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E2C 2013 October 27-30, 2013 Budapest, Hungary Experimental Study of Phase Change Materials for Thermal Storage in the Temperature Range of 300-400 o C R. Adinberg, D. Zvegilsky, M. Epstein
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Discussion Topics Thermal Energy Storage (TES) for Concentrating Solar Power (CSP) plants Selection of Phase Change Materials (PCM) for Solar TES Thermal analysis of PCM and Main results Reflux Heat Transfer Storage (RHTS) experimental system TES prototype design Conclusions 2
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Q1Q1 Power Block Q L CSP System Q 0 ~ Q3Q3 Q 2 QFQF Electricity Grid FOSSIL FUEL Power Control System: Q 0 …....Q L (HTF flow), E S QRQR SOLAR POWER Solar-Fossil Hybrid Power System Thermal Storage Operation Buffering during transient weather conditions Dispatchability / time-shifting into peak/night hours Achieve full load operation of the steam turbine cycle Increase of annual capacity factor 20 to 40/50% 3
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State of the art Thermal Storage Technology 2-tank Molten Salt System Tank Size 14 m height 38 m diameter Amount28,500 tons Capacity1010 MWh Molten Salt (K-Na)NO 3 Temperature 250-400 o C Andasol, Spain Solar Power Plant 50 MWe Temperature 300-400 o C (Parabolic Trough CSP) MethodEffectPhaseMaterials Sensible Heat CP ΔTCP ΔT Liquid Thermal oil Molten salt Pressured water Latent Heat Δ H T @ T melt Solid/LiquidPCM: Molten Salts Metal Alloys Thermo- Chemical Δ H R (Endo-Exo thermal reaction) Solid Gas CaO/H 2 O NH 3 → N 2 + H 2 4
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Reflux Heat Transfer Storage -RHTS Design Specifics Isothermal Process:T steam PCM m.p. Overall Thermal Conductivity:PCM-to-Steam Thermosyphon Energy density by volume: 2-5 times of 2-tank MS system Pressure-tight tank:5-10 bar Challenge : PCM-HTF Compatibility 1PCM Selected Materials: Zn Alloys, Molten Salts 2 HTF Diphyl Diphenyl Oxide + Biphenyl (Dowtherm A; Therminol VP- 1) 3 Temp. < 400 o C Key Features PCM-HTF Direct Contact HTF Vapor Natural Convection & Liquid Reflux Heat Exchanger External to PCM To Steam Generator PCM HTF Boiling 5
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PCM-HTF Thermo-Chemically Stable Systems HTFPCMMelting Temp. Density (solid) Latent Heat Max Test Temperature Diphyl Zn70Sn30 370 o C 7. g/ cm 3 107 J/g 400 o C Zn95Al53847.101400 KNO 3 3342.110360 (K/NA/Li) 2 CO 3 392/72.5280400 Thermal Analysis Applied TGA/DTADSCFTIR Q600 TA InstrumentsDSC 4000 PerkinElmerTensor 27 Bruker Optics Calorimetric results for the 3C-Diphyl chemical system including a few sequential heating-cooling cycles between 350 to 420 o C Time 6
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RHTS Lab-scale Experimental System Thermocouples K, T Sample Pan Sample Vessel Stirrer Water-filled Condenser (4 L) Insulation HTF: Diphyl 0.25 L 3C-PCM 0.9 kg Metering Valve Pressure Sensor HTF Flow Electric Furnace 1 2 Cross section of the sample pan containing 3C PCM after the long-term test Multiple Cycles 7
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RHTS Prototype Design Calculated parameters of a thermal storage tank for a 50MWe solar power plant PCM KNO 3 3C Amount PCM, ton 17,000 14,000 Amount HTF, ton ca. 2,000ca. 1,000 Height, m 20 Diameter, m 3224 Thermal capacity, MW th h 5001000 Thermal Storage for 7 operational hours (solar capacity factor 0.4) Number of tanks21 8
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Experimental Study of Phase Change Materials for Thermal Storage in the Temperature Range of 300-400oC SUMMARY RHTS is a synergistic process that integrates the PCM solid–liquid and HTF liquid–vapor reversible phase change effects for respectively storing and transferring heat in the thermal storage system. The experimental results of this work show that the (K/Na/Li) 2 CO3 - Diphyl storage medium is thermally and chemically stable and suitable for RHTS up to 400 o C. The experimental system has been demonstrated quite effective in heat transfer for improving the performance of thermal storage systems. A feasibility study is currently being done on integration of 3C-Diphyl RHTS module into a 50 MW solar thermal electric power plant.
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