CA2501086A1 - Once-through evaporator for a steam generator - Google Patents
Once-through evaporator for a steam generator Download PDFInfo
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- CA2501086A1 CA2501086A1 CA002501086A CA2501086A CA2501086A1 CA 2501086 A1 CA2501086 A1 CA 2501086A1 CA 002501086 A CA002501086 A CA 002501086A CA 2501086 A CA2501086 A CA 2501086A CA 2501086 A1 CA2501086 A1 CA 2501086A1
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- Prior art keywords
- tube
- tape
- evaporator
- tubes
- steam
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B15/00—Water-tube boilers of horizontal type, i.e. the water-tube sets being arranged horizontally
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
- F22B37/10—Water tubes; Accessories therefor
- F22B37/18—Inserts, e.g. for receiving deposits from water
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
- F22B1/1807—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines using the exhaust gases of combustion engines
- F22B1/1815—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines using the exhaust gases of combustion engines using the exhaust gases of gas-turbines
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B29/00—Steam boilers of forced-flow type
- F22B29/06—Steam boilers of forced-flow type of once-through type, i.e. built-up from tubes receiving water at one end and delivering superheated steam at the other end of the tubes
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A steam generator (A) has a once-through evaporator (14) which converts liqu id water into steam in tubes (30) over which hot gases flow. Each tube contains a metal tape (40) which is twisted into a helical configuration to induce turbulence in the mist produced by the boiling, and the turbulence insures that the mist wets the inside surfaces of the tubes, thus producing good hea t transfer and moderate temperatures in the tubes.
Description
ONCE-THROUGH EVAPORATOR FOR A STEAM GENERATOR
Cross-Reference to Related Applications This application derives and claims priority from U.S. Provisional Application Serial No. 60/416,083, filed October 4, 2002.
Technical Field This invention relates in general to steam generators and, more particularly, to an evaporator for a steam generator and tubing for such an evaporator.
Background Art Steam finds widespread use in industry, perhaps the most important of these uses being the generation of electrical power. Typically, hot gases, in many instances generated by combustion, pass through a steam generator which converts water into superheated steam. Representative of these installations are heat recovery steam generators (HRSGs) which are used to extract heat from the hot gases discharged by gas turbines that drive electrical generators. The heat extracted produces steam which passes on to a steam turbine that powers another electrical generator.
The typical steam generator, aside from a duct through which the hot gases pass, in its most basic form, includes three additional components namely, a superheater, an evaporator, and an economizer or feedwater heater arranged in that order with respect to the flow of gases in the duct.
The water flows in the opposite direction, that is through the economizer where it is heated, but remains a liquid, then through the evaporator where it is converted into mostly saturated steam, and then through the superheater where the saturated steam becomes superheated steam.
Evaporators come in two basic configurations - the circulation type and the once-through type - each with its own advantages and disadvantages. Both have an array of tubes in the duct through which the hot gases pass.
In the circulation type, the tubes reside in a circuit with a steam drum that is above the tubes. The drum contains water which flows from the drum, through a downcomer, and then into the tubes where some of it is converted into steam, but the steam exists as bubbles within the water, and is returned through a riser into the steam drum. Here the steam, which is saturated, separates from the liquid water and passes on to the superheater. It is replaced by feedwater which is supplied to the drum. The tubes of a circulation evaporator remain wet all the time - that is to say, liquid water exists against their interior surfaces throughout. This promotes good heat transfer. It also maintains the tubes at relatively moderate temperatures, thus eliminating the need for high temperatures alloys in the tubing.
But circulation evaporators have their detractions. Perhaps the greatest of these is the expense attributable to steam drums, large downcomers, and headers to supply water to their tubes. Moreover, the reservoirs of water contained in them require time to bring up the boiling temperature, so the start-up time for a circulation evaporator is extended.
Once-through evaporators do not require downcomers or drums and are less expensive to manufacture. Moreover, the only stored water in them resides in the tubes themselves and the supply header from which the tubes extend. This enables a once-through evaporator to be brought to operating conditions more rapidly than a natural circulation evaporator. However, a once-through evaporator must completely convert the water into steam, so that only steam escapes from its tubes and flows on to the superheater. No liquid water should leave the evaporator. The evaporator relies on a feedwater pump located upstream in the water circuit to circulate water through it at a controlled rate - a rate that if correct allows the steam to leave in a saturated or a slightly superheated condition.
Thus, in a once-through evaporator the tube walls nearest to the water inlet run wet as in a circulation type evaporator, because these ends of the tube see only liquid water. But farther on in the tubes the water turns into a mist and then into saturated steam. In the mist flow regime, water is sheered from the interior surfaces of the tube walls, so the mist exists in cores which extend through the centers of the tubes. The walls around these cores run dry. This produces higher temperature in the tube walls and less efficient heat transfer. The higher temperatures may require metals that are better able to withstand these temperatures or, in other words, a resort to expensive high alloy steels.
Brief Description of Drawings Figure 1 is a schematic sectional view of a steam generator equipped with a once-through evaporator constructed in accordance with and embodying the present invention;
Figure 2 is a perspective view of the evaporator;
Figure 3 is a sectional view taken along line 3-3 of Fig. 2;
Figure 4 is a fragmentary sectional view of the end of one of the evaporator tubes showing a twisted tape anchored in the tube;
Figure 5 is a fragmentary sectional view similar to Fig. 4, but rotated 90°; and Figure 6 is a fragmentary view of one of the evaporator tubes, partially cut away and in section, showing the flow in the tube.
Best Mode for Carrying Out the Invention Referring now to the drawings, a steam generator A (Fig. 1 ) basically includes a duct 2 having an inlet end 4 and a discharge end 6. The inlet end 4 is connected to a source of hot gases, such as a gas turbine or an incinerator, and those gases flow through the duct 12, leaving it at the discharged end 6. In addition, a steam generator A includes a superheater 12, an evaporator 14, and a feedwater heater or economizer 16 arranged in the duct 2 in that order from the inlet end 4 of the outlet end 6. Thus, the hot gases flow first through the superheater 12, then through the evaporator 14, and finally through the economizer 16. Water flows in the opposite direction. To this end, the economizer 16 is connected to a feedwater pump 18 which delivers feedwater to the economizer 16. It extracts heat from the hot gases and transfers that heat to the liquid water that flows through it, thereby elevating the temperature of the water, but the water remains a liquid. Leaving the economizer 16, the liquid water then flows to the evaporator 14 through which it passes. The evaporator 14 converts the water to steam, mostly saturated steam. The steam flows into the superheater 12 which raises its temperature, transforming it into superheated steam that may be used to power a turbine or in some industrial process or even to heat a building. The superheater 12, evaporator 14, and economizer 16 are basically tube banks. The evaporator 14 operates on the once-through principle. Actually, the steam generator A may have more than one evaporator 14.
The evaporator 14 includes (Fig. 2) a supply header 26, a discharge header 28 and tubes 30 which extend between the two headers 26 and 28.
The supply header 26 has an inlet port 32 that is connected to the economizer 16 and receives heated water from the economizer 16 - indeed, water which is delivered to it under the head produced by the pump 18. The discharge header 26 has outlet ports 34 which are connected to the superheater 12, and through the ports 34 steam, that is saturated or slightly superheated, is directed to the superheater 12. The tubes 30 have fins 36 which facilitate the extraction of heat from the gases flowing through the duct 2.
Within the tubes 30 the heated water from supply header 26 is converted into the steam which collects within the discharge header 28 and then passes on to the superheater 12. Thus, the portion of each tube 30 that is closest to the supply header 20 contains liquid water, while the portion that is closest to the discharge header 28 contains steam that is saturated and perhaps even slightly superheated. In the intermediate portion of each tube 30 the liquid water undergoes the change of phase and becomes steam. Here the water boils, becoming a mist or a mixture of water and saturated steam. Further along the mist becomes saturated steam, and finally the saturated steam may become superheated steam, albeit only slightly superheated. The superheated region of the tube 30, if indeed there is superheated steam, is quite short. The tubes 30 are formed from carbon steel or chrome-moly steel.
Each tube 30 contains a helical tape 40 (Figs. 3-5) which extends from its inlet and, that is its end which is connected to the supply header 26, through the regions in which the mist exists. The width of each tape 30 is slightly less than the inside diameter of the tube 30 through which it extends, so that the tape 40 can be inserted into or withdrawn from the tube 30 without interference from the tube 30 itself. Preferably, the width of each tape 40 should be about 1/16 inches smaller than the inside diameter of its tube 30, at least for a tube having a 2 inch inside diameter. The tape 40 is twisted multiple times between its ends, so that its edges form helices that lie along the inside surface of the tube 30. Indeed, a full 360° twist of the tape 40 should occur within a distance amounting to a length to diameter of 5 to 25. For example, for a tube 30 having a 2 inch inside diameter and a length to diameter ratio of 5 for the twist in its tape 40, a full 360°
twist of the tape 40 will occur in 10 inches of the tube 40. That end of the tape 40 that resides at the inlet of the tube 30 is fitted with an anchor bar 42 that extends transversely across like inlet end of the tube 32. The bar 42 is welded to the end of the tube 30 and to the tape 40, thus anchoring the tape 40 with its tube 30. The tapes 40 are formed from a metal that can withstand the temperatures associated with slightly superheated steam and are further compatible with the metal of the tube 30 in the sense electrolytic reactions are minimized. Stainless steel is suitable when the tubes 30 are carbon steel.
In the operation of the steam generator A, hot gases flowing through the duct 2 pass over the tubes of the superheater 12, the evaporator 14 and the economizer 16 in that order and at each undergo a reduction in temperature. The feedwater pump 18 forces water into and through the economizer 16 where the water extracts heat from the gases that flow over the tubes of the economizer 16. The temperature of the water rises, but the water remains in the liquid phase. Under the head produced by the pump 18, the water flows from the economizer 16 into the supply header 26 of the evaporator 14 and then into the tubes 30 of the evaporator 14. Within the tubes 30, the water encounters even higher temperatures derived from the gases passing through the duct 2. Indeed, the gases passing through the evaporator 14 elevate the temperature of the tubes 30 high enough to convert the water in the tubes 30 to steam. The water, initially upon entering the tubes 30, remains in the liquid phase, but as it flows through the tubes 30 it begins to boil, producing a mist. The tapes 40 extend through the region of mist flow and produce a good measure of turbulence in the mist as it flows on toward the discharge header 28. The turbulence brings the mist, that is to say the water particles, against the inside surfaces of the tubes (Fig. 6), thereby effecting better and more efficient transfer of heat between the gases flowing over the tubes 30 and the mist in the tubes 30. This further protects the tubes 30 from overheating. Were it not for the tapes 40, the mist would tend to remain in the center of the tubes 30 and would be surrounded by saturated or superheated steam along the interior surfaces of the tubes 30, thus causing the tubes 30 in the regions of the mist to operate at higher temperatures. As the mist in the tubes 30 flows on and approaches the discharge header 28 it transforms into saturated steam and may even change to superheated steam, albeit only slightly superheated.
But the regions of the tubes 30 that see only superheated steam are short and are maintained at relatively moderate temperatures by reason of heat conducted from them to the regions occupied by the mist and the liquid water.
In lieu of anchoring the tapes 40 to the tubes 30 at the supply header 26, they may be anchored at the discharge header 28, in which event they will extend toward the supply header 26. The tapes 40 may extend the full lengths of the tubes 30 through which they pass or only through the regions of mist flow. The evaporator 14 in lieu of having its tubes 30 arranged in a single bank, may have them organized in multiple banks.
Cross-Reference to Related Applications This application derives and claims priority from U.S. Provisional Application Serial No. 60/416,083, filed October 4, 2002.
Technical Field This invention relates in general to steam generators and, more particularly, to an evaporator for a steam generator and tubing for such an evaporator.
Background Art Steam finds widespread use in industry, perhaps the most important of these uses being the generation of electrical power. Typically, hot gases, in many instances generated by combustion, pass through a steam generator which converts water into superheated steam. Representative of these installations are heat recovery steam generators (HRSGs) which are used to extract heat from the hot gases discharged by gas turbines that drive electrical generators. The heat extracted produces steam which passes on to a steam turbine that powers another electrical generator.
The typical steam generator, aside from a duct through which the hot gases pass, in its most basic form, includes three additional components namely, a superheater, an evaporator, and an economizer or feedwater heater arranged in that order with respect to the flow of gases in the duct.
The water flows in the opposite direction, that is through the economizer where it is heated, but remains a liquid, then through the evaporator where it is converted into mostly saturated steam, and then through the superheater where the saturated steam becomes superheated steam.
Evaporators come in two basic configurations - the circulation type and the once-through type - each with its own advantages and disadvantages. Both have an array of tubes in the duct through which the hot gases pass.
In the circulation type, the tubes reside in a circuit with a steam drum that is above the tubes. The drum contains water which flows from the drum, through a downcomer, and then into the tubes where some of it is converted into steam, but the steam exists as bubbles within the water, and is returned through a riser into the steam drum. Here the steam, which is saturated, separates from the liquid water and passes on to the superheater. It is replaced by feedwater which is supplied to the drum. The tubes of a circulation evaporator remain wet all the time - that is to say, liquid water exists against their interior surfaces throughout. This promotes good heat transfer. It also maintains the tubes at relatively moderate temperatures, thus eliminating the need for high temperatures alloys in the tubing.
But circulation evaporators have their detractions. Perhaps the greatest of these is the expense attributable to steam drums, large downcomers, and headers to supply water to their tubes. Moreover, the reservoirs of water contained in them require time to bring up the boiling temperature, so the start-up time for a circulation evaporator is extended.
Once-through evaporators do not require downcomers or drums and are less expensive to manufacture. Moreover, the only stored water in them resides in the tubes themselves and the supply header from which the tubes extend. This enables a once-through evaporator to be brought to operating conditions more rapidly than a natural circulation evaporator. However, a once-through evaporator must completely convert the water into steam, so that only steam escapes from its tubes and flows on to the superheater. No liquid water should leave the evaporator. The evaporator relies on a feedwater pump located upstream in the water circuit to circulate water through it at a controlled rate - a rate that if correct allows the steam to leave in a saturated or a slightly superheated condition.
Thus, in a once-through evaporator the tube walls nearest to the water inlet run wet as in a circulation type evaporator, because these ends of the tube see only liquid water. But farther on in the tubes the water turns into a mist and then into saturated steam. In the mist flow regime, water is sheered from the interior surfaces of the tube walls, so the mist exists in cores which extend through the centers of the tubes. The walls around these cores run dry. This produces higher temperature in the tube walls and less efficient heat transfer. The higher temperatures may require metals that are better able to withstand these temperatures or, in other words, a resort to expensive high alloy steels.
Brief Description of Drawings Figure 1 is a schematic sectional view of a steam generator equipped with a once-through evaporator constructed in accordance with and embodying the present invention;
Figure 2 is a perspective view of the evaporator;
Figure 3 is a sectional view taken along line 3-3 of Fig. 2;
Figure 4 is a fragmentary sectional view of the end of one of the evaporator tubes showing a twisted tape anchored in the tube;
Figure 5 is a fragmentary sectional view similar to Fig. 4, but rotated 90°; and Figure 6 is a fragmentary view of one of the evaporator tubes, partially cut away and in section, showing the flow in the tube.
Best Mode for Carrying Out the Invention Referring now to the drawings, a steam generator A (Fig. 1 ) basically includes a duct 2 having an inlet end 4 and a discharge end 6. The inlet end 4 is connected to a source of hot gases, such as a gas turbine or an incinerator, and those gases flow through the duct 12, leaving it at the discharged end 6. In addition, a steam generator A includes a superheater 12, an evaporator 14, and a feedwater heater or economizer 16 arranged in the duct 2 in that order from the inlet end 4 of the outlet end 6. Thus, the hot gases flow first through the superheater 12, then through the evaporator 14, and finally through the economizer 16. Water flows in the opposite direction. To this end, the economizer 16 is connected to a feedwater pump 18 which delivers feedwater to the economizer 16. It extracts heat from the hot gases and transfers that heat to the liquid water that flows through it, thereby elevating the temperature of the water, but the water remains a liquid. Leaving the economizer 16, the liquid water then flows to the evaporator 14 through which it passes. The evaporator 14 converts the water to steam, mostly saturated steam. The steam flows into the superheater 12 which raises its temperature, transforming it into superheated steam that may be used to power a turbine or in some industrial process or even to heat a building. The superheater 12, evaporator 14, and economizer 16 are basically tube banks. The evaporator 14 operates on the once-through principle. Actually, the steam generator A may have more than one evaporator 14.
The evaporator 14 includes (Fig. 2) a supply header 26, a discharge header 28 and tubes 30 which extend between the two headers 26 and 28.
The supply header 26 has an inlet port 32 that is connected to the economizer 16 and receives heated water from the economizer 16 - indeed, water which is delivered to it under the head produced by the pump 18. The discharge header 26 has outlet ports 34 which are connected to the superheater 12, and through the ports 34 steam, that is saturated or slightly superheated, is directed to the superheater 12. The tubes 30 have fins 36 which facilitate the extraction of heat from the gases flowing through the duct 2.
Within the tubes 30 the heated water from supply header 26 is converted into the steam which collects within the discharge header 28 and then passes on to the superheater 12. Thus, the portion of each tube 30 that is closest to the supply header 20 contains liquid water, while the portion that is closest to the discharge header 28 contains steam that is saturated and perhaps even slightly superheated. In the intermediate portion of each tube 30 the liquid water undergoes the change of phase and becomes steam. Here the water boils, becoming a mist or a mixture of water and saturated steam. Further along the mist becomes saturated steam, and finally the saturated steam may become superheated steam, albeit only slightly superheated. The superheated region of the tube 30, if indeed there is superheated steam, is quite short. The tubes 30 are formed from carbon steel or chrome-moly steel.
Each tube 30 contains a helical tape 40 (Figs. 3-5) which extends from its inlet and, that is its end which is connected to the supply header 26, through the regions in which the mist exists. The width of each tape 30 is slightly less than the inside diameter of the tube 30 through which it extends, so that the tape 40 can be inserted into or withdrawn from the tube 30 without interference from the tube 30 itself. Preferably, the width of each tape 40 should be about 1/16 inches smaller than the inside diameter of its tube 30, at least for a tube having a 2 inch inside diameter. The tape 40 is twisted multiple times between its ends, so that its edges form helices that lie along the inside surface of the tube 30. Indeed, a full 360° twist of the tape 40 should occur within a distance amounting to a length to diameter of 5 to 25. For example, for a tube 30 having a 2 inch inside diameter and a length to diameter ratio of 5 for the twist in its tape 40, a full 360°
twist of the tape 40 will occur in 10 inches of the tube 40. That end of the tape 40 that resides at the inlet of the tube 30 is fitted with an anchor bar 42 that extends transversely across like inlet end of the tube 32. The bar 42 is welded to the end of the tube 30 and to the tape 40, thus anchoring the tape 40 with its tube 30. The tapes 40 are formed from a metal that can withstand the temperatures associated with slightly superheated steam and are further compatible with the metal of the tube 30 in the sense electrolytic reactions are minimized. Stainless steel is suitable when the tubes 30 are carbon steel.
In the operation of the steam generator A, hot gases flowing through the duct 2 pass over the tubes of the superheater 12, the evaporator 14 and the economizer 16 in that order and at each undergo a reduction in temperature. The feedwater pump 18 forces water into and through the economizer 16 where the water extracts heat from the gases that flow over the tubes of the economizer 16. The temperature of the water rises, but the water remains in the liquid phase. Under the head produced by the pump 18, the water flows from the economizer 16 into the supply header 26 of the evaporator 14 and then into the tubes 30 of the evaporator 14. Within the tubes 30, the water encounters even higher temperatures derived from the gases passing through the duct 2. Indeed, the gases passing through the evaporator 14 elevate the temperature of the tubes 30 high enough to convert the water in the tubes 30 to steam. The water, initially upon entering the tubes 30, remains in the liquid phase, but as it flows through the tubes 30 it begins to boil, producing a mist. The tapes 40 extend through the region of mist flow and produce a good measure of turbulence in the mist as it flows on toward the discharge header 28. The turbulence brings the mist, that is to say the water particles, against the inside surfaces of the tubes (Fig. 6), thereby effecting better and more efficient transfer of heat between the gases flowing over the tubes 30 and the mist in the tubes 30. This further protects the tubes 30 from overheating. Were it not for the tapes 40, the mist would tend to remain in the center of the tubes 30 and would be surrounded by saturated or superheated steam along the interior surfaces of the tubes 30, thus causing the tubes 30 in the regions of the mist to operate at higher temperatures. As the mist in the tubes 30 flows on and approaches the discharge header 28 it transforms into saturated steam and may even change to superheated steam, albeit only slightly superheated.
But the regions of the tubes 30 that see only superheated steam are short and are maintained at relatively moderate temperatures by reason of heat conducted from them to the regions occupied by the mist and the liquid water.
In lieu of anchoring the tapes 40 to the tubes 30 at the supply header 26, they may be anchored at the discharge header 28, in which event they will extend toward the supply header 26. The tapes 40 may extend the full lengths of the tubes 30 through which they pass or only through the regions of mist flow. The evaporator 14 in lieu of having its tubes 30 arranged in a single bank, may have them organized in multiple banks.
Claims (18)
1. A once-through evaporator for a steam generator, said evaporator comprising:
a supply header for receiving liquid water;
a discharge header spaced from the supply header for receiving steam;
tubes extending between and connected to the supply and discharge headers, so that water from the supply header may flow toward the discharge header and be converted to steam by heat to which the tubes are subjected; and tapes in at least some of the tubes for inducing turbulence in a mist that is produced in such tubes as the water converted to steam in such tubes.
a supply header for receiving liquid water;
a discharge header spaced from the supply header for receiving steam;
tubes extending between and connected to the supply and discharge headers, so that water from the supply header may flow toward the discharge header and be converted to steam by heat to which the tubes are subjected; and tapes in at least some of the tubes for inducing turbulence in a mist that is produced in such tubes as the water converted to steam in such tubes.
2. An evaporator according to claim 1 wherein each tape is twisted such that its edges form helices that lie along the interior surfaces of the tubes in which they lie.
3. An evaporator according to claim 2 wherein each tape has a length to diameter for a 360° twist of about 5 to 25.
4. An evaporator according to claim 1 wherein the tape is anchored at one end of the tube through which it extends.
5. An evaporator according to claim 2 and further comprising a bar extending transversely across each tube that contains a tape at the end of the tube at which it is anchored; wherein the bar is attached to the tube across which it extends; and wherein the tape for the tube is secured to the bar.
6. An evaporator according to claim 4 wherein each tape is anchored to the tube through which it extends at that end of the tube which is at the supply header.
7. An evaporator according to claim 2 wherein the width of each tape is less than the inside diameter of the tube through which it extends.
8. In a steam generator including a duct through which hot gases pass, a superheater and an economizer located in the duct, with the superheater being located upstream from the economizer with respect to the flow of the gases, a pump for delivering liquid water to the economizer, an improved once-through evaporator located in the duct between the superheater and the evaporator and being connected to the economizer and to the superheater such that water from the economizer flows into the evaporator which converts it into a mist flow and then into steam that is directed into the superheater where it leaves as superheated steam, said evaporator comprising:
tubes which lie within the duct so that the hot gases pass over them;
and a twisted tape located within each tube in the region of the mist flow.
tubes which lie within the duct so that the hot gases pass over them;
and a twisted tape located within each tube in the region of the mist flow.
9. The combination according to claim 8 wherein the tapes are twisted such that their edges form helices that lie along the inside surfaces of the tubes.
10. The combination according to claim 8 wherein each tape is anchored at one end of the tube through which it extends.
11. The combination according to claim 10 and further comprising a bar extended across and is secured to each tube at the end at which the tape is anchored; and wherein the twisted tape in that tube is attached to the bar.
12. The combination according to claim 8 wherein the liquid water within each tube transforms into a mist and then into saturated steam; and wherein the tape for the tube lies at least within the region of the mist.
13. The combination according to claim 12 wherein the twisted tape in each tube extends from the inlet and through at least the region of the tube in which the mist exists.
14. For use in a once-through evaporator, the combination comprising:
a tube having an inlet end and an outlet end; and a twisted tape located within the tube and having helical edges that lie along the inside surfaces of the tube.
a tube having an inlet end and an outlet end; and a twisted tape located within the tube and having helical edges that lie along the inside surfaces of the tube.
15. The combination according to claim 14 wherein the tape is anchored to the tube at one the ends of the tube.
16. The combination according to claim 14 wherein the tape possesses a length to diameter for a full 360° twist of 5 to 25.
17. The combination according to claim 14 wherein the width of the tape for each tube is slightly less than the inside diameter of the tube.
18. The combination according to claim 14 and further comprising water within one end of the tube and steam in the other end and a mist flow region between the water and the steam, and wherein the tape lies within the mist flow region.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US41608302P | 2002-10-04 | 2002-10-04 | |
| US60/416,083 | 2002-10-04 | ||
| PCT/US2003/031174 WO2004033962A2 (en) | 2002-10-04 | 2003-10-02 | Once-through evaporator for a steam generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2501086A1 true CA2501086A1 (en) | 2004-04-22 |
Family
ID=32093813
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002501086A Abandoned CA2501086A1 (en) | 2002-10-04 | 2003-10-02 | Once-through evaporator for a steam generator |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US20040069244A1 (en) |
| EP (1) | EP1546607A4 (en) |
| KR (1) | KR20050086420A (en) |
| CN (1) | CN1703599A (en) |
| AU (1) | AU2003275378A1 (en) |
| CA (1) | CA2501086A1 (en) |
| MX (1) | MXPA05003380A (en) |
| WO (1) | WO2004033962A2 (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7065967B2 (en) * | 2003-09-29 | 2006-06-27 | Kalex Llc | Process and apparatus for boiling and vaporizing multi-component fluids |
| US7770544B2 (en) * | 2004-12-01 | 2010-08-10 | Victory Energy Operations LLC | Heat recovery steam generator |
| EP1793163A1 (en) * | 2005-12-05 | 2007-06-06 | Siemens Aktiengesellschaft | Steam generator tube, method of manufacturing the same and once-through steam generator |
| KR100752635B1 (en) * | 2006-05-02 | 2007-08-29 | 삼성광주전자 주식회사 | Heat exchanger for refrigerator |
| US7882809B2 (en) * | 2006-11-07 | 2011-02-08 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Heat exchanger having a counterflow evaporator |
| EP2141411B1 (en) | 2008-06-30 | 2013-08-21 | Cockerill Maintenance & Ingenierie S.A. | Header distributor for two-phase flow in a single pass evaporator |
| EP2184536A1 (en) * | 2008-09-09 | 2010-05-12 | Siemens Aktiengesellschaft | Steam generator pipe, accompanying production method and once-through steam generator |
| US8695344B2 (en) * | 2008-10-27 | 2014-04-15 | Kalex, Llc | Systems, methods and apparatuses for converting thermal energy into mechanical and electrical power |
| US8408003B2 (en) * | 2008-11-05 | 2013-04-02 | General Electric Company | Combined cycle power plant |
| US8474263B2 (en) | 2010-04-21 | 2013-07-02 | Kalex, Llc | Heat conversion system simultaneously utilizing two separate heat source stream and method for making and using same |
| EP2839213B1 (en) | 2012-01-17 | 2018-09-05 | General Electric Technology GmbH | Tube and baffle arrangement in a once-through horizontal evaporator |
| WO2013108218A2 (en) | 2012-01-17 | 2013-07-25 | Alstom Technology Ltd | Tube arrangement in a once-through horizontal evaporator |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL267585A (en) * | 1961-06-09 | |||
| US3648754A (en) * | 1969-07-28 | 1972-03-14 | Hugo H Sephton | Vortex flow process and apparatus for enhancing interfacial surface and heat and mass transfer |
| US3756202A (en) * | 1971-11-22 | 1973-09-04 | American Standard Inc | Heat exchange tube for use in a boiler and boiler incorporating the same |
| NL52674C (en) * | 1973-11-02 | |||
| EP0349834B1 (en) * | 1988-07-04 | 1996-04-17 | Siemens Aktiengesellschaft | Once-through steam generator |
| RU2075690C1 (en) * | 1991-04-18 | 1997-03-20 | Сименс АГ | Flow-through steam generator |
| JPH05164482A (en) * | 1991-12-12 | 1993-06-29 | Kobe Steel Ltd | Liquefied natural gas vaporizer |
| DE4333404A1 (en) * | 1993-09-30 | 1995-04-06 | Siemens Ag | Continuous steam generator with vertically arranged evaporator tubes |
| JP3037073B2 (en) * | 1994-07-20 | 2000-04-24 | 株式会社神戸製鋼所 | Cryogenic liquid vaporizer |
| US5799622A (en) * | 1997-06-30 | 1998-09-01 | Decker Manufacturing | Furnace heat exchanger tube cleaning system |
| US6092589A (en) * | 1997-12-16 | 2000-07-25 | York International Corporation | Counterflow evaporator for refrigerants |
| US5924389A (en) * | 1998-04-03 | 1999-07-20 | Combustion Engineering, Inc. | Heat recovery steam generator |
| DE19858780C2 (en) * | 1998-12-18 | 2001-07-05 | Siemens Ag | Fossil-heated continuous steam generator |
| DE19901430C2 (en) * | 1999-01-18 | 2002-10-10 | Siemens Ag | Fossil-heated steam generator |
| DE19929088C1 (en) * | 1999-06-24 | 2000-08-24 | Siemens Ag | Fossil fuel heated steam generator e.g. for power station equipment |
-
2003
- 2003-10-02 MX MXPA05003380A patent/MXPA05003380A/en not_active Application Discontinuation
- 2003-10-02 AU AU2003275378A patent/AU2003275378A1/en not_active Abandoned
- 2003-10-02 CN CNA2003801009215A patent/CN1703599A/en active Pending
- 2003-10-02 US US10/677,443 patent/US20040069244A1/en not_active Abandoned
- 2003-10-02 CA CA002501086A patent/CA2501086A1/en not_active Abandoned
- 2003-10-02 WO PCT/US2003/031174 patent/WO2004033962A2/en not_active Application Discontinuation
- 2003-10-02 EP EP03759654A patent/EP1546607A4/en not_active Withdrawn
- 2003-10-02 KR KR1020057005565A patent/KR20050086420A/en not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| AU2003275378A8 (en) | 2004-05-04 |
| MXPA05003380A (en) | 2005-06-22 |
| EP1546607A4 (en) | 2006-05-03 |
| AU2003275378A1 (en) | 2004-05-04 |
| KR20050086420A (en) | 2005-08-30 |
| US20040069244A1 (en) | 2004-04-15 |
| EP1546607A2 (en) | 2005-06-29 |
| CN1703599A (en) | 2005-11-30 |
| WO2004033962A3 (en) | 2004-06-03 |
| WO2004033962A2 (en) | 2004-04-22 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FZDE | Discontinued |