US20130269347A1 - Combined power and water production system and method - Google Patents
Combined power and water production system and method Download PDFInfo
- Publication number
- US20130269347A1 US20130269347A1 US13/445,025 US201213445025A US2013269347A1 US 20130269347 A1 US20130269347 A1 US 20130269347A1 US 201213445025 A US201213445025 A US 201213445025A US 2013269347 A1 US2013269347 A1 US 2013269347A1
- Authority
- US
- United States
- Prior art keywords
- water
- steam
- power
- exhaust
- liquid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 176
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 33
- 238000000034 method Methods 0.000 title claims description 11
- 239000007788 liquid Substances 0.000 claims description 70
- 238000010248 power generation Methods 0.000 claims description 27
- 235000012206 bottled water Nutrition 0.000 claims description 15
- 239000003651 drinking water Substances 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 7
- 238000010612 desalination reaction Methods 0.000 claims description 6
- 238000011084 recovery Methods 0.000 claims description 5
- 238000010586 diagram Methods 0.000 description 5
- 239000002699 waste material Substances 0.000 description 4
- 238000010304 firing Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000003190 augmentative effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K17/00—Using steam or condensate extracted or exhausted from steam engine plant
- F01K17/02—Using steam or condensate extracted or exhausted from steam engine plant for heating purposes, e.g. industrial, domestic
- F01K17/025—Using steam or condensate extracted or exhausted from steam engine plant for heating purposes, e.g. industrial, domestic in combination with at least one gas turbine, e.g. a combustion gas turbine
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/14—Combined heat and power generation [CHP]
Definitions
- the subject matter disclosed herein relates to combined power and water production systems.
- Combined power and water production systems generate steam and use the steam to drive steam turbines to produce power.
- the steam is also used to produce water after expansion in a turbine.
- the steam may be used in a desalination plant to heat saltwater to extract waste and produce potable water.
- Combined power and water production systems generate ratios of power to water at differing levels, depending upon the design requirements of the system.
- a heat recovery steam generator HRSG having multiple steam drums is used.
- the multiple steam drums provide output steam at varying temperatures and pressures.
- the HRSG receives high temperature gas from a gas turbine exhaust and is sometimes augmented by supplementary firing to produce additional steam for water and/or power production.
- the steam production capability of intermediate and lower pressure drums decreases and overall efficiency of the HRSG and water or power plant decreases.
- the subject matter disclosed herein relates to a system for extracting a portion of steam from steam turbine to heat water entering a power generator to improve system efficiency when varying levels of supplementary firing is adopted to achieve power to water ratios.
- a combined power and water production system includes a steam generator to generate steam; a power generating assembly to receive the steam from the steam generator, to generate power using the steam, and to output exhaust; a water producing facility to receive the exhaust from the power generating assembly and to use the exhaust to produce first liquid water; and a heater to heat second liquid water and to provide the second liquid water heated by the heater to the steam generator to generate the steam.
- a method of providing water and power in a combined water and power production system includes generating steam at a steam generator, providing the steam to a power generation assembly to generate power, providing the steam to a water production facility to produce first liquid water, and heating second liquid water used by the steam generator prior to supplying the second liquid water to the steam generator.
- a combined power and water generation system includes a steam generator to generate steam; a power generation assembly to generate power with the steam; a water production facility to receive non-potable water and to use the steam to produce potable water; and a heater to heat water before the water is provided to the steam generator.
- FIG. 1 is a block diagram of a combined power and water generation system according to an embodiment of the invention.
- FIG. 2 is a diagram of a combined power and water generation system.
- FIG. 3 is a block diagram of a heat recovery steam generator according to one embodiment of the invention.
- FIG. 4 is a block diagram of a heat recovery steam generator according to another embodiment of the invention.
- FIG. 5 is a flowchart illustrating a method of operating a combined power and water generation system according to an embodiment of the invention.
- FIG. 1 illustrates a block diagram of a combined power and water system 1 (“the system 1 ”) according to one embodiment.
- the system 1 includes a heat recovery steam generator (“HRSG”) 10 , a power generation assembly 20 , a water producing facility 30 , and a heater 40 .
- HRSG heat recovery steam generator
- the solid arrows 2 , 7 , and 8 represent liquid water
- the solid arrow 5 FIG. 2
- the dashed arrow 3 represents steam from the HRSG 10
- the dashed and dotted arrow 4 represents steam from the power generation assembly 20
- the arrow 9 represents a gas stream.
- the HRSG 10 receives a gas stream 9 and receives water 2 from the heater 40 .
- the gas stream 9 is introduced to the HRSG 10 as a heated gas stream, and the HRSG 10 converts the water to steam at one or more predetermined pressures and temperatures using the heated gas stream 9 and outputs the steam 3 to the power generation assembly 20 to drive the power generation assembly 20 .
- the power generation assembly 20 uses the steam 3 to generate power. Steam 4 from the power generation assembly 20 is supplied to each of the water producing facility 30 and the heater 40 .
- the water producing facility 30 uses exhaust steam 4 a to convert input liquid water 7 into output liquid water 8 .
- the water producing facility 30 is a desalination facility
- the input liquid water 7 is saltwater
- the output liquid water 8 is potable water.
- the desalination facility heats the saltwater 7 with the exhaust steam 4 a to extract waste from the saltwater to produce the potable water 8 .
- the heater 40 receives steam 4 b from the power generation assembly 20 and liquid water 2 from the water producing facility 30 and heats the liquid water 2 prior to providing the liquid water 2 to the HRSG 10 . Since the liquid water 2 is heated prior to being provided to the HRSG 10 , less energy is required by the HRSG 10 to convert the liquid water 2 to steam 3 , making the HRSG 10 more efficient.
- the steam 4 b is extracted from the low pressure steam turbine 24 upstream from the exhaust, so that the steam 4 b provided to the heater 40 has a higher energy level than the steam 4 a provided to the water producing facility 30 .
- FIG. 2 illustrates in more detail a combined power and water system 1 according to one embodiment.
- the power generation assembly 20 includes a high-pressure steam turbine 22 , a low-pressure steam turbine 24 , and a generator 26 .
- the high-pressure steam turbine 22 receives the steam 3 from the HRSG 10 which drives a shaft 28 . After driving the high-pressure steam turbine 22 , the steam 3 is then provided to a low-pressure steam turbine 24 .
- the shaft 28 which is connected to the high-pressure steam turbine 22 and the low-pressure steam turbine 24 drives the generator 26 to generate power.
- FIG. 2 illustrates only a high-pressure steam turbine 22 and a low-pressure steam turbine 24 , any number and type of turbines may be used.
- the power generation assembly 20 may include one or more intermediate-pressure steam turbines, multiple high- or low-pressure steam turbines 22 and 24 , and dual-flow steam turbines.
- the power generation assembly may include one or more gas turbines.
- the power generation assembly includes multiple generators 26 , and the high-pressure steam turbine 22 may be connected to a different shaft than the low-pressure steam turbine 24 to drive a different generator 26 than the low-pressure steam turbine 24 .
- the HRSG 10 includes an economizer 11 to heat the liquid water 2 , an evaporator 12 including a steam drum 13 to evaporate the water from the economizer 11 to generate steam, and a superheater 14 to heat the steam 3 and output the steam to the power generation assembly 20 .
- the HRSG 10 includes multiple evaporators to generate steam at different pressure levels.
- FIG. 3 illustrates an example of an embodiment in which the HRSG 10 includes multiple evaporators.
- the low-pressure economizer 11 heats the liquid water 2 and outputs the heated liquid water 2 to the low-pressure evaporator 12 , which corresponds to the evaporator 12 of FIG. 2 .
- the low-pressure evaporator 12 evaporates the water 2 to generate steam, and outputs the steam to a low-pressure superheater 21 , which outputs steam 6 at a low pressure to the low-pressure steam turbine 24 .
- the liquid water 2 is also output to a high-pressure economizer 15 to heat the liquid water 2 and to output the heated liquid water 2 to a high-pressure evaporator 16 including a steam drum 17 .
- the high-pressure evaporator 16 outputs the steam to the superheater 14 , which further heats the steam and outputs the steam 3 to the high-pressure steam turbine 22 .
- the HRSG 10 includes a burner 18 to further heat a gas stream in the HRSG 10 to enable additional steam production.
- the burner 18 is located between a first superheater 14 , corresponding to the superheater 14 of FIG. 2 , and a second superheater 19 .
- the heated and pressurized steam 3 is output to the power generation assembly 20 from the second superheater 19 .
- the HRSG 10 may include any number and variety of economizers, evaporators, superheaters, and burners to generate steam at varying temperatures and pressures.
- the water producing facility 30 receives the exhaust steam 4 a from the low-pressure steam turbine 24 , and uses the exhaust steam 4 a to produce liquid water 8 .
- the input liquid water 7 is saltwater and the output liquid water 8 is potable water.
- the exhaust steam 4 a is used to heat the saltwater to separate the salt and waste in the water from the water, producing the potable water 8 .
- the water producing facility 30 outputs excess exhaust steam 4 a as residual water 5 .
- the residual water 5 may be a condensate or steam, or a combination of condensate and steam.
- a condensate pump 52 pumps the residual water 5 , and transmits the resulting liquid water 2 to the heater 40 .
- the heater 40 is a feedwater heater.
- the liquid water 2 is heated by the steam 4 b and transmitted to a reservoir 51 , also known as a deaerator.
- the pre-heated liquid water 2 is transmitted to the HRSG 10 to generate steam 3 , and since the liquid water 2 is already heated, the HRSG 10 operates more efficiently, because less energy is expended to heat and evaporate the water in the HRSG 10 .
- the pre-heating of the liquid water 2 by the heater 40 enables the use of additional evaporators to provide steam at additional pressures.
- the steam 4 c is combined with the residual water 5 and condensed into the liquid water 2 , which is then used by the HRSG 10 to generate steam 3 , as discussed above. Consequently, the steam 4 c and residual water 5 are recovered and re-used to generate power at the power generation assembly 20 and to produce potable liquid water 8 at the water producing facility 30 .
- the liquid water 2 , 7 , and 8 , the steam 4 , the residual water 5 , and the steam 3 and 6 represent flows of molecules rather than specific molecules at one location at one point in time.
- the steam 4 b is described as heating the second liquid water 2 , then being condensed and becoming a part of the second liquid water 2 that is heated by the steam 4 b .
- This disclosure does not mean that molecules in the steam 4 b having a gaseous form heat themselves in a liquid form. Instead, molecules that make up a gaseous flow of steam 4 c are condensed into liquid form to become part of the second liquid water 2 . Then, the molecules that now make up the second liquid water 2 are heated by subsequent molecules that make up the flow of steam 4 b.
- FIG. 5 illustrates a method of producing power and water according to an embodiment of the invention.
- steam is generated by a steam generator, such as by an HRSG 10 illustrated in FIGS. 1-4 .
- the steam is output to a power generation assembly to generate power using the steam.
- exhaust from the power generation assembly is provided to a water producing facility to produce water.
- the water producing facility is a desalination plant, the exhaust heats saltwater to separate the water in the saltwater from the salt and other waste.
- steam is provided to the water producing facility directly from a steam generator, such as an HRSG 10 either instead of or in addition to the exhaust from the power generation assembly.
- the liquid water is heated by a heater.
- the heater is a feedwater heater that uses heated exhaust from the power generation assembly to heat the liquid water in the heater.
- the heated liquid water is provided to the steam generator to generate steam, and the cycle begins again at operation 61 . Since the liquid water is heated prior to being supplied to the steam generator, the steam generator is able to operate with increased efficiency.
- liquid water is heated prior to being provided to a steam generator, less energy is required to convert the liquid water to steam, and the steam generator is able to operate with increased efficiency.
- increasing the temperature of the liquid water prior to providing the liquid water to the steam generator allows the power generator to be operated at higher levels of efficiency.
- exhaust from a power generating unit such as a steam turbine is used to produce potable water, heat water provided to an HRSG, and is then converted into the water to be provided to the HRSG to generate steam for the steam turbine.
- a power generating unit such as a steam turbine is used to produce potable water, heat water provided to an HRSG, and is then converted into the water to be provided to the HRSG to generate steam for the steam turbine.
Abstract
A combined power and water production system includes a steam generator, a water production facility, and a heater to heat water and to provide the heated water to the steam generator to generate steam.
Description
- The subject matter disclosed herein relates to combined power and water production systems.
- Combined power and water production systems generate steam and use the steam to drive steam turbines to produce power. The steam is also used to produce water after expansion in a turbine. For example, the steam may be used in a desalination plant to heat saltwater to extract waste and produce potable water.
- Combined power and water production systems generate ratios of power to water at differing levels, depending upon the design requirements of the system. To produce the varying ratios of water and power, a heat recovery steam generator (HRSG) having multiple steam drums is used. The multiple steam drums provide output steam at varying temperatures and pressures. The HRSG receives high temperature gas from a gas turbine exhaust and is sometimes augmented by supplementary firing to produce additional steam for water and/or power production. For increasing levels of supplementary firing in the HRSG, the steam production capability of intermediate and lower pressure drums decreases and overall efficiency of the HRSG and water or power plant decreases. Specifically, the subject matter disclosed herein relates to a system for extracting a portion of steam from steam turbine to heat water entering a power generator to improve system efficiency when varying levels of supplementary firing is adopted to achieve power to water ratios.
- According to one aspect of the invention, a combined power and water production system includes a steam generator to generate steam; a power generating assembly to receive the steam from the steam generator, to generate power using the steam, and to output exhaust; a water producing facility to receive the exhaust from the power generating assembly and to use the exhaust to produce first liquid water; and a heater to heat second liquid water and to provide the second liquid water heated by the heater to the steam generator to generate the steam.
- According to another aspect of the invention, a method of providing water and power in a combined water and power production system includes generating steam at a steam generator, providing the steam to a power generation assembly to generate power, providing the steam to a water production facility to produce first liquid water, and heating second liquid water used by the steam generator prior to supplying the second liquid water to the steam generator.
- According to yet another aspect of the invention a combined power and water generation system includes a steam generator to generate steam; a power generation assembly to generate power with the steam; a water production facility to receive non-potable water and to use the steam to produce potable water; and a heater to heat water before the water is provided to the steam generator.
- These and other advantages and features will become more apparent from the following description taken in conjunction with the drawings.
- The subject matter, which is regarded as the invention, is particularly pointed out and distinctly claimed in the claims at the conclusion of the specification. The foregoing and other features, and advantages of the invention are apparent from the following detailed description taken in conjunction with the accompanying drawings in which:
-
FIG. 1 is a block diagram of a combined power and water generation system according to an embodiment of the invention. -
FIG. 2 is a diagram of a combined power and water generation system. -
FIG. 3 is a block diagram of a heat recovery steam generator according to one embodiment of the invention. -
FIG. 4 is a block diagram of a heat recovery steam generator according to another embodiment of the invention. -
FIG. 5 is a flowchart illustrating a method of operating a combined power and water generation system according to an embodiment of the invention. - The detailed description explains embodiments of the invention, together with advantages and features, by way of example with reference to the drawings.
-
FIG. 1 illustrates a block diagram of a combined power and water system 1 (“thesystem 1”) according to one embodiment. Thesystem 1 includes a heat recovery steam generator (“HRSG”) 10, apower generation assembly 20, awater producing facility 30, and aheater 40. In the figures, thesolid arrows FIG. 2 ) represents residual water from thewater producing facility 30, the dashed arrow 3 (and 6 inFIG. 3 ) represents steam from theHRSG 10, the dashed and dottedarrow 4 represents steam from thepower generation assembly 20, and thearrow 9 represents a gas stream. - The HRSG 10 receives a
gas stream 9 and receiveswater 2 from theheater 40. In one embodiment, thegas stream 9 is introduced to the HRSG 10 as a heated gas stream, and the HRSG 10 converts the water to steam at one or more predetermined pressures and temperatures using theheated gas stream 9 and outputs thesteam 3 to thepower generation assembly 20 to drive thepower generation assembly 20. Thepower generation assembly 20 uses thesteam 3 to generate power. Steam 4 from thepower generation assembly 20 is supplied to each of thewater producing facility 30 and theheater 40. - The
water producing facility 30 usesexhaust steam 4 a to convert inputliquid water 7 into outputliquid water 8. According to one embodiment, thewater producing facility 30 is a desalination facility, the inputliquid water 7 is saltwater, and the outputliquid water 8 is potable water. The desalination facility heats thesaltwater 7 with theexhaust steam 4 a to extract waste from the saltwater to produce thepotable water 8. - The
heater 40 receivessteam 4 b from thepower generation assembly 20 andliquid water 2 from thewater producing facility 30 and heats theliquid water 2 prior to providing theliquid water 2 to the HRSG 10. Since theliquid water 2 is heated prior to being provided to theHRSG 10, less energy is required by the HRSG 10 to convert theliquid water 2 tosteam 3, making the HRSG 10 more efficient. In one embodiment, thesteam 4 b is extracted from the lowpressure steam turbine 24 upstream from the exhaust, so that thesteam 4 b provided to theheater 40 has a higher energy level than thesteam 4 a provided to thewater producing facility 30. -
FIG. 2 illustrates in more detail a combined power andwater system 1 according to one embodiment. - In the embodiment illustrated in
FIG. 2 , thepower generation assembly 20 includes a high-pressure steam turbine 22, a low-pressure steam turbine 24, and agenerator 26. The high-pressure steam turbine 22 receives thesteam 3 from the HRSG 10 which drives ashaft 28. After driving the high-pressure steam turbine 22, thesteam 3 is then provided to a low-pressure steam turbine 24. Theshaft 28, which is connected to the high-pressure steam turbine 22 and the low-pressure steam turbine 24 drives thegenerator 26 to generate power. - Although
FIG. 2 illustrates only a high-pressure steam turbine 22 and a low-pressure steam turbine 24, any number and type of turbines may be used. For example, thepower generation assembly 20 may include one or more intermediate-pressure steam turbines, multiple high- or low-pressure steam turbines multiple generators 26, and the high-pressure steam turbine 22 may be connected to a different shaft than the low-pressure steam turbine 24 to drive adifferent generator 26 than the low-pressure steam turbine 24. - The HRSG 10 includes an
economizer 11 to heat theliquid water 2, anevaporator 12 including asteam drum 13 to evaporate the water from theeconomizer 11 to generate steam, and asuperheater 14 to heat thesteam 3 and output the steam to thepower generation assembly 20. According to alternative embodiments, the HRSG 10 includes multiple evaporators to generate steam at different pressure levels. -
FIG. 3 illustrates an example of an embodiment in which the HRSG 10 includes multiple evaporators. InFIG. 3 , the low-pressure economizer 11 heats theliquid water 2 and outputs the heatedliquid water 2 to the low-pressure evaporator 12, which corresponds to theevaporator 12 ofFIG. 2 . The low-pressure evaporator 12 evaporates thewater 2 to generate steam, and outputs the steam to a low-pressure superheater 21, which outputssteam 6 at a low pressure to the low-pressure steam turbine 24. Theliquid water 2 is also output to a high-pressure economizer 15 to heat theliquid water 2 and to output the heatedliquid water 2 to a high-pressure evaporator 16 including asteam drum 17. The high-pressure evaporator 16 outputs the steam to thesuperheater 14, which further heats the steam and outputs thesteam 3 to the high-pressure steam turbine 22. - According to another embodiment, illustrated in
FIG. 4 , the HRSG 10 includes aburner 18 to further heat a gas stream in the HRSG 10 to enable additional steam production. Theburner 18 is located between afirst superheater 14, corresponding to thesuperheater 14 ofFIG. 2 , and asecond superheater 19. The heated andpressurized steam 3 is output to thepower generation assembly 20 from thesecond superheater 19. - While
FIGS. 2-4 illustrate different embodiments of the HRSG 10, according to various embodiments, the HRSG 10 may include any number and variety of economizers, evaporators, superheaters, and burners to generate steam at varying temperatures and pressures. - Referring to
FIG. 2 , thewater producing facility 30 receives theexhaust steam 4 a from the low-pressure steam turbine 24, and uses theexhaust steam 4 a to produceliquid water 8. According to one embodiment, the inputliquid water 7 is saltwater and the outputliquid water 8 is potable water. Theexhaust steam 4 a is used to heat the saltwater to separate the salt and waste in the water from the water, producing thepotable water 8. After producing the outputliquid water 8, thewater producing facility 30 outputsexcess exhaust steam 4 a asresidual water 5. Theresidual water 5 may be a condensate or steam, or a combination of condensate and steam. Acondensate pump 52 pumps theresidual water 5, and transmits the resultingliquid water 2 to theheater 40. In the embodiment illustrated inFIG. 2 , theheater 40 is a feedwater heater. Theliquid water 2 is heated by thesteam 4 b and transmitted to areservoir 51, also known as a deaerator. The pre-heatedliquid water 2 is transmitted to theHRSG 10 to generatesteam 3, and since theliquid water 2 is already heated, theHRSG 10 operates more efficiently, because less energy is expended to heat and evaporate the water in theHRSG 10. In particular, in an embodiment in which multiple evaporators are utilized, such as in the embodiment illustrated inFIG. 3 , the pre-heating of theliquid water 2 by theheater 40 enables the use of additional evaporators to provide steam at additional pressures. - In one embodiment, after heating the
liquid water 2 in theheater 40, thesteam 4 c is combined with theresidual water 5 and condensed into theliquid water 2, which is then used by theHRSG 10 to generatesteam 3, as discussed above. Consequently, thesteam 4 c andresidual water 5 are recovered and re-used to generate power at thepower generation assembly 20 and to produce potableliquid water 8 at thewater producing facility 30. - It is understood by the present disclosure that the
liquid water steam 4, theresidual water 5, and thesteam steam 4 b is described as heating the secondliquid water 2, then being condensed and becoming a part of the secondliquid water 2 that is heated by thesteam 4 b. This disclosure does not mean that molecules in thesteam 4 b having a gaseous form heat themselves in a liquid form. Instead, molecules that make up a gaseous flow ofsteam 4 c are condensed into liquid form to become part of the secondliquid water 2. Then, the molecules that now make up the secondliquid water 2 are heated by subsequent molecules that make up the flow ofsteam 4 b. -
FIG. 5 illustrates a method of producing power and water according to an embodiment of the invention. Inoperation 61, steam is generated by a steam generator, such as by anHRSG 10 illustrated inFIGS. 1-4 . Inoperation 62, the steam is output to a power generation assembly to generate power using the steam. Inoperation 63, exhaust from the power generation assembly is provided to a water producing facility to produce water. For example, if the water producing facility is a desalination plant, the exhaust heats saltwater to separate the water in the saltwater from the salt and other waste. According to some embodiments, steam is provided to the water producing facility directly from a steam generator, such as anHRSG 10 either instead of or in addition to the exhaust from the power generation assembly. - In
operation 64, residual water from the water producing facility is condensed into liquid water. Inoperation 65, the liquid water is heated by a heater. In one embodiment, the heater is a feedwater heater that uses heated exhaust from the power generation assembly to heat the liquid water in the heater. - In
operation 66, the heated liquid water is provided to the steam generator to generate steam, and the cycle begins again atoperation 61. Since the liquid water is heated prior to being supplied to the steam generator, the steam generator is able to operate with increased efficiency. - According to the above embodiments since liquid water is heated prior to being provided to a steam generator, less energy is required to convert the liquid water to steam, and the steam generator is able to operate with increased efficiency. In particular, for varying levels of power to water ratio, increasing the temperature of the liquid water prior to providing the liquid water to the steam generator allows the power generator to be operated at higher levels of efficiency. In addition, exhaust from a power generating unit such as a steam turbine is used to produce potable water, heat water provided to an HRSG, and is then converted into the water to be provided to the HRSG to generate steam for the steam turbine. Thus, the water and steam is recycled within the HRSG/power generation/water generation system to operate with increased efficiency.
- While the invention has been described in detail in connection with only a limited number of embodiments, it should be readily understood that the invention is not limited to such disclosed embodiments. Rather, the invention can be modified to incorporate any number of variations, alterations, substitutions or equivalent arrangements not heretofore described, but which are commensurate with the spirit and scope of the invention. Additionally, while various embodiments of the invention have been described, it is to be understood that aspects of the invention may include only some of the described embodiments. Accordingly, the invention is not to be seen as limited by the foregoing description, but is only limited by the scope of the appended claims.
Claims (20)
1. A combined power and water production system, comprising:
a steam generator to generate steam;
a power generating assembly to receive the steam from the steam generator, to generate power using the steam, and to output exhaust;
a water producing facility to receive the exhaust from the power generating assembly and to use the exhaust to produce first liquid water; and
a heater to heat second liquid water and to provide the second liquid water heated by the heater to the steam generator to generate the steam.
2. The combined power and water production system of claim 1 , wherein the steam generator is a heat recovery steam generator (HRSG) having at least one economizer to increase a temperature the second liquid water, at least one evaporator to evaporate the second liquid water from the at least one economizer to generate the steam, and at least one superheater to superheat the steam.
3. The combined power and water production system of claim 2 , wherein the HRSG includes at least two evaporators to output steam from the HRSG to the power generating assembly at different pressures.
4. The combined power and water production system of claim 2 , wherein the HRSG includes at least one burner to increase a temperature of the steam.
5. The combined power and water production system of claim 1 , wherein the power generating assembly includes at least one steam turbine.
6. The combined power and water production system of claim 5 , wherein the at least one steam turbine includes at least one high-pressure steam turbine and at least one low-pressure steam turbine.
7. The combined power and water production system of claim 5 , wherein the exhaust output from the power generating assembly is heated steam.
8. The combined power and water production system of claim 7 , wherein the exhaust is provided to the heater to heat the second liquid water.
9. The combined power and water production system of claim 7 , wherein the water producing facility is a desalination plant, and
the exhaust is output from the water producing facility as residual water.
10. The combined power and water production system of claim 9 , further comprising a condenser to condense the residual water.
11. The combined power and water production system of claim 10 , wherein the exhaust is provided to the heater to heat the second liquid water, and
the exhaust output from the heater is condensed by the condenser.
12. The combined power and water production system of claim 11 , wherein the condenser outputs the second liquid water to the heater.
13. The combined power and water production system of claim 1 , wherein:
the power generating assembly is a steam turbine, the water producing facility is a desalination plant, and the heater is a feedwater heater,
the first liquid water is potable water output from the water producing facility,
the exhaust from the power generating assembly is heated steam and is provided to the water producing facility to heat saltwater to produce the potable water,
the second liquid water includes residual water output from the water producing facility, and
the exhaust from the power generating assembly is provided to the feedwater heater to the heat the residual water output from the water producing facility.
14. A method of providing water and power in a combined water and power production system, the method comprising:
generating steam at a steam generator;
providing the steam to a power generation assembly to generate power;
providing the steam to a water production facility to produce first liquid water; and
heating second liquid prior to supplying the second liquid water to the steam generator to generate the steam.
15. The method of claim 14 , wherein heating the second liquid water used by the steam generator includes heating the second liquid water with exhaust from the power generation assembly.
16. The method of claim 15 , wherein the first liquid water is potable water, and
the water production facility uses the steam to produce the potable water and emits residual water composed of water from the steam after the steam is used to produce the potable water.
17. The method of claim 16 , wherein the second liquid water includes the residual water, and
the method further comprises condensing the residual water from the water production facility.
18. The method of claim 17 , further comprising condensing exhaust steam output by the power generation assembly and used to heat the second liquid water,
wherein the second liquid water includes condensed exhaust steam previously used to heat the second liquid water.
19. A combined power and water generation system, comprising:
a steam generator to generate steam;
a power generation assembly to generate power with the steam;
a water production facility to receive non-potable water and to use the steam to produce potable water; and
a heater to heat water before the water is provided to the steam generator.
20. The combined power and water generation system of claim 19 , wherein the water production facility receives the steam from the power generation assembly,
the heater heats the water using steam output from the power generation assembly, and
at least a portion of the water heated by the heater is condensed steam from the water production facility.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/445,025 US20130269347A1 (en) | 2012-04-12 | 2012-04-12 | Combined power and water production system and method |
EP13162856.2A EP2650494A2 (en) | 2012-04-12 | 2013-04-09 | Combined power and water production system and method |
JP2013081697A JP2013221508A (en) | 2012-04-12 | 2013-04-10 | Combined power and water production system and method |
RU2013116445/06A RU2013116445A (en) | 2012-04-12 | 2013-04-11 | SYSTEM FOR JOINT PRODUCTION OF ELECTRIC POWER AND WATER (OPTIONS) AND METHOD FOR PRODUCING ELECTRIC POWER AND WATER IN SUCH SYSTEM |
CN2013101264093A CN103375206A (en) | 2012-04-12 | 2013-04-12 | Combined power and water production system and method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/445,025 US20130269347A1 (en) | 2012-04-12 | 2012-04-12 | Combined power and water production system and method |
Publications (1)
Publication Number | Publication Date |
---|---|
US20130269347A1 true US20130269347A1 (en) | 2013-10-17 |
Family
ID=48095609
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US13/445,025 Abandoned US20130269347A1 (en) | 2012-04-12 | 2012-04-12 | Combined power and water production system and method |
Country Status (5)
Country | Link |
---|---|
US (1) | US20130269347A1 (en) |
EP (1) | EP2650494A2 (en) |
JP (1) | JP2013221508A (en) |
CN (1) | CN103375206A (en) |
RU (1) | RU2013116445A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20150251924A1 (en) * | 2012-08-16 | 2015-09-10 | University Of South Florida | Systems and methods for water desalination and power generation |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103626250B (en) * | 2013-12-06 | 2015-06-03 | 天津滨瀚海水淡化有限公司 | Comprehensive utilization technology used in seawater power generation and device |
CN103775150B (en) * | 2014-01-22 | 2016-03-02 | 牟大同 | A kind of electricity-water cogeneration system and method |
DE102014217280A1 (en) * | 2014-08-29 | 2016-03-03 | Siemens Aktiengesellschaft | Method and arrangement of a steam turbine plant in combination with a thermal water treatment |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3412558A (en) * | 1965-03-04 | 1968-11-26 | Applied Res And Engineering Lt | Distillation and power producing plant |
US3476653A (en) * | 1967-02-01 | 1969-11-04 | George D Doland | Multistage distillation unit for water and power plant system |
US3479820A (en) * | 1966-11-08 | 1969-11-25 | Abraham Rutenberg | Economical utilization of existing power plants |
US3760868A (en) * | 1971-01-28 | 1973-09-25 | Us Interior | Disposal of waste heat |
US6220013B1 (en) * | 1999-09-13 | 2001-04-24 | General Electric Co. | Multi-pressure reheat combined cycle with multiple reheaters |
US20110100005A1 (en) * | 2009-10-30 | 2011-05-05 | Sampson Glenn A | Water reclamation in a concentrated solar power-enabled power plant |
WO2011148422A1 (en) * | 2010-05-27 | 2011-12-01 | 日立Geニュークリア・エナジー株式会社 | Power generation/seawater desalination complex plant |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1737468A (en) * | 2004-08-17 | 2006-02-22 | Lg电子株式会社 | Electric generating and air conditioning system with water heater |
US9328631B2 (en) * | 2009-02-20 | 2016-05-03 | General Electric Company | Self-generated power integration for gasification |
-
2012
- 2012-04-12 US US13/445,025 patent/US20130269347A1/en not_active Abandoned
-
2013
- 2013-04-09 EP EP13162856.2A patent/EP2650494A2/en not_active Withdrawn
- 2013-04-10 JP JP2013081697A patent/JP2013221508A/en active Pending
- 2013-04-11 RU RU2013116445/06A patent/RU2013116445A/en not_active Application Discontinuation
- 2013-04-12 CN CN2013101264093A patent/CN103375206A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3412558A (en) * | 1965-03-04 | 1968-11-26 | Applied Res And Engineering Lt | Distillation and power producing plant |
US3479820A (en) * | 1966-11-08 | 1969-11-25 | Abraham Rutenberg | Economical utilization of existing power plants |
US3476653A (en) * | 1967-02-01 | 1969-11-04 | George D Doland | Multistage distillation unit for water and power plant system |
US3760868A (en) * | 1971-01-28 | 1973-09-25 | Us Interior | Disposal of waste heat |
US6220013B1 (en) * | 1999-09-13 | 2001-04-24 | General Electric Co. | Multi-pressure reheat combined cycle with multiple reheaters |
US20110100005A1 (en) * | 2009-10-30 | 2011-05-05 | Sampson Glenn A | Water reclamation in a concentrated solar power-enabled power plant |
WO2011148422A1 (en) * | 2010-05-27 | 2011-12-01 | 日立Geニュークリア・エナジー株式会社 | Power generation/seawater desalination complex plant |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20150251924A1 (en) * | 2012-08-16 | 2015-09-10 | University Of South Florida | Systems and methods for water desalination and power generation |
US10053374B2 (en) * | 2012-08-16 | 2018-08-21 | University Of South Florida | Systems and methods for water desalination and power generation |
Also Published As
Publication number | Publication date |
---|---|
EP2650494A2 (en) | 2013-10-16 |
CN103375206A (en) | 2013-10-30 |
JP2013221508A (en) | 2013-10-28 |
RU2013116445A (en) | 2014-10-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2595192C2 (en) | Power plant with built-in pre-heating of fuel gas | |
US20120297774A1 (en) | Exhaust heat recovery system, energy supply system, and exhaust heat recovery method | |
US20120037097A1 (en) | High efficiency feedwater heater | |
EP2650494A2 (en) | Combined power and water production system and method | |
EP2470754A1 (en) | Method and system for generating high pressure steam | |
JP2015183597A (en) | Exhaust heat recovery system, gas turbine plant including the same, and exhaust heat recovery method | |
RU2425987C1 (en) | Method of power plant operation | |
JP2010038160A (en) | System and method for use in combined or rankine cycle power plant | |
RU2498091C1 (en) | Method of operation of thermal power plant | |
CN106968732B (en) | Method for operating a steam power plant steam power plant for carrying out said method | |
KR101917430B1 (en) | Power generating apparatus | |
CN105765179A (en) | Selective pressure kettle boiler for rotor air cooling applications | |
WO2016047400A1 (en) | Boiler, combined cycle plant, and steam cooling method for boiler | |
RU2561776C2 (en) | Combined-cycle plant | |
CN102588019A (en) | A saturated steam thermodynamic cycle for a turbine and an associated installation | |
JP2012013062A (en) | Binary power generation system | |
JP2010096414A (en) | Ammonia absorption refrigeration type power generating device | |
CA2983533C (en) | Combined cycle power generation | |
JP2002371861A (en) | Steam injection gas turbine generator | |
JP2016065486A (en) | Combined cycle power generation facility | |
RU2542621C2 (en) | Steam and gas plant | |
RU2553477C2 (en) | Combined-cycle plant | |
RU2686541C1 (en) | Steam-gas plant | |
RU2340779C1 (en) | Method of thermal power plant operation | |
RU2674822C2 (en) | Method of steam gas installation operation with boiler-utilizer and instant boil evaporators of feed water |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: GENERAL ELECTRIC COMPANY, NEW YORK Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:MUTHURAMALINGAM, MAHENDHRA;REEL/FRAME:028033/0430 Effective date: 20120411 |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |