This invention is in the field of solar power plant technology, in particular a solar power tower structure and solar steam generators.
The following references are considered to be pertinent for the present invention:
1 A. Segal and M. Epstein, Solar Energy, 69 (suppl.), (2001), 229
2 A. Segal and M. Epstein, J. Solar Energy Engineering, 130, (2008), 011009
Solar power plants typically include solar collectors, such as a field of heliostat mirrors, which concentrate reflected sunlight on a number of receptors mounted on towers. A certain type of fluid is heated in the receptor and connected to a steam turbine type power block. The solar heat receptor cavity has generally a number of water or steam carrying tubes therein. A portion of the tubes (i.e. the boiling section) operates at a boiling temperature range suitable for heating boiler water and another portion of the tubes (i.e. the superheating section) is at a higher superheating temperature which serves as a steam superheater.
Direct steam generation in “solar tower” technology was developed and demonstrated already in the 1970's in Barstow, Calif., where an external steam receiver/boiler was installed on top of a solar tower. The receiver was built of vertical tubes creating a large cylindrical shape boiler operating in a mode of “once-through”, namely sub-cooled water enters the bottom of the tubes, flows up, boils, and finally at the top part of the tubes the saturated steam is superheated. Usually, the steam pressure range is 80-150 bars and the saturated steam temperature is therefore 296-343° C. respectively. A typical superheating temperature is around 200° C. above the saturated temperatures, namely at 500-550° C.
However, the superheating section operating in the once-through mode could not use any concentrated solar radiation until enough steam was generated at the boiling section. Therefore, the focusing strategy of the field was complicated. Also, the metal surface temperature of the superheating section was at least 50° C. above the steam inside, typically at 550-650° C., at which radiation losses outside became substantial. In addition, due to changes in solar intensity is during the day, the wetted sections in the tubes (e.g. region of two-phase flow) could become dry and suffer from overheating.
This approach was therefore replaced later by separating the superheating section from the boiling section. A typical solar thermal generation system of this type is illustrated in
Steam systems used in combination with solar towers are known. Such steam systems comprise solar receivers in which the boiling section and the superheating sections are configured as two separate adjacent elements, each placed inside an insulated cavity to reduce thermal losses. By using such configuration, the thermal losses of the boiling section are relatively small. Typically the surface temperatures of such boiling sections are in the range of about 400-450° C.
It should be understood, that conventionally, the insulated cavity has an to aperture through which the concentrated radiation enters, diverges inside the cavity and strikes the boiler tubes. The cavities are insulated enclosures, made of metal casing internally insulated, and the tube panels are installed inside, usually along the walls of the cavity. The cavity is costly and also suffers from radiation spillage around the aperture stemming from side heliostats in the field and from the changes in size of the solar image at various times of the day. Also, the cavity has a limited view angle, and therefore can match only a section of a surrounding heliostat field. Therefore, a single cavity can operate only with a specific limited field e.g. north field (in the northern hemisphere) or several cavities should be installed in a large commercial size plant to face different parts of the surrounding heliostat field. This results in operating conditions which are not uniform and which exist in each of the cavities and vary during the daily hours. Also, the cavity walls have to warm up every morning, which increases the startup time of the steam system.
Moreover, in such systems, it is not feasible technically and economically, to store superheated steam for later use during hours when the sun is not available. Even if the steam system is designed with thermal storage, the steam produced during the sunny hours has to exchange heat (through a first heat exchanger) to other storage mediums, e.g. molten salt (for example, eutectic mixture of sodium and potassium nitrates). During the time when the sun is not available, heat stored in the storage medium is extracted through a second heat exchanger to generate steam at inferior conditions because of temperature losses in each of these heat exchangers. Therefore, there is a need to provide a solar steam generator system having increased thermal efficiency.
The present invention provides a novel solar steam generator comprising a solar steam boiler compartment carrying water surrounding an internal superheater compartment. The boiler compartment is exposed to a first concentrated solar radiation. The boiler compartment is configured and operable to heat water to saturated temperatures and generate saturated steam. The boiler compartment operates as an integrated cavity enclosing the superheater compartment, reducing the thermal losses of the superheater compartment to the outside environment and absorbs most of the thermal losses of the superheater compartment. The internal superheater compartment is exposed to a second concentrated solar radiation and is configured and operable to superheat the saturated steam generated in the boiler compartment. The boiler compartment and the superheater compartment are thus arranged one with respect to the other such that the boiler compartment surrounds the internal superheater compartment. The boiler compartment therefore protects the superheater compartment from thermal losses from the environmental conditions, absorbs its thermal losses and thus increases the thermal efficiency of the solar steam generator. The solar steam generator of the present invention therefore provides effective solar energy collection (i.e. spillage losses of one compartment are used by the other and on the other hand reduces the thermal losses owing to the heat exchange between the concentric compartments. This configuration enables preheating of the superheater compartment by the boiler compartment during the start-up time, economical saving by eliminating the construction of insulated cavities enclosures in the state-of-the-art solar boilers and allows for effective energy storage.
It should be understood that as described above, typically a solar steam generator comprises a cavity surrounding the superheater compartment and/or the boiler compartment to reduce thermal losses. By using the configuration of the present invention, the steam generator does not include a conventional cavity surrounding the superheater compartment as an additional separate element. The boiler compartment reduces the thermal losses of the superheater compartment and therefore operates as a cavity. The boiler compartment has an aperture facing a part of the heliostat field. The aperture in the boiler compartment is configured for supplying energy to the superheater compartment.
Therefore, the arrangement of the boiler and superheater compartments provides that the boiler compartment is configured such that the boiler compartment operates as an integrated cavity reducing thermal losses and startup time of the superheater compartment. The startup time of the superheater refers to the initialization period of time that the steam generator goes through until the creation of superheated steam.
In some embodiments, the boiler compartment comprises an aperture through which the superheater compartment is exposed to the second concentrated radiation. It should be understood that when the steam process starts from cold water, the production of steam at 100 bars, requires an enthalpy of the water at the boiling point (312° C.) of 1.41 MJ/kg, and an evaporation enthalpy of 1.31 MJ/kg (the total enthalpy of the superheated steam at 100 bars and at 512° C. is 3.4 MJ/kg). Therefore, the superheating requires about 25% of the total enthalpy for the production of the saturated steam.
In some embodiments, the superheater compartment is configured as a second open cylinder embedded/surrounded with/by the cavity of the boiler compartment. The superheater compartment includes a plurality of open tubes. A part of the heliostat field, e.g. the north part, is configured to affect the superheating. It is operated when enough saturated steam is produced in the boiler compartment.
It should be noted that light spillage rays that strike around the superheating aperture (the solar radiation inside the collection angle of the superheater compartment, not entering into the aperture) is not lost (as usually occurring in conventional systems) but rather strikes the boiler compartment. Also, when heated up in the morning, the boiler compartment warms up gradually and warms, indirectly, the internal superheating tubes to the boiler temperature, and thus shortens the superheater compartment startup time in a safe manner. Therefore, the arrangement of the boiler and superheater compartments is configured such that the boiler compartment exploits light spillage of the second concentrated solar radiation and heats the internal superheater compartment during the start-up time.
In some embodiments, the solar steam generator comprises a steam drum configured and operable to separate the phases of the saturated steam/water mixture.
The solar steam generator may also comprise recycling pumps placed between the steam drum and the boiler compartment to enable the operation of the boiler compartment in a recycle mode.
In some embodiments, the solar steam boiler compartment comprises an array of tubular water members (pipes) arranged along a first arc-like path defining an aperture through which the superheater compartment is exposed to the second concentrated radiation. The first arc-like path is exposed to the first concentrated solar radiation enabling heating of the tubular water members. The first arc-like path defines an inner space accommodating the internal superheater compartment, thus enabling heat exchange between the boiler compartment and the superheater compartment. The superheater compartment comprises an array of tubular steam members arranged along a second arc-like path. The second arc-like path defines an aperture through which the tubular members are exposed to the second concentrated solar radiation enabling heating of the tubular steam members.
In some embodiments, the first arc-like path and the second arc-like path define a common aperture.
In some embodiments, at least one of said first and second arc-like paths defines substantially semi-cylindrical geometrical circumferences.
In some embodiments, the arrangement of the boiler and superheater compartments is concentric.
In some embodiments, the arrangement of the boiler and superheater compartments is configured such that the boiler compartment and the superheater compartment are exposed to spatially separated first and second concentrated light portions having substantially non-overlapping solid-angle sectors of radiation focusing towards (incident on) the solar steam generator. The boiler and superheater compartments are exposed to radiations propagated from different directions.
In some embodiments, the internal superheater compartment is operable at a temperature of typically about 200° C. above saturated temperatures (but not limited to) and/or at superheating temperatures in the range of about 500-550° C.
The steam generator of the present invention is therefore an integrated superheater/boiler arrangement assuring high thermal efficiency, low thermal losses from the hotter superheater compartment, shorter startup time and better optical efficiency. The heliostat field reflects the solar radiation toward the steam generator. The solar radiation irradiating the steam generator is split between the boiler compartment, which usually occupies the majority of the field, and the superheater compartment.
According to another broad aspect of the present invention, there is provided a solar tower power structure comprising: a solar tower; a solar steam generator placed on top of the tower, and a heliostat field defined by controllably tracking heliostats arranged such that the field surrounds the steam generator. The heliostat field is configured and operable to reflect and concentrate solar radiation onto the steam generator in at least two radiation propagation sectors having predetermined directions. A first sector of the heliostat field is configured to focus a first part of the concentrated radiation onto a first arc-like path of the boiler compartment and a second sector of the heliostat field is configured to focus a second part of the concentrated radiation onto the superheater compartment through an aperture formed in the boiler compartment.
In some embodiments, there is provided a solar power plant comprising a solar steam boiler and a superheater configured as two concentric compartments of the same solar power receiver, such that the solar steam boiler and the superheater define a common energy collection surface. This on one hand provides effective solar energy collection (i.e. spillage losses of one compartment are used by the other, and on the other hand reduces thermal losses) owing to the heat exchange between the concentric compartments. This configuration also allows for effective energy storage, by using for example “beam down” optics.
The steam generator may be connected to a steam turbine power plant.
The solar steam generator is placed on a tower surrounded by a field of heliostats (tracking mirrors). A part of the field is configured for boiling the water and for generating steam and another part of the field is used for superheating the steam.
In some embodiments, the solar tower power structure comprises a reflector configured and operable to form beam-down optics and to reflect sunlight energy to the ground, and a ground receiver configured and operable to heat a storage medium for further generation of steam. The reflector is positioned to form beam-down optics. The ground receiver receives sunlight energy from the reflector. The beam-down system comprises inter alia three main components: a section of the heliostat field, the tower reflector and the ground receiver/secondary concentrator e.g. compound parabolic concentrator (CPC). The reflector causes the ray oriented to the aim point of the field to be reflected down to the receiver entrance located near the ground. Such beam-down optics can be configured and operable for ground storage. There are a number of configuration parameters, which connect the layout of the heliostat field, the size, location and inclination of the tower reflector, and the size and configuration of the array of the ground CPC elements. The sizing of the tower reflector is directly linked to the layout of the heliostat field and the geometry of the ground secondary concentrator. It depends on its position relative to the aim point of the field, amount of spillage around it, and the allowable solar flux striking the tower reflector. Its position influences the size of the image at the entrance plane of the ground CPC and the spillage around the CPC aperture. The spillage around the CPC is also directly related to the exit diameter of the CPC (equal to the entrance opening of the solar reactor, matching the CPC exit) and therefore linked to the input energy concentration, thermal losses, and working temperature in the steam generator.
In this case, the heliostat field is divided into three sectors. A first sector of the heliostat field is configured to focus the first part of the concentrated radiation onto the boiler compartment; a second sector of the heliostat field is configured to focus the second part of the concentrated radiation onto the superheater compartment; and a third sector of the heliostat field is configured to focus a third part of the concentrated radiation onto the tower reflector.
In some embodiments, the third sector of the heliostat field surrounds the tower in a circular manner.
In some embodiments, the heliostat field is configured to orient the solar radiation at a predetermined aim point on an external surface of the boiler compartment. Alternatively, the heliostat field is configured and operable to aim at different aim points along an external surface of the boiler compartment or on its main geometrical axis to provide substantially a uniform radiation flux on the external surface of the boiler compartment.
The solar radiation is then used to heat the storage medium directly. The storage medium is thus not heated by the steam via a heat exchanger. During the day, the superheated steam is directly generated in the tower's top receivers, and in the evening, the stored heat is extracted from the storage medium e.g. molten salt storage, for further generation of steam and for providing extra hours of operation. The direct heating of the storage medium saves heat exchanges, piping and temperature losses during the charging of the storage as done in state-of-the-art technology. In this case, a part of the heliostat field is dedicated to the storage of solar energy and its size depends on the desired number of storage hours. The storage unit is placed on the ground close to the tower base.
According to another broad aspect of the present invention, there is provided a method for steam generation. The method comprises: integrating a boiler compartment for water circulation therein with a superheater compartment for receiving saturated steam from the boiler compartment, and exposing the boiler compartment to solar radiation and exposing the superheater compartment to solar radiation through the boiler compartment, thereby enabling saturated steam to be generated in the boiler compartment, and upon reaching the desired saturated temperatures, to pass to the superheater compartment and to generate superheated steam in the superheater compartment upon reaching superheating temperatures. The saturated steam generated/produced in the boiler compartment is separated from the water circulating in the steam drum and is then transferred and flows into the superheater compartment for further heating and then is fed into the turbine.
In some embodiments, the method comprises at least partially embedding the superheater compartment inside the boiler compartment.
In some embodiments, the method comprises directing two portions of the solar radiation onto respectively the boiler and superheater compartments.
The method may comprise reflecting solar radiation by a heliostat field towards a reflector to thereby generate a concentrated reflected radiation, and directing the concentrated reflected radiation onto a ground receiver in which a storage medium is placed, to thereby provide thermal storage.
In order to understand the invention and to see how it may be carried out in practice, embodiments will now be described, by way of non-limiting example only, with reference to the accompanying drawings, in which:
Reference is made to
In a specific and non-limiting example, the boiler/external receiver 102 is composed of about 450 tubes, each having a diameter of 5 cm, forming a semi-cylinder (i.e. a part of its circumference is open) of a radius of about 5 m and height of about 8 m. The open part of the semi-cylinder faces a predetermined direction e.g. the north direction with an aperture of about 7.6 m width and 6 m height. The superheater compartment surrounded by the boiler compartment is shaped as an arc with a radius of about 4 m. The superheater compartment is composed of about 330 tubes, each having a diameter of about 5 cm and a height of about 8 m, forming a semi-cylinder. The aperture of the semi-cylinder faces a predetermined part of the heliostat field. In this connection, reference is made to
In this specific and non-limiting example, the heliostat field is composed of 1900 heliostats. Each heliostat has a gross area of 100 m2 and reflective surface of 95 m2. This field has been optimized following the method described in [1] which is incorporated herein by reference, resulting in an elliptic field having a semiaxis of 420 m in the North-South direction and semiaxis of 460 m in the an East-West direction. The tower is located 140 m south of the ellipse center. The first row of heliostats is at 70 m distance from the tower.
The S-sector, comprising 1113 heliostats, collects and reflects about 64 MW (assuming direct insolation of 800 W/m2, average cos φ=0.85, heliostat reflectivity 0.9, average shadowing 1%). The rays deflected by the heliostats are directed to an aim point taken at 138 m and hit the external boiler compartment. The average flux on this receiver (i.e. external circumference of the boiler compartment) is about 220 kW/m2 and might have higher peaks incident on some zones/regions on the boiler compartment. In order to avoid this situation and provide substantially uniform radiation flux on the surface of the boiler compartment, the heliostats aim the reflected rays to variable aim points by dividing the S-sector in groups of heliostats having different aim points, namely different groups of heliostats focus the radiation on different locations along the boiler surface. The inventors have estimated that by using the configuration of the external boiler compartment as described above, the boiler compartment can absorb daily (at the design point) about 210 MWh that corresponds to a production of about 495.6 tons of saturated steam/day at 100 bars (boiling point 311.8° C.).
The solar radiation originated in the N-sector is dedicated to superheat the steam produced by the boiler compartment. The superheater compartment is placed inside the cavity formed by the external receiver. The aim-point of this group of heliostats has been calculated to be at 138 m on the tower axis. About 20.5 MW enter the cavity at the design point with a negligible amount of spillage. Being a cavity receiver, the calculus is more complicated, because radiation heat exchange inside a cavity occurs. Following these calculations, the daily energy absorbed in the superheater receiver is about 123 MWh. This amount of energy superheats the above amount of saturated steam to 550° C. (degrees superheat of 238.2° C.) assuming 85% thermal efficiency of the superheater compartment.
Reference is made to
In some embodiments, the solar tower power structure 200 comprises a reflector 204 configured and operable to generate beam-down optics and a ground receiver 202 configured and operable to heat a storage medium (e.g. molten salt) pumped through it to a hot storage tank, and to receive concentrated sunlight from the reflector 204, in order to continue operating a number of hours after sunset. The ground receiver 202 collects the rays reflected by a tower reflector 204 as described by [2] and incorporated herein by reference. Generally, the tower reflector is an optical system comprising a quadric surface mirror (hyperboidal or ellipsoidal), where its upper focal point coincides with the aim point of a heliostat field and its lower focal point is located at a specified height, coinciding with the entrance plane of the ground receiver. In this specific but non-limiting example, the tower reflector 204 is situated at a height of 118 m and having a hyperboloid shape with radius of 24.2 m and a total area of 1595 m2. The beams from the heliostats are reflected downward by the reflector situated below their aim point. The calculations take into assumption a solar power tower structure producing power of 100 MW.
The ground receiver 202 comprises a compound parabolic concentrators (CPC) cluster. In the ground receiver 202, the molten salt is heated from 250° C. to 550° C. and is used for thermal storage. Therefore, this configuration directly uses solar radiation for a storage medium and eliminates the need to use heat exchanger(s).
The power entering the ground receiver at the design point is 19.5 MW (for this specific example). On a designated day, the ground receiver can absorb about 120 MWh, meaning about 3 hours of storage.
In a specific and non-limiting example, the ground receiver 202 is configured as a cavity having at its ceiling, a plurality of apertures (e.g. of 1.6 m diameter), endowed with compound parabolic concentrators (CPC). Each CPC can have a hexagonal cross section at its entrance with an area of 37 m2 and a height of about 15 m (CPC truncated).
As illustrated in the figure, the S-sector is focused onto the boiler compartment the N-sector is focused onto the superheater compartment and the C-sector is oriented to an aim point at 140 m. The rays intersect the reflector 204 (e.g. hyperboloid mirror).
Number | Date | Country | Kind |
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61241057 | Sep 2009 | US | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IL2010/000723 | 9/2/2010 | WO | 00 | 4/11/2012 |