The Role of Innovation in Industry Product Deployment: Developing Thermal Energy Storage for Concentrated Solar Power
Abstract
:1. Introduction
2. Innovation in Concentrating Solar Power (CSP)
- A case based on the acquisition of new competences in the field of solar energy but that integrated and enhanced the existing competences in conventional power plant engineering.
- A product innovation to offer renewable solar plants with energy dispatchability. A process innovation for excellence in manufacturing and operation processes.
- A system innovation (solar plant parabolic through collector and tower plants) but also a component innovation. In a solar plant there are many critical components designed, “ad-hoc” that constitute in themselves new products/equipment for the value chain. Solar receivers, thermal energy storage systems, solar trackers, specific measurement equipment, etc.
- A disruptive innovation (PS-10 the first commercial solar thermal plant in the world) but also an incremental innovation for cost reduction and efficiency improvement: parabolic trough solar thermal plants with large opening manifolds, tower plants with superheated steam and molten salts.
- Technological risks: materials in extreme conditions of temperature and pressure, corrosion associated with heat transfer fluids, desert environments and subject to wind loads, physical limits on optical properties, thermodynamic limits.
- Non-technological component: geographies and first to market.
3. Case Study: Thermal Energy Storage (TES) for CSP at Abengoa
- The first stage was the creation of the R&D network in 2007, funded with the Spanish CENIT project ConSOLida 2008–1005, where the biggest challenges were the confidentiality needed between the company and the R&D institutions, the training activity needed, the need to achieve results following a schedule fixed by market demands, and last but not least, the need to develop deep relationships of trust.
- The second stage was the testing at pilot plant at the University of Lleida, where a 0.3 MWht pilot plant was built to carry out a deep characterisation of the molten salt properties [38]. At the same time research was carried out at the University of Barcelona, where thermomechanical testing under operating conditions of container materials such as A516Gr70 were developed [39], and at Inasmet, where corrosion tests were performed [40].
- The TES pilot plant was integrated in a parabolic trough plant that uses thermal oil as HTF. The heat transfer fluid cedes heat to the salt through a heat exchanger. The design capacity of the plant was 2.1 MWth with four hours of thermal storage, representing a total thermal capacity of 8.4 MWth. The salts used in this system are the so-called solar salts, comprising a mix of NaNO3 (sodium nitrate) and KNO3 (potassium nitrate).
- The next step was the development of high-level collaboration with a framework of collaboration agreement of the newly developed TES system (Interconecta Thesto ITC-20111050) to develop a new TES concept for direct steam generation, based on solid particle and phase change materials (PCM) solutions. The idea was to explore alternatives to the molten salt sensible heat TES with more technologically complex solutions, leveraging the baseline developments.
- Then, advanced development of the technology was achieved with several frameworks of collaboration in thermochemical storage with European funding under the H2020 funding scheme.
- To finally achieve leadership in the sector with 6000 MWht installed in a thermal storage system, strong collaboration agreements with several R&D partners worldwide, and the development of hybridization new concepts.
4. The Dichotomy: Private versus Public Funding
5. Conclusions
Author Contributions
Funding
Acknowledgments
Conflicts of Interest
References
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Strategy | Horizon 1 (2007) | Horizon 2 (2012) | Horizon 3 (2020) |
---|---|---|---|
Business and products | Saturated and superheated towers: PS10, PS20, and PS50 | - Parabolic trough collector - Molten salt tower and superheater tower | Dispatchability: effective response to the “electricity peak demand” |
Objectives: master technologies | - Parabolic trough technology - Superheated steam towers - Saturated steam towers - Heliostats - Molten salts thermal energy storage - Solar field calculation codes | - Molten salt tower - Advanced cycles - Heliostat of the future - Collector of the future | - Design receivers at higher temperature - Seek breakthrough innovations - Hybrid solutions |
Main actions | - Support PS10 and PS20 - New funding for research and development (R&D) facilities - Manage IP portfolio - Manage costs and grants follow up | - Operation of molten salt pilot plant - Engineering of a commercial molten salt tower plant - Operation of air receiver solar plant Solugas - Potent maps and IP gap identification | - Assess feasibility of new concepts (high temperature, light management) - New fluids and materials - Technical surveillance - File patents in key technologies |
Type of CSP | Name | Power | Solar Collectors | Heat Transfer Fluid | Maximum Working Temperature | Operation | Hours of Operation | Used in Commercial Plant | Reference |
---|---|---|---|---|---|---|---|---|---|
Trough technology | Repow | 2.1 MWt | 1 loop of 600 m (4 collector) | Oil | 400 °C | 2007–2012 | 30,000 h in 2014 | PTC components used in Solnova 1 (Spain) Xina Solar One | [26] |
2 larger aperture collectors of 300 m | Oil | 400 °C | 2014–2016 | 500 h | DEWA Hybrid solar-gas plant WAS (Waad Al-Shamal) | [27] [28] | |||
Indirect molten salt storage | Molten salts dual tank TES | 9 MWht | --- | Oil/MS | 400 °C | 2009–2012 | >32,000 | Solana Power Plant | [21,22,23,24] |
Superheater steam receiver | Eureka | 5 MWt | 60 heliostats of 120 m2 | Solar salt | 550 °C | 2009–2011 | >2000 | Khi Solar One | [29] |
Direct steam generation | Eureka-DSG | 8 MWt | 3 loops saturated; 2 loops superheated | Water | 550 °C | 2009–2011 | 2000 | Process heat | [30] |
Molten salt receiver | CRS Sales | 5 MWt | 85 heliostats of 120 m2 | Solar salt | 565 °C | 2012–2015 | 3600 | Cerro Dominador | [31] |
New HTF | Avanza2 | --- | --- | Ternary carbonate | 700 °C | 2014–2015 | 1000 | --- | [32] |
Gas receiver (tubular receiver and volumetric pressurized air receiver) | Solugas | 3 MWt | 69 heliostats of 120 m2 | Air | 800 | 2012–2014 | 1200 | --- | [33] |
Cersol | 105 kWht | 1000 | 2014 | 100 | --- | --- | |||
Soltrec | 3 MWt | 1000 | 2015 | 200 | --- | [34] |
Receiver Panel Conditions | Flow Conditions | ||
---|---|---|---|
Paths | 2 | HTF | Superheated steam |
Panels | 6 | Inlet temperature | 300 °C |
Passes per panel | 4 | Outlet temperature | 530 °C |
Tubes per pass | 7 | Inlet pressure | 85 bar |
– | – | Mass flow | 3.4 kg/s |
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Prieto, C.; Fereres, S.; Cabeza, L.F. The Role of Innovation in Industry Product Deployment: Developing Thermal Energy Storage for Concentrated Solar Power. Energies 2020, 13, 2943. https://doi.org/10.3390/en13112943
Prieto C, Fereres S, Cabeza LF. The Role of Innovation in Industry Product Deployment: Developing Thermal Energy Storage for Concentrated Solar Power. Energies. 2020; 13(11):2943. https://doi.org/10.3390/en13112943
Chicago/Turabian StylePrieto, Cristina, Sonia Fereres, and Luisa F. Cabeza. 2020. "The Role of Innovation in Industry Product Deployment: Developing Thermal Energy Storage for Concentrated Solar Power" Energies 13, no. 11: 2943. https://doi.org/10.3390/en13112943
APA StylePrieto, C., Fereres, S., & Cabeza, L. F. (2020). The Role of Innovation in Industry Product Deployment: Developing Thermal Energy Storage for Concentrated Solar Power. Energies, 13(11), 2943. https://doi.org/10.3390/en13112943