• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A CSP system is disclosed which couples a thermal and a chemical energy pathway. The thermal pathway utilizes a heat transfer fluid to collect concentrated sunlight as thermal energy at medium temperature and transfer this energy to a thermal-to-electric power cycle. In parallel, the chemical pathway uses a redox material which undergoes direct photoreduction in the receiver to store the solar energy as chemical potential. This redox material is then oxidized at very high temperatures in the power cycle in series with the thermal pathway heat exchanger. This coupling allows the receiver to perform at the high efficiencies typical of state of the art thermal power towers while simultaneously achieving the power cycle efficiencies typical of natural gas combustion plants and achieving a very high overall solar-to-electric conversion efficiency.
    公开号:ES2544002A2
    申请号:ES201590033
    申请日:2013-10-10
    公开日:2015-08-26
    发明作者:Luke Erickson；Russell Muren
    申请人:Abengoa Solar LLC；
    IPC主号:
    专利说明:

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    P201590033
    06-12-2015 DESCRIPTION
    Method and associated chemical-thermal solar energy system. Technical field
    The embodiments set forth herein include systems and methods in the field of concentration solar energy generation ("CSP"), also known as thermal solar energy generation. The exposed systems and methods generally use two combined parallel energy paths, one thermal and one chemical, to convert solar energy into electrical energy with high efficiency. Specifically, the disclosed embodiments include a solar receiver in combination with a separate chemical energy storage material and a heat transfer fluid that flows or is transported in the separate tracks. The chemical energy storage material undergoes low temperature photoreduction in the receiver. In addition, the heat transfer fluid ("HTF") is heated to an operational temperature in the solar receiver. The chemical energy storage material and the HTF are used to activate an energy cycle that operates at relatively high temperatures because the chemical energy storage material is oxidized exothermically as, or in sequence with, the HTF being cooled . Background
    Solar concentration techniques can generally be divided into thermal systems for the generation of electrical energy and chemical systems for the production of fuels and chemical processing. Variations in thermal CSP plants that use different types of reflector configurations such as, depressed surfaces, parabolic plates, and heliostat fields are well known in the art. Known CSP systems use many alternative heat transfer fluids such as oils, molten salts, and steam and can be used to perform different energy cycles such as the Rankine steam, Supercritical steam Rankine, and Dioxide Brayton cycles. of supercritical carbon.
    The current state of the art in high temperature CSP towers is represented by direct steam generating towers such as those shown in US Patent Application 2008/0302314 and molten nitrate salt towers such as those shown in United States Patent Application 2008/0000231. These types of towers normally operate at temperatures up to approximately 600 ° C. The greatest power generation efficiency could be achieved with operational temperatures of more than 600 ° C.
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    It is difficult to achieve operational temperatures above 600 ° C with conventional CSP strategies.
    Concentration solar towers for chemical reactions have been suggested in several ways. A known concept uses concentrated sunlight to generate heat to decompose biomass, such as the one described in US Patent Application 2010/0249468. Another known method is characterized by the use of concentrated sunlight to cause water to undergo photolysis through interaction with catalysts, such as that described in US Patent 4,045,315. Other technologies use concentrated sunlight and an oxidation / reduction cycle to create hydrogen gas from water or carbon monoxide gas from carbon dioxide, such as those described in US Patent Application 2009/0107044 . The above chemical methods are not particularly suitable for electric power generation using energy turbines based on energy cycle.
    Maximizing the efficiency of a power plant for a concentrating solar energy system is of great importance because it produces a reduction in the total cost of the system requiring a smaller solar field and receiver for the same net energy production . In a concentrated solar power tower, total solar to electric efficiency is the product of solar field efficiency, receiver (solar to thermal) efficiency, storage efficiency, and (solar to electric) cycle efficiency. Energy. The thermal to electrical conversion system is very similar to fossil fuel systems at comparable temperatures, however, the conversion efficiency of a solar energy cycle is typically much lower than that of a combined cycle gas plant due to low operational temperatures
    The embodiments set forth herein are directed to overcome one or more of the problems set forth herein. Summary of achievements
    The embodiments set forth herein include solar energy concentration systems and methods (CSP) that combine a thermal and chemical energy path. The thermal path uses a heat transfer fluid to collect concentrated sunlight as thermal energy at an average temperature and transfer this energy to a cycle of thermal to electrical energy. In parallel, the chemical pathway uses a redox material that undergoes direct photoreduction in the receiver to store solar energy as a chemical potential. This redox material is then oxidized at very high temperatures in the series energy cycle.
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    with heat exchanger heat track. This combination allows the receiver to work at high efficiencies typical of thermal energy towers state of the art while at the same time achieving energy cycle efficiency typical of natural gas combustion plants and achieving high overall efficiency Conversion from solar to electric.
    An exposed embodiment is a CSP system comprising a solar receiver configured to receive concentrated solar luminous flux and an amount of heat transfer fluid (HTF) in thermal communication with the solar receiver so that the concentrated solar luminous flux heats the HTF. The system also includes a heat exchanger in thermal communication with the HTF that provides heat exchange between the HTF and the working fluid of a power generation cycle. In addition, the system also includes a chemical energy storage material that flows in a chemical path combined with the thermal path. The chemical energy storage material is also in communication with the solar receiver so that the concentrated solar luminous flux reduces an amount of chemical energy storage material in the reduction part of an oxidation-reduction reaction. In this way, the chemical energy storage material can alternatively be referred to as redox material.
    The system also includes an oxidizer in communication with the chemical energy storage material, the oxidizer providing the exothermic oxidation of the chemical energy storage material and also providing heat exchange between the chemical energy storage material and the working fluid. of the energy cycle. In this way, the system uses parallel energy paths, one thermal and one chemical. The use of two combined paths in the solar receiver results in a high efficiency CSP plant.
    The system may further include storage of chemical energy operatively associated with an HTF conduit. In addition, the system may include separate chemical energy storage that includes a chemical storage system that reduces the operation of chemical energy storage material from the solar receiver; and / or an oxidized chemical storage system that receives the chemical energy storage material from the oxidizer.
    An alternative embodiment set forth herein comprises a method of generating power that has certain steps that can be performed in any suitable order and that will typically be performed in a cyclic manner. The embodiments of the method are initiated by providing a solar receiver configured to receive the concentrated solar light flux. HTF of any suitable type is flowed, transported or otherwise brought to thermal communication with
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    the solar receiver where the HTF is heated with concentrated solar luminous flux. The heated HTF is then flowed or transported from the solar receiver to a heat exchanger in the heat transfer fluid conduit. In the heat exchange, the heat is exchanged between the heated heat transfer fluid and the working fluid of an energy cycle.
    In a parallel cycle, a (redox) chemical energy storage material in communication with the solar receiver is irradiated by the concentrated solar luminous flux thereby causing a quantity of chemical energy storage material to be reduced. The reduced chemical energy storage material is then made fluid
    or transported between the solar receiver and an oxidizing element. In the oxidizer, the chemical energy storage material is oxidized causing it to release heat energy. The heat energy released is exchanged with the working fluid of the energy cycle. Energy can be generated with the heated working fluid of the energy cycle.
    The exposed embodiments are all characterized by having double paths of thermal and chemical energy. The embodiments can be implemented in any type of concentration solar energy apparatus and with any type of cycle generation or power generation cycles. Brief description of the drawings
    Fig. 1 is a schematic diagram of the simplified system illustrating a prior art CSP system.
    Fig. 2 is a simplified system schematic diagram illustrating an embodiment of the system having chemical energy pathways as described herein.
    Fig. 3 is a schematic diagram illustrating a redox cycle.
    Fig. 4 is a schematic simplified energy cycle illustrating an energy cycle suitable for implementation with systems described herein.
    Fig. 5 is a simplified receiver scheme illustrating how the combined pathways set forth herein reduce radiation losses.
    Fig. 6 is a simplified system schematic diagram illustrating an alternative received design.
    Fig. 7 is a flow chart representation of a representative method as set forth herein.
    P201590033
    06-12-2015 Detailed description
    Unless otherwise indicated, all numbers expressing quantities of ingredients, reaction conditions of dimensions etc. used in the specification and the claims are understood to be modified in all cases by the term "approximately".
    In this application and claims, the use of the singular includes the plural unless otherwise indicated. In addition, the use of "o" means "and / or" unless otherwise indicated. In addition, the use of the term "including" as well as other forms, such as "includes" and "included," is not limiting. Also, terms such as "element" or "component" encompass both elements and components comprising a unit and elements and components comprising more than one unit unless otherwise indicated.
    As noted above, known CSP systems generally operate at significantly lower total efficiency when compared to a combined cycle power generation plant. The reduced efficiency of a CSP system is mainly due to the low operating temperatures. To maximize the efficiency of the total solar plant, it would be advantageous to use the high efficiency energy cycles available for combined cycle gas systems with a CSP plant, assuming this could be done without compromising the balance of the CSP plant. This achievement could not be carried out in the state-of-the-art solar power towers, such as nitrate salt towers or superheated steam towers. In these towers, the energy path is strictly thermal, which means that all the energy transferred from the receiver to the energy cycle is transferred as thermal energy. A representative energy flow in a conventional CSP system is illustrated in Fig. 1. Solar radiation is concentrated by the solar field. The concentrated solar radiation is transferred as thermal energy to the receiver and captured with an intermediate heat transfer fluid. The thermal energy is then stored as heat transfer fluid from hot storage in large tanks. When needed, the hot heat transfer fluid is sent to the energy cycle through a heat exchanger. Finally, thermal energy is converted into electricity in a thermodynamic energy cycle.
    In the known CSP plant configurations, the factors control the receiver and the energy cycle efficiencies fundamentally counteract each other. The energy cycle efficiency increases with the heat transfer fluid inlet temperature. However, the efficiency of the solar receiver decreases with the increase in temperature due to higher heat losses from convection and radiation. In addition, the receiver has limits
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    absolute temperature of salt decomposition and the receiver contains restrictions. Because the temperatures of the energy cycle and the receiver are fundamentally combined in a plant with only one thermal energy path, very high total system efficiency cannot be achieved.
    The embodiments of the system and method set forth herein use parallel, thermal and chemical pathways in a high efficiency concentrated solar power plant (CSP). As shown in Fig. 2, a representative system 100 includes one or more thermal paths 102 consisting of a heat transfer fluid (HTF) such as steam / water, molten salt
    or solid, molten or solid metal, oil, a phase change material or other HTF suitable in thermal communication with the solar receiver 104. The solar receiver 104 is typically associated with a central receiving tower and receives the concentrated solar light flux reflected by A field of heliostats. The methods set forth herein could be implemented with other CSP designs, however, that include but are not limited to depressed parabolic, linear Fresnel, and plate / motor surface systems.
    The HTF heated in the solar receiver 104 is flowed or transported to a heat exchanger 106 in a heat transfer fluid conduit 108. It is important to note that although conventional heat transfer fluid (HTF) terminology is used here , the system and methods can be implemented with a solid, liquid, gaseous or phase-changing HTF. Thus, the heat transfer fluid conduit 108 can be a suitable pipe or conduit system and valves for fluid flow control, or the heat transfer fluid conduit 108 can be any type of system suitable for solids transport. The heat transfer fluid conduit 108 may include fluid flow sections in some solid transport sections.
    In heat exchanger 106, thermal energy is exchanged between HTF and the working fluid of the energy cycle. The exchanger (s) can be of any type or any level of sophistication necessary to provide heat exchange between the HTF and a power generation cycle work fluid. The heat exchanger 106 and other subsystems are, for thermal convenience, described and shown in the figures as simple schematic elements. All the elements of a commercial system would be implemented with more complex devices. As generally shown in Fig. 2, the heated working fluid activates a power generation cycle 110. Accordingly, the working fluid is either directly or through an intermediate energy cycle fluid, converted in mechanical energy and then in electrical energy.
    System 100 and the methods set forth herein also include a chemical energy path that
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    It includes a chemical energy storage material that undergoes reversible oxidation and reduction reactions (alternatively referred to herein as a "redox material"). In particular, the redox material is reduced in the receiver 104 and oxidized in an oxidizer 112. The oxidizer or an associated apparatus also provides heat exchange with the working fluid of the energy cycle 110. The redox material is made fluid or transported between the receiver and the oxidizer in a conduit of chemical energy storage material 114 that may be configured for fluid flow or solids transport as described herein with respect to the HTF conduit 108.
    As noted here, the redox material is directly photoreduced by the high concentration of photons incident on the receiver 104, thus, the redox material stores the absorbed electromagnetic energy as a chemical potential. In oxidizer 112, the redox material is oxidized, thereby releasing high temperature thermal energy. A representative diagram of this type of chemical process is shown in Fig. 3 and described below. It is important to note that the oxidizer element 112 will typically be implemented with significantly more complex apparatus than those shown in Fig. 2. For example, the oxidizer 112 may include separate oxidation chambers, air or gas supplies, fluidized bed, heat exchanger and other elements.
    Typically, CSP systems achieve a certain level of efficiency when implemented, for example, with molten salt or steam receivers of the state of the art. In addition, the power plants implemented with combustion energy cycles have very good performance (for example, combined cycle natural gas dishes). The combined thermochemical architecture described here allows a CSP system to have an advantage over both power generation technologies without the consumption of any fossil fuel and environmentally harmful emissions. Thus, the exposed systems and methods have an advantage over the state-of-the-art CSP plants known in the increased efficiency of thermal to electrical conversion due in part to the high temperature of the oxidation process. For example, typical CSP molten salt or steam-based power generation plants achieve thermal to electrical efficiencies of 40-44%. As shown in Fig. 2 and detailed below, the systems and methods described can achieve adequate temperatures to realize a power generation system that has total efficiencies of approximately 60% that are much closer to the efficiencies presented by plants of combined cycle natural gas.
    The chemical energy path described above represents the new system architecture in the CSP industry. While the thermal path transfers energy by heating and cooling a
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    Heat transfer fluid, a chemical pathway transfers energy by storing energy in a material through an endothermic reaction and releasing it in an exothermic reaction. As noted above, the chemical pathway consists of a material that undergoes reversible reduction and oxidation reactions. For illustrative purposes, a set of potential reactions is shown in Fig. 3, although the embodiments set forth herein can be implemented with any alternative redox material.
    As shown schematically in Fig. 3, a representative redox cycle is characterized by a reduction stage (upper frame) that takes place in the solar receiver. A photon hits the oxidized material and breaks it into a reduced material and free oxygen. This stage depends only on the photon supply energy to break the bond between the metal and oxygen atoms. The reduced material (MnO in this example) is transferred to a storage tank. When necessary, it is transferred to the energy cycle in which it is burned in oxygen releasing heat and looping back creating the original oxidized material.
    The previous representative redox process is governed by the balance between the energy of the chemical bonds and the energy of the photon. The bond energies are typically described in terms of Gibbs free energy, ∆G, and the energy required to perform an endothermic reaction or the energy released by an exothermic reaction can be calculated with Equation 1
    ∆Greaction = Σ coeffproducts-∆Gproducts -Σcoeffreactive ∆Greactive Equation 1
    The ∆G reference values can be obtained from the chemical texts NITS databases or other sources. The coefficients come from the balanced chemical equation. For photoreduction to occur, the energy of the photon that causes the reaction must be higher than the free energy required for the reaction to occur. To compare the energies, photon energy can be calculated from Equation 2.
    Efotón = hc / λ Equation 2
    where h is the Planck constant, c is the speed of light, and λ in the photon wavelength. The photons available for solar capture are generally in the visible range, 380-750 nm.
    Several potential redox materials have been examined for their ability to adapt in the systems described using Equations 1 and 2. A sample of the results is presented in Table 1. All the presented equations assume a temperature of
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    500 ° C reaction.
    Lenght of
    ∆Greaction
    Balanced chemical equation photon wave [kJ / molreactant]
    required
    Mn2O3 + hv → 2MnO + ½ O2 30 <3940 nm
    2Al2O3 + hv → 4Al + 3O2 717 <167 nm
    CoO + hv → Co + ½O2 176 <678nm
    NiO + hv → Ni + ½O2 167 <718nm
    Table 1. Sample calculations for direct photoreduction of redox material
    From this table, it can be seen that aluminum is not a good choice of material
    5 redox because its oxide cannot be reduced by visible light. Cobalt and nickel oxides cannot be absorbed from the entire red end of the spectrum but could capture most of the available energy. Manganese oxide, alternatively, does not absorb all the energy of the visible light for the reaction so that instead some photon energy will be converted to kinetic or thermal energy.
    10 An ideal chemical energy storage (redox) material for the system described will have four characteristics:
    -a high absorption of the UV spectrum and visible so that the maximum maximum amount of light is absorbed.
    -a difference in energy between the oxidized and reduced states slightly smaller than
    15 the energy of the visible spectrum photons so that the greatest amount of energy is converted from electromagnetic potential to chemical potential.
    -a low oxidation rate at lower temperatures and in the absence of an ignition mechanism to minimize re-oxidation before desired time.
    -a high oxidation rate under energy cycle conditions to maximize efficiency.
    Various materials that present these characteristics to varying degrees have been previously identified. Generally, the best known materials are transition oxides. By
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    For example, manganese oxides and cobalt oxides with additions of iron oxide and aluminum oxide have previously been identified as major amounts to direct photoreduction technologies. See for example, General Atomics. “Thermochemical heat storage for concentrated solar power based on multivalent metal oxides.” DOE Program Review, May 2011. http://www1.eere.energy.gov/solar/csp_pr2011.html accessed December 19, 2011, whose Description is incorporated here in its entirety. However, heat loss management was identified as a problem in the previous rotary kiln reactor study. Additionally, the fraction of material undergoing the reduction is low, of the order of 3%, which implies high capital costs.
    The systems and methods presented here use solar photons to directly reduce the redox material. The energy does not travel through a thermal state between the electromagnetic potential state (solar photon) and the chemical. In fact, the exposed technology works best with materials that do not dissociate thermochemically below 1400 ° C, the hot energy cycle temperature, which is much hotter than what can be achieved with known CSP technologies.
    The systems and methods presented here can be used to drive any type of power generation cycle. The most suitable known energy cycle to operate with near efficiencies or above 60% is however, the Brayton air cycle or a variation thereof. A highly simplified diagram of a possible non-limiting and representative energy cycle configuration 400 is illustrated in Fig. 4. The example configuration of Figure 4 illustrates how the thermal and chemical heat sources described above could be integrated into a cycle of Brayton energy of air 402 in combination with the tail cycle or “bottoming” of steam Rankine 404. As noted above, other energy cycles can also be used. Certain advantages can be obtained if the working fluid contains an oxidizing agent. For example, an open loop supercritical carbon dioxide cycle could be used in which CO2 or H2O would be reduced to CO or H2, respectively, which could then be used for the generation of liquid fuel or as fuel for fuel cells. .
    In the embodiment of Fig. 4, the upper open air Brayton cycle uses air as a working fluid and an oxidizing agent. The air is initially compressed in the compressor 406 which is driven by a mechanical connection to a downstream turbine 408. The compressed air from the compressor 406 is heated through heat exchange with the HTF in the heat exchanger 106. The air heated and compressed oxidizes the chemical energy storage material in the oxidizer 112 and thus is further heated by
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    Direct contact or indirect heat exchange with the chemical energy storage material as it releases heat during the exothermic oxidation reaction. The now high-temperature air drives one or more turbines 408 which in turn drives the compressor 406 and one
    or more generators (not shown in Fig. 4) to generate electricity.
    The embodiment of Fig. 4 also includes a tail cycle or bottoming of lower steam Rankine 404 that receives some cooled air from the turbine outlet 508. The heat is exchanged between the air and a flow fluid. secondary work, for example steam, in a heat exchanger / exchanger 410. The heated steam then drives a second turbine 412 or a second series of turbines which in turn drives one or more generators to generate electrical energy. The steam leaving the turbine 412 is condensed in a condenser 414 and pumped as water back to the recuperator / heat exchanger 410 by means of the pump 416.
    A source of inefficiency for direct and thermal chemical direct photoreduction receptors is the loss of heat during the reduction stages. In a combined thermochemical receiver as described herein, some or most of the heat losses of the redox material can be recaptured by the thermal receiver and any residual heat stored in the redox material at the outlet of the receiver can be transferred again to Preheat the HTF entering the receiver.
    A diagram illustrating a receiver design with improved heat loss management is shown in Fig. 5. The incident solar radiation (shown as arrows 502) is concentrated in the receiver 104 where some of the photons are absorbed by the redox material (points 504). A large part of the remaining incident photons is absorbed by the thermal receiver (illustrated as panel 506). HTF is flowing into panel 506 absorbing heat. Of the photons absorbed by the redox material, some cause photoreduction while others directly heat the redox material. Part of this absorbed heat is radiated and is lost in the environment but part is reabsorbed by the thermal receiver (illustrated by dashed arrows 508). Similarly, part of the radiation losses from the thermal receiver will be reabsorbed by the redox material. Because the redox material will be at a lower temperature than the thermal receiver, the average surface temperature seen by the environment will be less than the surface temperature of the thermal receiver, so the total thermal radiation losses are reduced. Therefore, despite the relatively low efficiency of the photoreduction stage, the receiver will still maintain a high overall efficiency.
    The embodiment of the receiver of Fig. 5 combines a gravity feed curtain of the
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    Redox material with a traditional cavity receiver tube sheet that has HTF cooling. Alternatively, as shown in Fig. 6, the receiving element can be implemented as a rotating cavity receiver 104 in which the walls are cooled by the HTF and deflectors are used to continuously pour the redox material 600 through the cavity space In the configuration of Fig. 6, the redox material particles are contained in one or more of the rotating cavity receivers 602. When the receiver 603 rotates, the particles 600 are agitated and fall through space, absorbing solar radiation . Some of the photons will be absorbed by the reactor walls instead of the particles and will be converted into heat. The reactor walls will be cooled by heat transfer fluid from thermal path 604. The configuration provides minimized radiation and convection heat losses and maximizes the conversion of solar energy into thermal energy and chemical potential.
    A further advantage of the combined thermal-chemical path system is that parallel thermal and chemical systems can be used to store energy at different time scales. Thermal CSP systems, such as molten salt towers, provide relatively low cost short-term thermal storage / day scale). For example, referring to Fig. 2, the heated HTF can be stored directly in a thermal storage system 116 operatively associated with the HTF conduit 108 receiving the flow from the receiver 104 before the heat exchanger 106. Alternatively, the Heated HTF could be used to heat a separate thermal storage medium through heat exchange in the hot thermal storage system. The heat can then be provided to the HTF from the hot thermal storage system 116 during periods of low solar light flux, at night or during periods covered by clouds, for example. Similarly, the cooled HTF can be stored, or used to heat a separate heat storage medium in a cold thermal energy storage system 118. The cold thermal energy storage system 118 could be operatively associated with the HTF conduit 108 to receive flow from heat exchanger 106 to receiver 104 and be used as mentioned above during a period of less solar radiation.
    The exposed parallel chemical system makes long-term (seasonal) storage possible because the redox material is not stored at a high temperature and therefore does not suffer heat losses during storage. For example, as also shown in Fig. 2, the oxidized or reduced redox material can be stored for a long period of time in a storage material storage system
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    oxidized chemical 120 and a reduced chemical storage material storage system 122, respectively. Both chemical storage systems 120 and 122 could be operatively associated with the conduit of chemical energy storage material with the oxidized material storage system that is downstream of the oxidizer 112 and the reduced material storage system that is downstream of receiver 104.
    A representative embodiment of the system 100 uses a phase change material (PCM) of aluminum silicon (AlSi) as HTF or in this example, the heat transfer material. AlSi PCM can reach higher temperatures than steam or nitrate salts, so improved receiver performance is provided. High temperatures are advantageous because the system will work better when most of the system's heat requirements are supplied by a high efficiency thermal receiver.
    As noted above, the system and the exposed methods can be advantageously implemented in a power tower configuration consisting of a field of heliostats focused on a receiver at the top of the tower structure. The AlSi PCM (or other suitable HTF) and the redox material will be transferred from the receiver to the storage tanks or storage systems at the base of the tower. The PCM or other suitable HTF and the redox materials can then be transferred to the energy cycle when electricity generation is needed.
    As noted above, the suitable but not exclusive thermal to electrical conversion system is an open air Brayton energy cycle with a tail or bottoming cycle of steam Rankine. The inlet air will be compressed at high pressure, it will pass through a heat exchanger with AlSi PCM or another HTF to heat it to medium temperatures, then it will be passed through the oxidation chamber to oxidize the redox material and heat the air at very high temperatures. Highly heated air will be used to power a turbine and an electric generator. The exhaust air would be used as a heat source for a typical Rankine tail cycle or “bottoming” of steam through a heat recovery steam generator.
    The exposed embodiments also include power generation methods, for example the power generation method 700 illustrated in Fig. 7. The method of Fig. 7 includes several steps that can be performed in any suitable order and which will typically be performed. in a cyclic way. The method is initiated by providing a solar receiver configured to receive concentrated solar light flux (step 702). Heat transformation fluid of any type is flowed or otherwise conveyed in
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    Communication ends with the solar receiver where the HTF is heated with the concentrated solar luminous flux (step 704). The heated HTF is then made fluid or transported from the solar receiver to a heat exchanger in a heat transfer fluid conduit (Step 706). In the heat exchanger, heat is exchanged between the fluid of
    5 Heated heat transfer and the working fluid of an energy cycle (Step 708).
    In a parallel cycle, the chemical energy storage material (redox) in communication with the solar receiver is irradiated by the concentrated solar luminous flux which results in a reduced amount of chemical energy storage material (Step 710). The reduced chemical energy storage material is then flowed or transported between the solar receiver and an oxidizer in the conduit of chemical energy storage material (Step 712). In the oxidizer, the chemical energy storage material is oxidized producing energy release (Step 714). The heat energy released is exchanged with the working fluid of the energy cycle (Step 716). Energy can be generated with the working fluid heated by the cycle of
    15 energy (Stage 718).
    In summary, the systems and methods described here that are characterized by combined thermal and chemical pathways will potentially achieve a higher total to solar conversion rate than the other known CSP technology. This will result in direct capital cost savings and LCOE because each component can be proportionally
    20 smaller for a given electricity generation speed. A comparison of the exposed state-of-the-art technology and developing CSP technologies can be found in Table 2. All the values in this table without estimates of target values and may not have been commercially tested to date.
    Solar field efficiency Receiver efficiencyStorage efficiencyEnergy cycle efficiencyTotal Efficiency
    Molten salt 50-60%80-90%97%40-45%16-24%
    Air 50-60%70-80%n / a50-55%18-26%
    Saturated Steam 50-60%85-90%n / a30-35%13-19%
    Superheated steam 50-60%80-85%n / a40-45%16-23%
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    Solid Particle 50-60%60-70%97%45-50%13-20%
    Combined thermal and chemical 50-60%70-85%97%55-60%19-30%
    Table 2: Comparison of the proposed technology with the state of the art and developing technologies (estimated target values).
    In addition to the high efficiency of the system at low cost, the combined thermal and chemical path systems and methods offer two significant benefits. First, as described in detail above, the two energy paths offer two energy storage means. The thermal path uses any existing thermal storage system for short-term storage. This is an important advantage that the CSP supports wind and photovoltaic technologies because it allows CSP plants to meet the demand while reducing the LCOE. The described system can also combine cheap short-term storage with long-term storage to adapt to seasonal demand. Once reduced, the redox material can be stored in an inert environment for very long periods of time and used for energy production when necessary. This will also allow the CSP to meet network demands during times when there is very little renewable generation.
    The second additional benefit is the ability to produce syngas. Instead of using air as an oxidant in the energy cycle, the redox material could be burned with carbon dioxide or value to produce carbon monoxide or hydrogen. Together, these two gases constitute syngas that can be used to create liquid fuels. This process could possibly decrease the power generation capacity of the system but it can be a relatively efficient way to produce renewable neutral carbon fuels.
    Various embodiments of the invention could also include permutations of the various elements mentioned in the claims as if each dependent claim was a multiple dependent claim that incorporates the limitations of each of the preceding dependent claims as well as the independent claims. Such permutations are expressly within the scope of this invention.
    Although the invention has been described and shown particularly with reference to a certain number of embodiments, those skilled in the art will understand that changes in the form and details of the various embodiments set forth herein can be made without departing from the field of philosophy and field of the invention and that the various embodiments set forth herein
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    they are not intended to act as limitations to the field of the claims. All references cited here are incorporated in their entirety as a reference.
    权利要求:
    Claims (16)
    [1]

    1. A concentration solar energy system comprising: a solar receiver configured to receive concentrated solar light flux;
    5 a heat transfer fluid in thermal communication with the solar receiver so that the concentrated solar luminous flux heats a quantity of heat transfer fluid;
    a heat exchanger in thermal communication with the heat transfer fluid, the heat exchanger providing heat exchange between the fluid
    10 heat transfer and a working fluid of an energy cycle;
    a heat transfer fluid conduit that provides the flow or transport of heat transfer fluid between the solar receiver and the heat exchanger;
    a chemical energy storage material in communication with the solar receiver so that the concentrated solar luminous flux reduces a quantity of
    15 chemical energy storage material;
    an oxidizer in communication with the chemical energy storage material, the oxidizer providing oxidation of the chemical energy storage material and also providing heat exchange between the chemical energy storage material and the working fluid of the energy cycle; Y
    20 a conduit of chemical energy storage material that provides the flow
    or transport of chemical energy storage material between the solar receiver and the oxidizer.
    [2]
    2. The concentration solar energy system of claim 1, which further
    It comprises an operationally stored thermal energy storage system 25 with the heat transfer fluid conduit.
    [3]
    3. The concentration solar energy system of claim 2, further comprising:
    a thermal energy storage system that receives heat transfer fluid 30 heated from the solar receiver; Y

    a thermal energy storage system that receives the heat transfer fluid cooled from the heat exchanger.
    [4]
    4. The concentration solar energy system of claim 1, further comprising:
    5 a storage system of reduced chemical energy storage material operatively associated with the conduit of chemical energy storage material and receiving the reduced chemical energy storage material from the solar receiver; Y
    a chemical energy storage material storage system
    10 oxidized operatively associated with the conduit of chemical energy storage material and receiving the oxidized chemical energy storage material from the oxidizer.
    [5]
    5. The concentration solar energy system of claim 1, wherein the fluid
    Heat transfer comprises one or more of water, a solid salt; a molten salt, a solid metal; A molten metal and an oil.
    [6]
    6. The concentration solar energy system of claim 1, wherein the heat transfer fluid comprises an aluminum silicon phase change material.
    [7]
    7. The concentration solar energy system of claim 1, further comprising:
    a tower that supports the solar receiver; Y
    a field of heliostats that has heliostats located to focus sunlight on the receiver.
    [8]
    8. The concentration solar energy system of claim 1, wherein the energy cycle comprises:
    a superior Brayton open air energy cycle; Y
    a tail or “bottoming” cycle of steam Rankine.
    [9]
    9. The concentration solar energy system of claim 1, wherein the working fluid 30 of the energy cycle contains an oxidizing agent.

    [10]
    10. A method of power generation comprising the steps of:
    provide a solar receiver configured to receive concentrated solar light flux;
    heating a heat transfer fluid in thermal communication with the solar receiver with the concentrated solar light flow;
    5 flow or transport the heat transfer fluid between the solar receiver and a heat exchanger in the heat transfer fluid conduit;
    exchanging heat between the heated heat transfer fluid and a working fluid of an energy cycle within the heat exchanger;
    reduce a chemical energy storage material in communication with the
    10 solar receiver radiating the chemical energy storage material with concentrated solar flux;
    flow or transport chemical energy storage material between the solar receiver and an oxidizer in a conduit of chemical energy storage material;
    15 oxidizing the reduced chemical energy storage material in an oxidizer, providing the oxidizer in addition to heat exchange between the chemical energy storage material and the working fluid of the energy cycle; Y
    generate energy with the working fluid of the energy cycle.
    [11]
    11. The method of claim 10 further comprising storing the fluid of
    Heat transfer in a thermal energy storage system operatively associated with the heat transfer fluid conduit.
    [12]
    12. The method of claim 10 further comprising:
    storing the heated heat transfer fluid received from the solar receiver in a hot thermal energy storage system; Y
    25
    storing the cooled heat transfer fluid received from the heat exchanger in a cold thermal energy storage system.
    [13]
    13. The method of claim 10, further comprising:

    storing the reduced chemical energy storage material from the receiver in a storage system of reduced chemical energy storage material; Y
    storing the oxidized chemical energy storage material received from the oxidizer in a storage system of oxidized chemical energy storage material.
    [14]
    14. The method of claim 10, wherein the heat transfer fluid comprises one or more of the following materials: water, a solid salt; a molten salt, a solid metal; A molten metal and an oil.
    The method of claim 10, wherein the heat transfer fluid comprises an aluminum silicon phase change material.
    [16]
    16. The method of claim 10, further comprising the steps of:
    provide a tower to support the solar receiver; Y
    provide a heliostat field that has heliostats located to focus on the receiver.
    [17]
    17. The method of claim 10, further comprising generating energy with an energy cycle comprising:
    a superior Brayton open air energy cycle; Y
    a tail or “bottoming” cycle of steam Rankine.
    The method of claim 10, which comprises oxidizing the reduced chemical energy storage material in the oxidizer with an oxidizing agent in the working fluid of the energy cycle.
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    同族专利:
    公开号 | 公开日
    ES2544002B1|2016-10-06|
    WO2014062464A1|2014-04-24|
    CL2015000934A1|2016-03-28|
    ZA201501984B|2016-09-28|
    EP2909546A1|2015-08-26|
    EP2909546A4|2016-11-16|
    ES2544002R1|2015-10-23|
    CN104884874A|2015-09-02|
    US20150253039A1|2015-09-10|
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    PCT/US2013/064226|WO2014062464A1|2012-10-16|2013-10-10|Coupled chemical-thermal solar power system and method|
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