Concentrated Solar Power on Demand

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Concentrated Solar Power on Demand CSPonD Liquid Salts as Direct Receiver and Storage Media Charles Forsberg Department of Nuclear Science and Engineering (NSE) Massachusetts Institute of Technology 77 Massachusetts Ave; Bld. 42-207a; Cambridge, MA 02139 Tel: (617) 324-4010; Email: cforsber@mit.edu January 2015

CSPonD Summary 2 Solar thermal power system Direct conversion of light from heliostats to heat by absorption in liquid salt bath Liquid salt provides heat storage 24 hour power production Cold Salt from HX Non-Imaging Refractor Lid Lid Heat Extraction Light from Heliostats Absorbed As Travel Through Molten Salt Hot Salt to HX

3 Outline The Electricity Market: Defining Requirements CSPonD Description Experimental Program Status Backup Information

4 The Electricity Market Starting Point for Design Goals

Demand (10 4 MW(e)) Electricity Demand Varies With Time No Combination of Nuclear and Renewables Matches Electricity Demand 5 New England (Boston Area) Electricity Demand Time (hours since beginning of year)

In a Free Market Electricity Prices Vary 6 Low and Negative Prices High- Price Electricity 2012 California Electricity Prices

Generation (MW) Adding Solar and Wind Changes Electricity Prices & Price Structure Unstable Electrical Grid 7 Excess Electricity with Price Collapse 35,000 30,000 25,000 20,000 15,000 10,000 5,000 0 PV Gas Turbine Pumped Storage Hydro Combined Cycle Imports Coal Nuclear Wind Geo Exports -5,000 Base 2% 6% 10% (no PV) PV Penetration and Hour California Daily Spring Electricity Demand and Production with Different Levels of Annual Photovoltaic Electricity Generation

Notes on California Solar Production 8 Far left figure shows mix of electricity generating units supplying power on a spring day in California. The figures to the right shows the impact on grid of adding PV capacity assuming it is dispatched first low operating cost. Percent PV for each case is the average yearly fraction of the electricity provided by PV. The % of power from PV is much higher in late June in the middle of the day and is zero at night. Initially PV helps the grid because PV input roughly matches peak load. Problems first show up on spring days as shown herein when significant PV and low electricity load. With 6% PV, wild swings in power supply during spring with major problems for the grid. By 10% PV on low-electricity-demand days PV provides most of the power in the middle of many spring days. In a free market PV or producers with zero production costs will accept any price above zero. As PV grows, revenue to PV begins to collapse in the middle of the day. Collapsing revenue limits PV new build. Same happens if lots of wind is built. Large-scale PV or wind also damages base-load electricity market while increasing market for peak power when no sun or wind. In the U.S. that variable demand is getting filled with gas turbines with increases in greenhouse gas emissions. The revenue problem with renewables is similar to selling tomatoes in August when all the home-grown tomatoes turn red and the price collapses to near zero The other part of the story is the need for backup power when low wind or solar. For example, in Texas only 8% of the wind capacity can be assigned as dispatchable. That implies in Texas for every 1000 MW of wind, need 920 MW of backup capacity for when the wind does not blow almost a full backup of wind. In the Midwest grid, only 13.3% of the wind capacity can be assigned as dispatchable. Consequently, with today s technologies large scale renewables implies large-scale fossil fuel usage

Low-Carbon Electricity Free Market Implies More Hours of Low / High Price Electricity Large Sun and Wind Output Collapses Revenue Distribution of electricity prices, by duration, at Houston, Texas hub of ERCOT, 2012 No Sun and No Wind Current Prices The Future Market? Future Solar Economics Poor If Sell When Sun is Out 9

MIT Concentrated Solar Power on Demand (CSPonD) 10 Description Power Plus Storage Joint Program Between MIT Mechanical and Nuclear Science and Engineering Departments Alex Slocum leads the CSPonD Project. C. Forsberg leads the Fluoride-salt-cooled High-temperature Reactor (FHR) project see appendix. Both projects both based on properties of high temperature salts with many common challenges. A. Slocum, J. Buongiorno, C. W. Forsberg, T. McKrell, A. Mitsos, J. Nave, D. Codd, A. Ghobeity, C. J. Noone, S. Passerini, F. Rojas, Concentrated Solar Power on Demand, Journal Solar Energy, 85, 1519-1529, 2011

Existing Solar Power Technology 11 Mirrors reflect sunlight to boiler Boiler tubes on top of tall tower absorb light Heat water and convert to steam Steam turbine produces electricity PS-10, 11 MWe peak, image courtesy of N. Hanumara

The Challenge is Cost 12 Low efficiency system In theory high efficiency In practice Lower steam temperatures to avoid boiler-tube thermal fatigue from variable light High heat loses from exposed boiler tubes Marginal economics Need efficient light-to-electricity system Peak power not match peak demand with peak electricity prices PS-10, Spain, 11MWe peak, image courtesy of N. Hanumara

CSPonD Description Figure Next Page 13 Mirrors shine sunlight to receiver Receiver is a high-temperature liquid salt bath inside insulated structure with open window for focused light Light volumetrically absorbed through several meters of liquid salt Structure minimizes heat losses by receiver Enables salt temperatures to 900 C Small window minimizes heat losses but very high power density of sunlight through open window Power density would destroy conventional boiler-tube collector Light absorbed volumetrically in several meters in salt Requires high-temperature (semi-transparent) salt

Two Component System 14 Non-Imaging Refractor Lid Lid Heat Extraction Hot Salt to HX Light Reflected From Hillside Heliostats to CSPonD System Flat Land Options Exist (Not to scale) Cold Salt from HX Light Collected By Absorption in Liquid Salt Inside Insulated Building With Open Window

CSPonD Heliostats Shine Light Through Pinhole into Liquid-Salt Collector 15 Efficient light-to-heat collection Concentrate light Focus light through open window in insulated structure Minimize heat losses Challenge Light energy per unit area very high Will vaporize solid collectors Cold Salt from HX Non-Imaging Refractor Lid Lid Heat Extraction Hot Salt to HX Light Collected As Travel Through Molten Salt Similar to Sunlight Absorbed by the Ocean

Light Focused On Transparent Salt 16 Light volumetrically absorbed through several meters of salt Molten salt experience Metal heat treating baths (right bottom) Molten salt nuclear reactor Advantages No light-flux limit No thermal fatigue High efficiency Energy storage Like Ocean Absorption of Sunlight Molten Chloride Salt Metallic Heat Treatment Bath (1100 C) 16

Two Classes Of Molten Salts 17 Appearance of molten NaCl-KCl salt at 850 C Near-term: Nitrates Used in some concentrated thermal solar systems Off the shelf Temperature limit of ~550 C (Decompose salt) Long-term: Chlorides and Carbonates Thermodynamically stable Peak temperatures > 1000 C

fraction of incident energy at aperture System Design Enables Efficient Light Collection and High Temperatures Ideal CSPonD Receiver Performance: Overall Capture Efficiency 18 1.0 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0.0 NREL Solar I: steam 500C NREL Solar II: salt 565C Peak & average values Nitrate Salt: 550C lid temp 240C Aperture to Illuminated Pond Area ratio 0 500 1000 1500 2000 2500 3000 3500 NREL (2003) Peak Concentration (kw/m^2, 'suns') Chloride Salt: 950C lid temp 660C Compares favorably with measured values for CSP Power Tower Systems System output (MWe): 4 Nominal pond size diameter (m): 25.0 depth (m): 5.0 Avg beam down angle (deg): 21.4 Nitrate Salt, Lid peak temp (C): 550/240 Chloride, Lid peak temp (C): 18/29 950/660

Salt Selection Salts Used in Commercial Metal Heat Treating Operations Initial candidates (Other options to be examined): Binary nitrate mixture, KNO 3 -NaNO 3, (eutectic 40-60 wt%, melting point 222 C) Commercial in closed solar systems Family of options with variable compositions Ternary carbonate salt, Li 2 CO 3 -Na 2 CO 3 -K 2 CO 3 cartecsal (eutectic 32-33-35 wt%, melting point 397 C) Used for heat treating metals No experience in power cycles Binary chloride salt, NaCl-KCl (eutectic 50-50 wt%, melting point 657 C) long term option 19

Properties At Operating Conditions 20 NaCl-KCl at 800 C Li 2 CO 3 -Na 2 CO 3 -K 2 CO 3 at 800 C KNO 3 -NaNO 2 -NaNO 3 at 350 C Density kg/m 3 1520 1902 1850 Viscosity mpa s Thermal conductivity W/m-K 1.2 4.3 2.360 0.45 0.822 0.61 Specific heat J/kg-K 1090 1560 1560 Power Cycle Temp. C ~800 ~700 ~500

CSPonD Integral Heat Storage Salt tank has insulated separator plate Plate functions Separates hot and cold salt Bottom light absorber creating mixing currents in hot salt Storage role If excess heat input, plate sinks to provide cold salt to heat to become hot salt and storage If power demand high, plate raised with cold salt return from power cycle stored under plate 21 Daytime Divider plate (moves down) Nighttime Divider plate (moves up)

Alternative CSPonD Heat Storage 22 Separate collector and heat storage tank Liquid storage with solid fill (Several options) May reduce required salt inventory Centralized storage from several receivers with common power plant lower power-cycle costs No definitive studies New hot salt storage options (Backup materials) Heat In/Out Cold Salt Out/In

Multiple Power Cycle Options 23 Salt Temperature: 500 C, 700 C, and 700+ C Steam (500 to 700 C) Off-the-shelf technology Expensive Air Brayton (700 C and up) Existing technology Small or limited cooling water requirements Requires 700 C salt temperatures Supercritical carbon dioxide (600 to 700 C) High efficiency Very compact and potentially low-capital cost Advanced technology: Not fully developed

Options for Power and Heat 24 CSPonD has cooling systems in lid Prevent overheating and equipment damage Cooler temperatures than salt to provide condensing surface for salt vapors Lowers salt losses at very high temperature operations Creates liquid mirror reflective surface to minimize heat loses High temperature heat not as hot as salt so options for use Integrate into power cycle Use for other uses such as water desalination

CSPonD Experimental Program 25

Salt Optical Characterization Experimental Molten Salt Measurements 26 Solar Irradiance Attenuation of NaCl- KCl (50-50wt%) salt at 850 C (l) Variable optical path length transmission apparatus (r) Appearance of molten NaCl-KCl salt at 850 C Experimental Range Stefano Passerini, Dr. Tom McKrell, Prof. Jacopo Buongiorno, MIT

Calculated Optical Power (kw/m 2 ) Spectral Intensity (arbitrary units) 60-Sun Solar Simulator 27 MIT CSP Simulator Terrestrial solar spectrum Commercial Xenon Solar Simulator 80 300 400 500 600 700 800 900 1000 wavelength (nm) 70 ε n = α solar = 0.11 60 ε n = 0.05 α solar = 0.11 50 40 ε n = 0.06 α solar = 0.14 30 MIT CSP Solar Simulator 10.5 kw e 20 10 0 0 2 4 6 8 10 X = radial offset from aperture center (cm) x

Height (x/l) Volumetric Light Absorption Experiments 28 1 0.9 0.8 0.7 0.6 0.5 Increasing time Increasing time t = 0 2.8 h 8.3 h 0.4 0 h salt 0.3 0 h tank 2.8 h salt 0.2 2.8 h tank 0.1 8.3 h salt 8.3 h tank 0 200 220 240 260 280 300 320 340 360 Temperature ( C) Temperature distribution of NaNO 3 - KNO 3 (60-40wt%) heated optically

Virtual Two-Tank System Testing 29 Salt tank @ 300 C with nitrate salt Ceramic (high temp) insulation Fiberglass insulation Inside Solar Simulator

30 CSPonD Status Joint Program Between MIT and Masdar Institute, Abu Dhabi, UAE

Joint Program Initiated 2014 31 Design and deploy a pilot CSPonD experimental system in Abu Dhabi Field proof of principle using Masdar solar test facilities within 3 years Includes new Chinese partners

CSPonD Project Masdar Test Facility CSPonD Test Module To Be Installed Under Tower

CSPonD Conclusions 33 Analysis and experiments indicate better economics than existing concentrated solar thermal systems Higher efficiency Electricity when needed Significant uncertainties Pilot plant to address many uncertainties Large incentives for higher-temperature salt than nitrate but limited experimental data Experimental program between MIT and Masdar Institute to deploy small pilot plant at test facility in Abu Dhabi Recent discoveries indicate route to major improvements

Questions 34

END 35

Biography: Charles Forsberg 36 Dr. Charles Forsberg is the principle investigator and director of the Fluoride-salt-cooled High-Temperature Reactor Project. He is a coinventor and principle investigator for the Concentrated Solar Energy on Demand (CSPonD) system. Before joining MIT, he was a Corporate Fellow at Oak Ridge National Laboratory. He is a Fellow of the American Nuclear Society, a Fellow of the American Association for the Advancement of Science, and recipient of the 2005 Robert E. Wilson Award from the American Institute of Chemical Engineers for outstanding chemical engineering contributions to nuclear energy, including his work in hydrogen production and nuclear-renewable energy futures. He received the American Nuclear Society special award for innovative nuclear reactor design on salt-cooled reactors and the 2014 Seaborg Award from the ANS. Dr. Forsberg earned his bachelor's degree in chemical engineering from the University of Minnesota and his doctorate in Nuclear Engineering from MIT. He has been awarded 11 patents and has published over 200 papers.

Solar Cost Is Generation Plus Storage To Meet Electricity Demand 37 Photovoltaic Costs Include Backup Storage Power output from a 4.6 MW PV system in Springerville, Arizona at 10 second time resolution for one day are shown Apt, J. (n.d.). The Spectrum of Power from Utility-Scale Wind Farms and Solar Photovoltaic Arrays. Carnegie Mellon Electricity Industry Center Working Paper CEIC-08-0

Concentrated Solar Power on Demand (CSPonD) 38 Hillside heliostat field Receiver Molten salt loop Separator plate Steam generator Conventional CSP Power Tower Hillside beam-down CSPonD System

39 39 High-Temperature Salt Power Programs at MIT

MIT Has Two High-Temperature-Salt Electricity-Generation Projects Shared Liquid-Salt Technology Base: Heat Transfer, Heat Storage, and Power Cycles 40 Fluoride-Salt-Cooled High- Temperature Reactor (FHR) Concentrated Solar Power on Demand (CSPonD)

41 The Base-Load FHR Produces Variable Electricity to Match Market Needs FIRES for Peak Electricity Stored Heat Combustible Fuels for Peak Electricity Gas-Turbine (NACC) Constant High- Temperature Heat (600 to 700 C) Reactor (FHR) Electricity Prices Horizontal Axis

42 NACC Power System Base-load and Peak Electricity (Auxiliary Natural Gas or Stored Heat)

Notes on NACC (Long-term CSPond Option) 43 With base-load operation, air is compressed, heated using heat from the FHR, sent through a turbine to produce electricity, is reheated using heat from the FHR to the same temperature (670C), sent through a second turbine to produce electricity and exhausted at low pressure to a heat recovery steam generator (HRSG) In the HRSG the warm air is used to produce steam to produce added electricity or steam for industrial sale. The base-load operations are very similar to a natural-gas fired combined cycle plant. The efficiency is ~42%. The cooling water requirements are about 40% of a conventional light water reactor. That is partly because of the higher efficiency and partly because some of the heat rejection is via warm air similar to stand alone combined cycle natural gas plants. For peak power, after second reheat using nuclear heat, natural gas is injected into the hot air stream to raise compressed air temperatures. This increases electricity production from the second turbine and the HRSG. The system may also contain a Firebrick Resistance-Heated Energy Storage (FIRES) System. The firebrick is heated with electricity when the price of electricity is below that of natural gas. At times of high prices, compressed air after the second reheat is sent through FIRES to increase its temperature. This results in higher power output from the second turbine and the HRSG Peak heat to electricity efficiency is above 66% because it s a topping cycle above the lower-temperature 700C nuclear heat

FHR and CSPonD Share Liquid-Salt Heat-Transfer / Power-Cycle Technologies 44 Materials, Pumps, Power Cycles, Valves, Etc. Nuclear New reactor concept Forsberg, Peterson, and Pickard FHR (Joint MIT, Berkeley, Wisconsin program) High-temperature heat transfer loop between hightemperature reactors and power systems China to build first FHR (10 MWt) by 2020 Solar Drive to more efficient systems CSPonD Near-term nitrate salts to 550 C Next generation chloride or carbonate salts to 700 C Nuclear systems only looking at 700 C systems