This application is based upon and claims the benefit of priority from Japanese Patent Application No. 2012-162098, filed on Jul. 20, 2012; the entire contents of which are incorporated herein by reference.
Embodiments described herein relate generally to a turbine.
In a conventional power generation plant, a gas turbine, a steam turbine and so on are used as a power source for power generation.
To obtain much motive force from the turbine, a turbine of specifications of employing working fluid at a temperature equal to or higher than the heat proof temperature of turbine blades has also been developed. In this kind of turbine, for example, coolant is injected and is made to pass through the inside of the turbine blades to cool the turbine blades.
The turbine of the specifications is also constantly required to improve the energy efficiency.
In one embodiment, a turbine using CO2 as working fluid and coolant including a rotor, a plurality of moving blades, a plurality of stator blades, a working fluid transport flow path, a coolant transport flow path, and a coolant recovery flow path. The plurality of moving blades are arranged along an axis of the rotor. The plurality of stator blades constitute a plurality of turbine stages together with the plurality of moving blades. The working fluid transport flow path is configured to transport the working fluid sequentially to the plurality of turbine stages. The coolant transport flow path is configured to transport the coolant by allowing the coolant to sequentially pass through the inside of the plurality of stator blades from an upstream to a downstream of the working fluid. The coolant recovery flow path is configured to recover the coolant passing through the inside of the stator blade at a predetermined turbine stage and merge the recovered coolant with the working fluid transport flow path at a turbine stage on an upstream side of the predetermined turbine stage.
Hereinafter, embodiments will be described based on the drawings.
As illustrated in
The CO2 pump 1 compresses highly-pure CO2 made by separating water from a combustion gas (CO2 and vapor) by the humidity separator 8, and supplies the CO2 at high pressure to the combustor 4 and the CO2 turbine 5 in a branching manner through the regenerative heat exchanger 2.
Note that the highly-pure CO2 at higher pressure generated in the CO2 pump 1 may be stored or utilized for enhanced oil recovery. In short, the one CO2 pump 1 doubles as supply sources for working CO2 and cooling CO2. The working CO2 may be called working gas or working fluid, and the cooling CO2 may be called cooling gas, cooling fluid, or coolant.
The regenerative heat exchanger 2 supplies CO2 increased in temperature by heat exchange to the combustor 4. The regenerative heat exchanger 2 supplies part of CO2 to the CO2 turbine 5 before complete heat exchange. CO2 supplied to the combustor 4 is for working. CO2 supplied to the CO2 turbine 5 is for cooling or sealing. Further, the regenerative heat exchanger 2 cools through heat exchange the combustion gas (CO2 and vapor) exhausted from the CO2 turbine 5.
The oxygen producer 3 produces oxygen and supplies the produced oxygen to the combustor 4. The combustor 4 combusts injected natural gas such as methane gas, CO2 and oxygen to generate combustion gas (CO2 and vapor) at high temperature and high pressure, and supplies the combustion gas to the CO2 turbine 5 as the working CO2.
The CO2 turbine 5 is driven by the working CO2 at high temperature and high pressure. The CO2 turbine 5 rotates moving blades 13 in the turbine and a turbine rotor 11 supporting the moving blades 13, and transmits their rotation force to the power generator 6. The turbine rotor 11 is also called an axle.
In other words, the CO2 turbine 5 uses CO2 supplied from the one CO2 pump 1 mainly as the working fluid for rotating the turbine rotor 11 and the coolant (fluid for cooling).
The power generator 6 generates power using the rotation force of the turbine rotor 11 of the CO2 turbine 5. A combination of the CO2 turbine 5 and the power generator 6 may be sometimes called a CO2 turbine power generator. The cooler 7 further cools the combustion gas (CO2 and vapor) passed through the regenerative heat exchanger 2, and supplies the cooled combustion gas to the humidity separator 8.
The humidity separator 8 separates water from the combustion gas (CO2 and vapor) at low temperature outputted from the cooler 7 to generate highly-pure CO2, and returns the highly-pure CO2 back to the CO2 pump 1.
The thermal power generation system 20 is constituted by a circulation system of oxygen combustion using CO2 at supercritical pressure and is a zero mission power generation system which is capable of effectively utilizing CO2 without exhausting CO2. Use of this system makes it possible to recover and recycle the highly-pure CO2 at high pressure without separately installing facilities for separating and recovering CO2.
Hereinafter, the operation of the thermal power generation system 20 according to this embodiment will be described. In the case of this embodiment, power is generated by rotating (the moving blades of) the CO2 turbine 5 by the CO2 at high temperature (working CO2) generated by injecting and combusting CO2, natural gas and oxygen.
Then, the combustion gas (CO2 and vapor) exhausted from the CO2 turbine 5 is cooled through the regenerative heat exchanger 2 and the cooler 7 and has water therein separated in the humidity separator 8 into CO2 gas. The CO2 gas is then circulated back to the CO2 pump 1 and compressed, and most of CO2 is fed back to the combustor 4.
Next, the structure of a coolant recovery flaw path 37 provided in the CO2 turbine 5 in this embodiment will be described based on
The working fluid transport flow path 35 transports the working fluid (working CO2) from its upstream side (high pressure side) to its downstream side (low pressure side) with respect to a plurality of turbine stages each composed of a set of a nozzle (stator blade) 16 and the moving blade 13.
As illustrated in
The coolant transport flow path 36 transports the coolant (cooling CO2) from the upstream side to the downstream side while allowing the coolant (cooling CO2) to pass through the inside of the nozzle 16 at each turbine stage. More specifically, the coolant transport flow path 36 has a major flow path 36a as illustrated in
Further, the coolant transport flow path 36 passes through the inside of the nozzle 16 and then goes through the inside of a nozzle side wall 38a of the nozzle segment 38 to the outside of the main body of the nozzle segment 38 for discharge as illustrated in
On the other hand, the coolant recovery flaw path 37 recovers the coolant passing through the inside of the nozzle 16 at a predetermined turbine stage along the coolant transport flow path 36. The coolant recovery flaw path 37 merges the recovered coolant with the working fluid transport flow path 35 at a turbine stage on the upstream side of the predetermined turbine stage. Specifically, the coolant recovery flaw path 37 is composed of seal plates 40 as seal members and the nozzle segments 38 in combination as illustrated in
In more detail, a set of seal plates 40 are arranged opposite each other with a gap intervening therebetween in a gap between end faces opposite each other of a set of nozzle segments 38 to constitute the coolant transport flow path 36 and the coolant recovery flaw path 37 as illustrated in
Here, the CO2 turbine 5 in this embodiment recovers the coolant passing through the nozzle 16, for example, at a fifth turbine stage (predetermined turbine stage) 55 and merges the recovered coolant with the working fluid transport flow path 35 on the upstream side of the fifth turbine stage (for example, on the downstream side of a second turbine stage 52) as illustrated in
More specifically, the coolant is not simply transported to a further downstream side of the above-described fifth turbine stage (predetermined turbine stage) 55 but the coolant with a sufficient working pressure is merged with the working fluid transport flow path 35 from an appropriate turbine stage. As a result of this, the merged coolant can be made to serve as the working fluid.
As has been described, according to the CO2 turbine 5 in this embodiment, the enthalpy loss (energy loss) of the coolant (cooling CO2) is suppressed (the pressure of the coolant is effectively utilized). As a result of this, the energy efficiency can be increased.
Next, a second embodiment will be described based on
A CO2 turbine in this embodiment includes a coolant recovery flow path 47 in place of the coolant recovery flow path 37 in the first embodiment as illustrated in
Further, the collection flow path 37c included in the coolant recovery flow path 47 passes through (goes through) the inside of a member of an inner casing 15a (15b) as illustrated in
In more detail, the coolant recovery flow path 47 further includes a relay flow path 37d and a supply flow path 37e as illustrated in
According to the CO2 turbine in the second embodiment configured as described above, it is possible to recover the coolant (the coolant with less pressure loss due to nozzle cooling) also from a turbine stage closer to the turbine stage with which the coolant is merged and cause the coolant to function as the working fluid. Therefore, the energy efficiency can further be increased.
Next, a third embodiment will be described based on
A CO2 turbine in this embodiment includes a coolant recovery flow path 57 in place of the coolant recovery flow path 47 in the second embodiment. As illustrated in
Note that in the CO2 turbine in this embodiment, a major flow path 36a of a coolant transport flow path 36 is provided also inside the shroud segment 39. In other words, the collection flow path 57c is arranged at a position where it does not physically overlap with the major flow path 36a inside the shroud segment 39.
According to the CO2 turbine in this embodiment, it is possible to process and form the collection flow path while it is divided into a plurality of shroud segments, unlike the case where the collection flow path is processed and formed in the casing. Therefore, it is possible in this embodiment to increase the processability of the collection flow path in addition to the effects in the second embodiment.
Next, a fourth embodiment will be described based on
A CO2 turbine in this embodiment includes a coolant recovery flow path 77 in place of the coolant recovery flow path 37 in the first embodiment as illustrated in
More specifically, the stator blade re-cooling flow path 77c is provided also at a turbine stage (for example, a fourth turbine stage 54) preceding to the turbine stage at which the coolant has been recovered. In other words, the stator blade re-cooling flow path 77c is a flow path for cooling the nozzle (stator blade) 16 at a preceding turbine stage in order from a subsequent turbine stage before merging with a working fluid transport flow path 35.
Consequently, according to the CO2 turbine in this embodiment, it is possible to improve the cooling performance with respect to the nozzle 16 as well as to effectively utilize the coolant as working fluid.
According to the embodiments described above, the energy efficiency can be increased.
While certain embodiments have been described, these embodiments have been presented by way of example only, and are not intended to limit the scope of the inventions. Indeed, the novel embodiments described herein may be embodied in a variety of other forms; furthermore, various omissions, substitutions and changes in the form of the embodiments described herein may be made without departing from the spirit of the inventions. The accompanying claims and their equivalents are intended to cover such forms or modifications as would fall within the scope and spirit of the inventions.
Number | Date | Country | Kind |
---|---|---|---|
2012-162098 | Jul 2012 | JP | national |
Number | Name | Date | Kind |
---|---|---|---|
4721433 | Piendel | Jan 1988 | A |
5088888 | Bobo | Feb 1992 | A |
5217347 | Miraucourt | Jun 1993 | A |
5640840 | Briesch | Jun 1997 | A |
5782076 | Huber et al. | Jul 1998 | A |
5953900 | Bannister et al. | Sep 1999 | A |
5980201 | Benoist | Nov 1999 | A |
6269624 | Frutschi | Aug 2001 | B1 |
6340285 | Gonyou | Jan 2002 | B1 |
6612806 | Bolms | Sep 2003 | B1 |
8585357 | DiPaola | Nov 2013 | B2 |
20020150467 | Tanioka | Oct 2002 | A1 |
20100071878 | Gilchrist, III et al. | Mar 2010 | A1 |
20120067054 | Palmer et al. | Mar 2012 | A1 |
20130186101 | Mundra | Jul 2013 | A1 |
20140331687 | Palmer et al. | Nov 2014 | A1 |
Number | Date | Country |
---|---|---|
1 249 592 | Oct 2002 | EP |
9-060531 | Mar 1997 | JP |
2000-511261 | Aug 2000 | JP |
2011-32954 | Feb 2011 | JP |
WO 9618810 | Jun 1996 | WO |
WO 9812421 | Mar 1998 | WO |
WO 2012040214 | Mar 2012 | WO |
Entry |
---|
Office Action dated Oct. 6, 2015, in Japanese Patent Application No. 2012-162098, filed Jul. 20, 2012, (with English-language Translation). |
Extended European Search Report issued Sep. 18, 2014 in Patent Application No. 13158939.2. |
Number | Date | Country | |
---|---|---|---|
20140020402 A1 | Jan 2014 | US |