This application claims priority to European application 13190995.4 filed Oct. 31, 2013, the contents of which are hereby incorporated in its entirety.
The present disclosure relates to Combined Cycle Power Plants (CCPP), and, more particularly, to feedwater preheating system and method for preheating feedwater to be fed into a Heat Recovery Steam Generator (HRSG) in the CCPP.
Where equipped, in Combined Cycle Power Plants (CCPP), feedwater heating systems are generally used to preheat water delivered Heat Recovery Steam Generators (HRSG) to up to or above a fixed minimum temperature required at the HRSG. Preheating the feedwater reduces the irreversibilities involved in steam generation in the HRSG and improves the thermodynamic efficiency of the CCPP. Among various others advantages of the preheating feedwater, such preheating also helps avoiding corrosion caused by flue gas condensation on outer tubes surface in inside the HRSG.
For the CCPP equipped with the feedwater heating systems, the preheating is achieved by different heating source, such as, pegging steam extracted from the HRSG, steam turbine extraction either in a condensate preheater, a separate feedwater preheater, feedwater recirculation from an economizer extraction or recirculation of feedwater in a dedicated HRSG coil at a cold end of the HRSG. A philosophy of the mentioned state of the art concepts is to control a fixed temperature, generally, in the feedwater tank.
A prior art
Using any such heating source may constantly affects the CCPP efficiency since the energy used to heat the feedwater is usually derived from a main steam source (CRH, LP, etc.) or extracted between the stages of the steam turbine. Therefore, the steam that would be used to perform expansion work in the turbine (and therefore generate power) is not utilized for that purpose. The percentage of the total cycle steam mass flow used for the feedwater heating must be carefully optimized for maximum CCPP efficiency since increasing in fraction of this steam causes a decrease in the CCPP efficiency.
Accordingly, there exists a need to minimize or preclude the need of utilizing such heating stream to heat the feedwater for heating HRSG to maximize efficiency of the CCPP.
The present disclosure describes improved feedwater preheating system and method, that will be presented in the following simplified summary to provide a basic understanding of one or more aspects of the disclosure that are intended to overcome the discussed drawbacks, but to include all advantages thereof, along with providing some additional advantages. This summary is not an extensive overview of the disclosure. It is intended to neither identify key or critical elements of the disclosure, nor to delineate the scope of the present disclosure. Rather, the sole purpose of this summary is to present some concepts of the disclosure, its aspects and advantages in a simplified form as a prelude to the more detailed description that is presented hereinafter.
An object of the present disclosure is to describe improved feedwater preheating systems and methods, which may minimize or preclude the need of utilizing high energetics heating stream to heat the feedwater to maximize efficiency of a Combined Cycle Power Plants (CCPP). Such improved feedwater preheating systems and methods may equally be capable in preventing corrosion caused by flue gas condensation on outer tubes surface in inside the HRSG. Further, object of the present disclosure is to describe an improved feedwater preheating systems and methods, which may be convenient to use in an effective and economical way. Various other objects and features of the present disclosure will be apparent from the following detailed description and claims.
The above noted and other objects, in one aspect, may be achieved by an improved feedwater preheating system. The feedwater preheating system is adapted to preheat feedwater to be fed into a Heat Recovery Steam Generator (HRSG). The feedwater preheating system includes a feedwater tank and a constant volume recirculation pump. The feedwater tank is adapted to store the feedwater. The feedwater tank includes a feed line and a return line. The feed line is adapted to feed the feedwater to the HRSG, and the return line adapted to enable returning of the feedwater into the feedwater tank. The return line precludes a control valve to reduce component loss while feedwater recirculation. Further, the constant volume recirculation pump is configured in the feed line to recirculate the feedwater between the HRSG and the feedwater tank. The constant volume recirculation pump recirculate the feedwater at constant speed and volume to reduce heat loss while feedwater recirculation, thereby increasing efficiency of the HRSG.
In one embodiment of the present disclosure, the feedwater is maintained above or at a minimum set temperature, defined during the design based on the sulphur/water content in the flue gas. In such embodiment, preclusion of the control valve from the return line and inclusion of the constant volume recirculation pump, instead of variable volume recirculation pump, enable the feedwater preheating system to recirculate the feedwater at constant speed and volume, reducing heat loss while feedwater recirculation, and maintaining the minimum set temperature of the feedwater, as set during designing.
In further embodiment of the present disclosure, instead of defining the minimum set temperature during the design, as in the above embodiment, the feedwater is maintained at a temperature, a required minimum or above set temperature, as required by the HRSG during operation. As per this embodiment, a Continuous Emission Monitoring System (CEMS) circuit or any other measuring device, such as dedicated water/acid dew point measurement device, is configured to the HRSG to enable calculation of the required minimum set temperature, based on parameters of the HRSG, at which the feedwater is required to be kept for recirculation in the HRSG. In this embodiment, preclusion of the control valve from the return line and inclusion of the constant volume recirculation pump, to recirculate the feedwater at constant speed and volume, reduce heat loss while feedwater recirculation, and maintain the required minimum set temperature of the feedwater, as calculated by the CEMS circuit.
In both the embodiments, the feedwater preheating system includes an optional provision of a pegging steam line source to supply pegging steam to the feedwater tank to preheat the feedwater up to the minimum temperature set during the designing or up to the required minimum set temperature calculated by the CEMS circuit. As and when the temperature of the feedwater in the feedwater tank reaches below the minimum set temperature or below the required calculated minimum set temperature, the pegging steam line source may be activated to attain the feedwater temperature requirement. Such control and reduced use of the pegging steam is capable of increasing efficiency of the HRSG and hence of the CCSS.
Both embodiments of the feedwater preheating system includes a control valve configured in the pegging steam source line to close and open the pegging steam source line to supply the pegging steam. Both the embodiments of the system also further includes a temperature control circuit configured to the control valve of the pegging steam source line and to the feedwater tank, to send signals to open and close the control valve based on the temperature of the feedwater tank in order to maintain the minimum set temperature of the feedwater.
In further aspect of the present disclosure, instead of minimizing the pegging steam for preheating the feedwater, it is complete precluded from the feedwater preheating system. In this aspect, the feedwater preheating system includes a feedwater tank, a constant volume recirculation pump and a pressure control means. The feedwater tank includes a feed line and a return line. The feed line is configured to feed the feedwater to the HRSG; and the return line is configured to enable returning of the feedwater into the feedwater tank. The return line precludes the control valve and is configured to the feedwater tank. Further, the constant volume recirculation pump is configured in the feed line to recirculate the feedwater between the HRSG and the feedwater tank. The constant volume recirculation pump is configured to recirculate the feedwater at constant speed and volume to reduce heat loss while feedwater recirculation. Furthermore, the pressure control means is configured to an evaporator of the HRSG to increase an operational pressure of steam in the evaporator to shift heat to the feed line to increase heat gain in the feedwater and maintain a minimum set temperature of the feedwater, thereby precluding the pegging steam requirement for preheating the feedwater as and when required in the above two embodiments, thereby increasing the efficiency of the HRSG.
The feedwater preheating system may further includes a temperature control circuit configured to the pressure control means of the evaporator and to the feedwater tank, to send signals to increase or decrease the operational pressure of the steam in the evaporator based on the temperature of the feedwater tank in order to maintain the minimum set temperature of the feedwater.
In further aspect, methods are disclosed in the present disclosure to be operable in view of the respective feedwater preheating systems.
Such improved feedwater preheating systems, either minimize or preclude the need of utilizing heating stream to heat the feedwater for heating a Heat Recovery Steam Generator (HRSG) to maximize efficiency of a Combined Cycle Power Plants (CCPP). Such improved feedwater preheating systems and methods may equally be capable in preventing corrosion caused by flue gas condensation on outer tubes surface in inside the HRSG. Further, the improved feedwater preheating systems may be convenient to use in an effective and economical way.
These together with the other aspects of the present disclosure, along with the various features of novelty that characterize the present disclosure, are pointed out with particularity in the present disclosure. For a better understanding of the present disclosure, its operating advantages, and its uses, reference should be made to the accompanying drawings and descriptive matter in which there are illustrated exemplary embodiments of the present disclosure.
The advantages and features of the present disclosure will be better understood with reference to the following detailed description and claims taken in conjunction with the accompanying drawing, wherein like elements are identified with like symbols, and in which:
Like reference numerals refer to like parts throughout the description of several views of the drawings.
For a thorough understanding of the present disclosure, reference is to be made to the following detailed description, including the appended claims, in connection with the above described drawings. In the following description, for purposes of explanation, numerous specific details are set forth in order to provide a thorough understanding of the present disclosure. It will be apparent, however, to one skilled in the art that the present disclosure can be practiced without these specific details. In other instances, structures and apparatuses are shown in block diagrams form only, in order to avoid obscuring the disclosure. Reference in this specification to “one embodiment,” “an embodiment,” “another embodiment,” “various embodiments,” means that a particular feature, structure, or characteristic described in connection with the embodiment is included in at least one embodiment of the present disclosure. The appearance of the phrase “in one embodiment” in various places in the specification are not necessarily all referring to the same embodiment, nor are separate or alternative embodiments mutually exclusive of other embodiments. Moreover, various features are described which may be exhibited by some embodiments and not by others. Similarly, various requirements are described which may be requirements for some embodiments but may not be of other embodiment's requirement.
Although the following description contains many specifics for the purposes of illustration, anyone skilled in the art will appreciate that many variations and/or alterations to these details are within the scope of the present disclosure. Similarly, although many of the features of the present disclosure are described in terms of each other, or in conjunction with each other, one skilled in the art will appreciate that many of these features can be provided independently of other features. Accordingly, this description of the present disclosure is set forth without any loss of generality to, and without imposing limitations upon, the present disclosure. The terms “a” and “an” herein do not denote a limitation of quantity, but rather denote the presence of at least one of the referenced item.
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The invention of the present disclosure is advantageous in various scopes. Such improved feedwater preheating systems, either minimize or preclude the need of utilizing heating stream to heat the feedwater for heating a Heat Recovery Steam Generator (HRSG) to maximize efficiency of a Combined Cycle Power Plants (CCPP). Such improved feedwater preheating systems and methods may equally be capable in preventing corrosion caused by flue gas condensation on outer tubes surface in inside the HRSG. Further, the improved feedwater preheating systems may be convenient to use in an effective and economical way. Various other advantages and features of the present disclosure are apparent from the above detailed description and appendage claims.
The foregoing descriptions of specific embodiments of the present disclosure have been presented for purposes of illustration and description. They are not intended to be exhaustive or to limit the present disclosure to the precise forms disclosed, and obviously many modifications and variations are possible in light of the above teaching. The embodiments were chosen and described in order to best explain the principles of the present disclosure and its practical application, to thereby enable others skilled in the art to best utilize the present disclosure and various embodiments with various modifications as are suited to the particular use contemplated. It is understood that various omission and substitutions of equivalents are contemplated as circumstance may suggest or render expedient, but such are intended to cover the application or implementation without departing from the spirit or scope of the claims of the present disclosure.
Number | Date | Country | Kind |
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13190995.4 | Oct 2013 | EP | regional |