Continuous steam generator with equalizing chamber
09581327 ยท 2017-02-28
Assignee
Inventors
- Donald W. Bairley (Farmington, CT, US)
- Wesley P. Bauver, II (Granville, MA, US)
- Thomas P. Mastronarde (West Hartford, CT, US)
Cpc classification
F22B37/227
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F22B29/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F22B37/22
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
An evaporator 10 for evaporating a liquid includes a plurality of harps 20 disposed within a duct or chamber such that a heated fluid flow 22 (e.g., heated gas or flue gas) passes through each successive row of harps 20 of the evaporator 10. Each of the harps 20 includes a lower header 24, a plurality of lower tubes 26, an intermediate equalizing chamber 28, a plurality of upper tubes 30, and an upper header 32. The lower tubes 30 are in fluid communication with the lower header 24 and extend upward vertically from the lower header. The upper ends of the lower tubes 26 are in fluid communication with the equalizing chamber 28. The upper tubes 30 are in fluid communication with the equalizing chamber 28 and extend upward vertically from the equalizing chamber. The upper ends of the upper tubes 30 are in fluid communication with the upper header 32.
Claims
1. An evaporator for evaporating a liquid in a heat recovery steam generator, the evaporator comprising: a duct having a heated fluid flow passing therethrough in a flow direction, and a harp having a portion disposed transversely in the duct, the harp including: a lower header with a liquid input pipe; plurality of lower tubes, each having an upper end and a lower end, the lower ends of the lower tubes being fluidly connected to the lower header; an intermediate chamber fluidly connected to the upper ends of the lower tubes, plurality of upper tubes having an upper end and a lower end, the lower ends of the upper tubes being fluidly connected to the intermediate chamber; and an upper header fluidly connected to the upper ends of the upper tubes; wherein the plurality of upper tubes, the plurality of lower tubes and the intermediate chamber are disposed in the duct transversely to the flow direction of the heated fluid flow, and wherein the flow direction of the heated fluid below the intermediate chamber is in the same direction as the flow direction of the heated fluid above the intermediate chamber; and wherein the plurality of upper tubes and the respective plurality of lower tubes are vertically offset for promoting mixing of the fluid and steam in the intermediate chamber before passing through the plurality of upper tubes.
2. The evaporator of claim 1, wherein the lower tubes are substantially vertically disposed between the lower header and the intermediate chamber.
3. The evaporator of claim 1, wherein the upper tubes are substantially vertically disposed between the intermediate chamber and the upper header.
4. The evaporator of claim 1, wherein each upper and/or lower tube includes a set of tubes, wherein the tubes of each respective set of tubes are sequentially disposed in a respective plane downstream of and transverse to the heated fluid flow.
5. The evaporator of claim 4, wherein the tubes in sequential arrangement are aligned and/or staggered in the direction of the heated fluid flow.
6. The evaporator of claim 1, wherein the intermediate chamber receives a plurality of upper tubes and lower tubes sequentially disposed in a respective plane downstream of and transverse to the heated fluid flow.
7. An evaporator for evaporating a liquid in a heat recovery steam generator, the evaporator comprising: a duct having a heated fluid flow passing therethrough in a flow direction, and a plurality of harps disposed sequentially in the duct in the flow direction, wherein a portion of each harp is disposed transversely in the duct, each harp including: a lower header with a liquid input pipe; a plurality of lower tubes, each having an upper end and a lower end, the lower ends of the lower tubes being fluidly connected to the lower header; an intermediate chamber fluidly connected to the upper ends of the lower tubes, plurality of upper tubes having an upper end and a lower end, the lower ends of the upper tubes being fluidly connected to the intermediate chamber; and an upper header fluidly connected to the upper ends of the upper tubes; wherein the plurality of upper tubes, the plurality of lower tubes and the intermediate chamber are disposed in the duct transversely to the flow direction of the heated fluid flow, and wherein the flow direction of the heated fluid below the intermediate chamber is in the same direction as the flow direction of the heated fluid above the intermediate chamber; and wherein the upper tubes of each harp and respective lower tubes of each harp are vertically offset.
8. The evaporator of claim 7, wherein the lower tubes of each harp are substantially vertically disposed between each respective lower header and the intermediate chamber.
9. The evaporator of claim 7, wherein the upper tubes of each harp are substantially vertically disposed between each respective intermediate chamber and the upper header.
10. The evaporator of claim 7, wherein each upper and/or lower tube of each harp includes a set of tubes, wherein the tubes of each respective set of tubes are sequentially disposed in a respective plane downstream of and transverse to the heated fluid flow.
11. The evaporator of claim 10, wherein the tubes of each harp in sequential arrangement are aligned and/or staggered in relation to the direction of the heated fluid flow.
12. The evaporator of claim 7, wherein the plurality of harps are fluidly interconnected in parallel.
13. The evaporator of claim 7, wherein the plurality of harps are fluidly interconnected in series.
14. The evaporator of claim 1, wherein the lower header and the upper header are located outside of the duct.
15. The evaporator of claim 7, wherein the lower header and the upper header are located outside of the duct.
16. An evaporator for evaporating a liquid in a heat recovery steam generator, the evaporator comprising: a duct having a heated fluid flow passing therethrough in a single flow direction, and a harp having a portion disposed transversely in the duct, the harp including: a lower header with a liquid input pipe; a plurality of lower tubes, each having an upper end and a lower end, the lower ends of the lower tubes being fluidly connected to the lower header; an intermediate chamber fluidly connected to the upper ends of the lower tubes, a plurality of upper tubes having an upper end and a lower end, the lower ends of the upper tubes being fluidly connected to the intermediate chamber; and an upper header fluidly connected to the upper ends of the upper tubes; wherein the heated fluid flow passes through the harp in a single direction, wherein the flow direction of the heated fluid below the intermediate chamber is in the same direction as the flow direction of the heated fluid above the intermediate chamber; and wherein the plurality of upper tubes and the plurality of lower tubes are vertically offset for promoting mixing of the fluid and steam in the intermediate chamber before passing through the plurality of upper tubes.
17. The evaporator of claim 1, wherein the heated fluid flow passes through the harp in a single direction.
18. The evaporator of claim 1, wherein a plane of the heated fluid flow passes through the plurality of upper tubes and the plurality of lower tubes at substantially the same time.
19. The evaporator of claim 1, wherein the heated fluid flow passes through the harp in a single and substantially horizontal direction.
20. The evaporator of claim 1, wherein the heated fluid flow passes through the harp once.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) Referring now to the figures, which are exemplary embodiments, and wherein the like elements are numbered alike:
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DETAILED DESCRIPTION
(12) For convenience in the description of the present invention, the present invention is described hereafter as an evaporator used in conjunction with a boiler or within a power plant. However, one skilled in the art will appreciate that the evaporator may be used for any application requiring evaporation of a liquid or superheating of a gas.
(13) As best shown in
(14) Referring to
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(16) The present invention introduces the equalizing chamber 28 at an optimum location in the vertical tubes 26,30 of the primary and/or secondary evaporator 12,14 to reduce the differential temperature in adjacent tubes of a respective harp 20. This favorable effect may be achieved in both the lower two-phase section of the evaporator tube (i.e., the lower primary stage 16) or the upper section (i.e., the upper secondary stage 18). The equalizing chamber 28 may be a cylindrical chamber with cross sectional area large compared to one tube cross sectional area to facilitate mixing of flows from the individual tubes.
(17) In the operation of the two-stage evaporator 10, a liquid (e.g., water) is provided to the input pipes 34 of the primary evaporator 12. The water is provided to the tubes of the lower primary stage 16 via the input header 24. The water is then heated to form a water/steam mixture therein, which is provided to the equalizing chamber 28 where the mixture exiting from each tube 26 mixes together. The equalizing chamber 28 of a harp blends the different steam water fractions from adjacent tubes 26 exiting from the lower primary stage 16 of the harp 20. This blending of different steam/water fractions promotes a more uniform blend quality exiting the equalizing chamber 28 to the tubes 30 of the upper secondary stage 18 of the harp 20. In the upper secondary stage 18 of the harp 20, mixing of flow streams with different steam temperatures in the intermediate equalizing chamber 28 will promote more uniform temperature entering the tubes 30 of the upper secondary stage 18 of the harp. Consequently, the heated or superheated gas entering the upper header 32 of the harp 20 is more uniform in temperature.
(18) The advantages of the equalizing chamber 28 in the primary evaporator 12 of the two-stage evaporator 10 are the same for providing an equalizing chamber 28 in the secondary evaporator 14. Ultimately, the addition of an equalizing chamber(s) 28 results in the temperature of the final superheated gas at the inlet to the upper headers 32 of the secondary evaporator 14 will be more uniform when an equalizing chamber 28 is introduced into the evaporator tube flow path. As a result, the differential thermal stresses will be reduced during startup and load ramps, extending the life of the evaporator tube-to-header connections.
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(23) While in each of the embodiments the headers are shown disposed external to the duct, the present invention contemplates that the the upper and/or lower headers may be disposed within the duct.
(24) While the invention has been described with reference to various exemplary embodiments, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the invention without departing from the essential scope thereof. Therefore, it is intended that the invention not be limited to the particular embodiment disclosed as the best mode contemplated for carrying out this invention, but that the invention will include all embodiments falling within the scope of the appended claims.