soon as the values detected by the control and detection means meet the requirements memorized in the control and processing unit to give the consensus for the execution of the functional groups still to be executed.
Therefore, in the plant according to this invention, the linkage between the different functional groups necessary to have a start or stop sequence, total or partial, of the plant does not depend anymore on the experience and free will of the plant operator, but is assured in its best and repeatable form, by the control and processing unit of the plant.
We will detail hereinafter some preferred example embodiments according to this invention in relation to some sequences of functional groups necessary to pass from a first operational configuration to a second operational configuration.
A. Start-up of a First as Turbine and Generator Group TG1 and of the Steam Turbine TV from an Off State.
The start up phases of a first gas turbine and generator group TG1 and of the steam turbine TV of the plant comprise the following functional groups sequence:
In the plant according to this invention, this start up sequence is characterized in that it comprises the following phases:
The start-up phases of a second gas turbine and generator group TG2 comprise, in order, the following sequence of functional groups:
In the plant according to the invention, said start up sequence is characterized in that it comprises the following phases:
The stopping phases of the second gas turbine and generator group TG2 and of the second steam generator GRV2 while the first gas turbine and generator group TG1 and steam turbine TV are still working comprise the following sequence of functional groups:
In the plant according to this invention, this stop sequence is characterized in that it comprises the following phases:
Preferably, said functional group GF3B (stopping of the second gas turbine and generator group TG2) comprises a simultaneous bottling of the second steam generator GRV2 to keep steam pressure and temperature as long as possible inside.
D. Total Stop of the Plant Starting from a Condition Where Only the First as Turbine and Generator TG1 and the Steam Turbine TV are Working
The total stop phases of the plant starting from a condition where only the first gas turbine and generator TG1 and the steam turbine TV are working comprise the following sequence of functional groups:
In the plant according to this invention, this stop sequence is characterized in that it comprises the following phases:
Preferably said functional group GF1B (stopping of said first gas turbine and generator group TG1) comprises a simultaneous bottling of the first steam generator GRV1 to keep steam pressure and temperature as long as possible inside.
As can be appreciated from what has been described, the method according to the present invention, and the plant according to the present invention, allow meeting above mentioned need and at the same time overcoming the drawbacks referred to in the introductory part of the present description with reference to the prior art. As a matter of fact, as already mentioned, the linkage between the different functional groups necessary to have a start or stop sequence, is not left anymore to the free will of the plant's operator, but is guaranteed in an optimal and repeatable way, by the control and processing unit of the plant.
Obviously, a technical expert, may apply several modifications and arrangements to the above detailed method and plant in order to satisfy contingent and specific needs but without exceeding the range of the protection of the present invention as defined by the following claims.
Number | Date | Country | Kind |
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MI2010A002463 | Dec 2010 | IT | national |
MI2010A002481 | Dec 2010 | IT | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB11/56026 | 12/30/2011 | WO | 00 | 9/13/2013 |