22.033 Process Heat - MIT OpenCourseWare22.033 Process Heat . Lauren Ayers Sarah Laderman Aditi...
Transcript of 22.033 Process Heat - MIT OpenCourseWare22.033 Process Heat . Lauren Ayers Sarah Laderman Aditi...
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22.033 Process Heat
Lauren Ayers Sarah Laderman
Aditi Verma Anonymous student
Presentation 1 October 5, 2011
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Outline
System Layout Heat Exchanger Designs Heat Storage Options Heat Transport Future Work
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Core Hydrogen Plant
Biofuel Plant
Heat Storage
Burn waste product to raise temperature for hydrogen plant.
650 C
240 C
760 C
Provide reactor with extra heat.
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System Layout
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Types of Heat
Exchangers Investigated
Standard shell and tube Printed circuit heat exchangers Helical shell and tube Thermosyphons
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Criteria for Selecting a Heat Exchanger
Operating temperature and pressure
High heat transfer performance
Effectiveness Fouling
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Courtesy of MERUS GmbH. Used with permission.
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Multiple Pass Shell and Tube
with Continuous Helical Baffles
Max. operating pressure: ~70 MPa Max. operating temperature: dependent on materials Induced turbulence + high shear stress = 6 less fouling
Courtesy of Elsevier, Inc., http://www.sciencedirect.com. Used with permission.
Photo from Q. Wang
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Printed Circuit Heat Exchangers (PCHEs)
• All-metal HXs made of diffusion bonded plates
• Long design life (up to 60 years)
• Compact, mass/duty ratio of 0.2 tons/MW
• High operating temperatures (up to
900 C) and pressure (60 MPa)
• High surface area density (2500 m2/m3)
• Hybrid fin and plate type PCHE, H2X, suitable for coupling gaseousand liquid working fluids
Current operatin7g experience of HeatricTM PCHEs (Gezelius, K., “Design of Compact Intermediate Heat Exchangers for Gas Cooled Fast Reactors,” Bachelors’ & Masters’ Thesis, MIT, June 2004.)
Cross sectional view of Diffusion bonding of
the semi-circular PCHE plates (HeatricTM)
passages (HeatricTM ) © Heatric. All rights reserved. This content is excluded from our CreativeCommons license. For more information, see http://ocw.mit.edu/fairuse.
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Heat ExchangerRequirements
Operating Temperatures HX connected to CO2 loop: 650-900 ºC Hydrogen plant: 700-900 ºC Biofuels plant: 240-300 ºC Heat storage: 300-500 ºC
Standardized heat exchanger design will reduce plant complexity and operating and maintenance costs
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Heat Exchanger Configurations
Two HX instead of single high temperature HX to increase design life
Connect process heat system in parallel or series
Remove heat from the secondary cycle before the power conversion system Need to decide with core
HX decisions will depend on flow rates and temperatures provided by core and needed by biofuels and hydrogen
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Benefits of Heat Storage
Plateau energy fluctuations during daily cycles Providing lower temperature to biofuels without
wasting heat
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Heat Storage Options
Latent Heat vs. Sensible Heat Latent – storing energy in chemical bonds Sensible – using change of temperature of material
to store heat (specific heat capacity) Decided on latent heat
Can store higher energy density Provides heat at constant operating temperature Uses phase change materials
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Phase Change Material Decision Tree
Courtesy of Elsevier, Inc., http://www.sciencedirect.com. Used with permission.
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PCM Selection
Must have melting point in desired operating temperature range
Ideal Characteristics: High latent heat of fusion per unit mass High density High specific heat High thermal conductivity Chemically stable Non-corrosive to the containment material
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Liquid-Solid PCMs
Paraffins & Salt Hydrates Operating temperature too low
Salts Large range of operating temperatures Issues: corrosion & low thermal conductivity
Metals Desirable thermodynamic properties Issues: freezing can cause stresses to containment,
temperature range is limited 14
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Salt and Metal PCMs
Courtesy of Elsevier, Inc., http://www.sciencedirect.com. Used with permission.
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Looking Ahead
Containment structure cannot be designed until a PCM is chosen Material compatibility concerns
Volume of material is dependent on: Thermodynamic properties of the material Amount of energy that needs to be stored
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Heat Transport Methods
Thermosyphons Uses gravity and phase changes to move heat long
distances with minimal heat loss Highly dependent on location of plant
Heat pipes Can use capillary action and if in correct orientation,
gravity can assist Can also use centripetal, electrokinetic, magnetic,
and osmotic forces • Not as practical for long distances and not as well
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Heat Transport Decisions
Method of condensate transport determined by distance between plants Will model hydrogen plant explosions and biofuel
plant fires to determine safe distances Material and working fluid determined by HX
choice and temperature environment
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Future Work
Finalize heat exchanger and heat storage designs
Model system once initial outputs/inputs are available Matlab, EES, RELAP
Heat sink as a safety measure at hydrogen plant
Determine plant distances as more data becomes available
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Questions?
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22.033 / 22.33 Nuclear Systems Design ProjectFall 2011
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