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Univer sity of Louisiana CLECO Power LLC Alternative Energy Research Center Solar Thermal Power Plant Jonathan R. Raush, M.S., P.E.
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Solar Thermal Powerpoint 7-27-2011

Oct 13, 2015

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    University of Louisiana

    CLECO Power LLC

    Alternative Energy Research Center

    Solar Thermal Power

    PlantJonathan R. Raush, M.S., P.E.

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    Overview

    Solar Energy Background Solar Radiation

    Available Resources

    U.S. Energy Outlook

    Solar Thermal Technology Concentrating Solar Power (CSP)

    Parabolic Trough CSP

    Steam Rankine Cycle

    Organic Rankine Cycle

    UL/CLECO Installation Background Information/ARRA

    Technology

    Goals

    Cycle Analysis

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    Solar Energy

    Sun Characteristics

    The sun is the most reliable and abundant source of energy.

    9900 F at surface

    36,000,000 F at center

    Solar Constant

    1353 W/m2(+/- 3%) .000000045% of energy emmitted

    428 Btu/ft2hr

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    Solar Energy

    Earth and atmosphere continuously receive 1.7x1014kW of

    radiation from the sun

    A world population of 10 billion with a total power need of

    10 kW per person would only require 1011

    kW of energy Solar energy intercepted by the planet is 5000 times

    greater than the sum of all other inputs (terrestrial nuclear,

    geothermal, gravitational, and lunar gravitational)

    Goswami, et. Al. Solar Radiation is responsible for Solar Thermal/ Wind/

    Biomass/ Photovoltaic/ Hydro Energy

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    Solar Energy

    Of total radiation received, 30% reflected tospace, 47% converted to low-temperature heatand reradiated to space, 23% powers the

    evaporation/precipitation cycle of the biospherewith

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    Solar Energy

    1.5x1017kWhr per year falls on land (6000 times totalenergy usage of U.S. in 2000)

    Utilizing only 1% of the earth's deserts to produce solarelectric energy would provide more electricity than is

    currently being produced on the entire planet by fossilfuels

    Energy reaching the earth is made up of two parts Direct beam radiation

    Diffuse energy in the sky

    Most manmade solar collectors can convert only directenergy efficiently

    Amount of direct energy depends on the cloudinessand position of the sun

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    Solar Energy

    In Summary:

    Fraction of radiation reaches ground in form

    of Direct Normal Radiation

    Can be as high as 1000 W/m2

    9 kWh/m2/day

    Lafayette: 750 W/m2

    4.36 kWh/m2/day

    DNI Averaged over 24 hrs: 182 W/m2

    Compare with solar constant of 1353W/m2

    24 hrs x /hour

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    Global DNI

    Direct Normal Irradiance is the fraction of sunlight which is not

    deviated by clouds, fumes or dust in the atmosphere and that

    reaches the earthssurface in parallel beams for concentration.

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    U.S. DNI

    Lafayette: 4.36

    kWh/m2/Day

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    U.S. Energy Sources By Demand

    Base Load

    Power

    Generation

    http://eia.gov/totalenergy/data/annual/
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    U.S. Energy Information Administration

    Annual Energy Outlook

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    U.S. EIA Annual Energy Outlook

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    U.S. EIA Annual Energy Outlook

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    U.S. Electric Capacity

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    Figure 1. U.S. Energy and Geothermal Resources

    Note: U.S. Total Resource Base from Characterization of U.S. Energy Resources and

    Reserves, December 1989, U.S.

    Department of Energy, DOE/CE-0279. Data for Estimated Accessible Geothermal

    Resource and Estimated Developable

    Resource are from Table 4 of this report.

    0.3% total

    657,000 BBOE

    U.S. Total Resource Base

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    Solar Energy Generation

    3 Main Components Solar Collector

    Energy Conversion

    Energy Storage Collector Technologies

    Photosynthesis converts light energy to chemical energyin plants

    Photovoltaics converts sunlight directly into electricity

    Solar Thermal Concentrating Solar Thermal (CSP)

    Direct Solar Thermal

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    Concentrating Solar Thermal (CSP)

    CSP concentrates the light from the sun tocreate heat, which is transferred to a fluid. The

    HTF is then used to power a heat engine,

    which turns a generator to produce electricity. Heat transfer fluid that is heated by the

    concentrated sunlight can be a liquid or a gas.

    Heat engine types include steam engines,Stirling engines, etc.

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    Concentrating Solar Thermal

    Different Forms Dish: Focuses sunlight from area onto a focal point,

    usually operating an external heat engine

    Power tower: A field of tracking mirrors focuses

    radiation onto point, creating high pressure steam fortraditional steam power cycle

    Parabolic Trough: A field of mirrors focusing radiationonto a heat transfer element, which carries a fluidthrough the field, for power production

    Fresnel Lens: Uses a series of long, narrow, shallow-curvature (or even flat) mirrors to focus light onto oneor more linear receivers positioned above the mirrors

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    CSP projects could generate over

    6 times the power needed by the U.S.

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    Dish System

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    Power Tower

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    Power Tower

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    Parabolic Trough

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    Parabolic TroughHistory of Development

    Archimedes212 BC

    http://www.willthomas.net/Convergence/Weekly/Burning_Mirrors.htm
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    History of Development

    1912 first parabolic trough collector by Shuman in Cairo

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    History of Development

    No development until the 1970s oil crunch Research and Development efforts led to Solar

    Energy Generating Systems (SEGS)

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    Solar Electric Generating Stations

    (SEGS)

    Between 1984 and 1991, the United States built nineSEGS plants in California's Mojave Desert, and today theycontinue to provide a combined capacity of 354megawatts of electrical energy annually, power used in

    500,000 Californian homes [source: Hutchinson]. SEGS I through IX (still in operation) built by LUZ

    (eventually went out of business) have generated farmore power than all other solar technologies combined

    Economic optimization drives plants to larger and largersizes

    High O&M costs

    High temp requirement restricts use to SW U.S.

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    Power CycleSolarSteam Rankine Cycle

    Heat transfer fluid (high temperature oil) isheated to about 740 F

    Heat used to boil water, creating high pressure

    steam (100 bar) High pressure steam expanded in a turbine,

    which in turn spins an electric generator

    Low pressure steam is then cooled andcondensed back into water to begin theprocess again

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    Rankine Cycle

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    T-s diagram for Ideal steam

    Rankine cycle

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    Organic Rankine Cycle (ORC)

    Similar to Steam Cycle except that the workingfluid is an organic (carbon based) fluid often arefrigerant

    Organic fluids often have lower boiling points

    than water, allowing lower temperatureresources to be employed in power generation

    Because of lower temperatures and pressuresinvolved, the entire system can be

    compartmentalized and operated remotely,without onsite supervision and very littlemaintenance

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    Why Organic Fluids?

    Steam dome comparison

    Dry fluid vs. Wet fluid

    Condensing pressures above ambient

    Low-maintenance turbines

    Simplified turbine design (related to fluid density

    and to smaller expansion pressure ratios

    inlet/outlet)

    Opportunity for Recuperation due to drying

    nature

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    T-s diagram for

    ORC

    in

    out

    in

    out

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    Working Fluid Selection

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    Solar Thermal & ORC

    Solar heat and ORC technology was firstattempted to be merged in the Coolidge SolarIrrigation Project in the early 1980s

    Suffered from problems including low collector

    performance and O&M problems with thecooling tower

    ORCs have become more mainstream with use ingeothermal and industrial waste heat

    applications Combining ORC technology with Parabolic Trough

    technology proposed by NREL in early 2000s

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    ORC Solar ThermalPros and Cons

    Smaller scale ORCs have several advantages over large, centralgenerating stations Lower temperature operation

    Less expensive HTF

    Smaller solar field, more efficient solar field

    Possibility of using air-cooling (radiator), eliminating need for largeamounts of make-up water

    Simple

    Can be operated remotely

    Supports integration of modular systems using standardized designsand prefabrication Minimizes on-site erection

    Shipment to site in containers

    Potentially lower capital costs

    Disadvantages Lower efficiencies

    Not optimal for displacing base load power

    1 MW ORC plant at Saguaro Power Plant south

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    1 MW ORC plant at Saguaro Power Plant south

    of Phoenix, AZ. Solargenix, APS

    2006

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    2 MW ORC plant at Holaniku Solar Thermal Plant

    on the Big Island of Hawaii by Sopogy

    2009

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    Energy Storage

    Stored energy allows for off peak dispatch tothe power cycle

    Heat can be stored during the day and then

    converted into electricity at night. Many types of energy storage in use and

    under investigation

    Two tank storage systems in use (hot and cold)

    Thermocline energy storage (one tank)

    Solid media (concrete)

    Phase Change Materials (PCMs)

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    Energy Storage

    Advantage of CSP overPhotovoltaics is the Storage of

    energy. Heat storage is a far

    easier and more efficient

    method than storing electricity. Solar thermal plants that have

    storage capacities can

    drastically improve both the

    economics and the

    dispatchability of solarelectricity.

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    American Recovery and Reinvestment

    Act of 2009

    Louisiana DNR received funds to distribute for

    projects

    EmPower LouisianaRenewable Energy

    Program

    Awarded funds to the University of Louisiana

    for development of a grid-tied solar thermal

    power plant in partnership with CLECO Power,LLC

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    Goals

    LDNR goals: To encourage the development, implementation and

    deployment of cost-effective renewable energytechnologies in Louisiana, to support the creation of

    additional employment opportunities, and tostimulate market demand for other emergingrenewable energy systems

    UL goals:1) Fulfill the Grant requirements

    2) Evaluate the feasibility and commercial viability oflarger scale solar thermal power plant in Louisiana

    3) Have a research/educational facility useful for futureUL/CLECO research

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    Scope of Work

    1) Obtain all necessary permits and site evaluations

    2) Obtain bids and place orders or sign contracts forall required equipment, designs, and services

    3) Prepare the site for installation4) Receive the equipment

    5) Install the equipment

    6) Test the completed system7) Operate the system to produce renewable power

    8) Report on the findings of the project

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    Preliminary Design

    Located at new UL/CLECO Energy Research

    Center in Crowley, LA

    20kWe of net electric output to grid

    245 Solar collectors oriented on N-S and on E-

    W axis

    Utilization of 65 kW ORC cycle power block

    Two tank Thermal Storage System

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    Projected Outcomes

    Create or retain 2.29 full-time equivalent jobs

    Produce 171,806 kWh of energy annually

    Offset the production of 79.8 metric tons of

    CO2 emissions

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    System Schematic

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    Site Plan

    Solar Field

    Thermal

    Storage

    Power Block

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    Site Plan

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    Sopogy

    Founded in 2002 at the Honolulu, Hawaii based clean technology incubator known asEnergy Laboratories

    SOlar POwer EnerGYand TechnoloGY

    Manufactures MicroCSP parabolic solar trough

    Smaller, lighter, lower temperature, lower capital cost

    Creates a good fit with small scale ORC power generation

    Operates first MicroCSP and ORC power generation facility on big island of Hawaii -2009

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    Collector Performance

    For UL plant:

    Collector Efficiency at Design = 63.40%

    Solar Collector Heating Element

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    Solar Collector Heating Element

    Heat Transfer

    Process qin Mirror focuses radiation onto

    element at 5 Conduction 5-4

    Free Convection and Radiation

    4-3

    Conduction 3-2

    Forced Convection 2-1

    Process qout Reflection, Free Convection

    and Radiation 3-4

    Conduction 4-5

    Radiation 5-7

    Forced Convection 5-6

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    ElectraTherm Developed ORC power generation unit, specialized for

    waste heat applications; provided by CLECO. Green Machine produces 65 kWe from low

    temperature (200 F) water

    Incorporates patented expander, pumps, and heat

    exchangers in an enclosed compartment No Recuperation

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    Screw expander

    Scroll compressor operating in reverse

    Less sensitive to varying operating conditions

    Less sensitive to condensation

    Single stage

    Low maintenance

    Less efficient than turbine optimized to oneoperating point

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    ORC Analysis

    Define steady state operating points for UL plantoperating at 20 kW net

    Determine cycle 1stLaw thermal efficiency

    Given:

    ElectraTherm Green Machine

    75% Expansion Efficiency

    91% Generator Efficiency

    60% Pump Efficiency (Estimated)

    Water cooled condensing

    Water as HTF

    R245fa as working fluid

    15 kW of parasitic losses external to cycle

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    Steady State Equations

    T Di f UL C l

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    T-s Diagram of UL Cycle

    in

    out

    in

    out

    1

    23

    4

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    Design Considerations

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    Design Considerations

    Superheating not advantageous

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    Superheating not advantageous

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    Design ConsiderationsHTF, in

    WF,out

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    Analysis, State 1

    Select 20 C pinch point at WF exit from Boiler

    THTF,in=96.1 C therefore Tboiler, out =76.1 C =T1

    Select T1

    = Tsat,g

    which corresponds to

    Psat=716 kPa

    From tables h1=459.1 kJ/kg; s1=1.777 kJ/kg-K

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    Analysis, States 2 and 3

    Select 4 C pinch point at WF exit for condenser Tcoolant, in=20 C therefore TWF,out=24 C=T3

    Select T3=Tsat,f which corresponds to Psat=142.4

    kPa=P3

    From Tables at Psat; h3,f=231.1 kJ/kg; s3,f=1.109

    From State 1, assume isentropic expansion (s2=s1)

    to constant pressure line at P3=P2

    From tables, h2,s=429.7 kJ/kg

    Then, from calculate h2=437.05 kJ/kg

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    Analysis, State 4

    Assume isentropic compression from P3to P4(s4=s3) and P4=P1

    At P4=716 kPa and s4=1.109 kJ/kg-K; h4,s=231.6

    kJ/kg and T4=24.2 C

    From =.6 calculate h4=231.93 kJ/kg

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    Turbine Work and Pump Work

    From = .91 and 35kW desiredoutput, calculate Wmechanical = 38.5 kW

    Then =38.5 kW and mWF =1.746

    kg/s

    Then =1.455 kW

    Then =396.64 kW

    And =359.6 kW

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    Thermal Efficiency

    Tlow =20 C (293.15 K)Thigh =96.1 C (369.25 K)

    ncarnot=0.2065

    ngenerator=.91Wturbine =38.5 kW

    Wpump =1.455 kW

    Qboiler =396.64 kW

    ncycle =.0847

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    Completing the Design

    From energy balance around boiler candetermine required HTF flow rate

    From energy balance around condenser, can

    determine required Coolant flow rate

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    Actual Design State Performance

    Difference in actual and ideal cyclesPressure drops due to friction losses

    Expander efficiency at part load

    Pump efficiency at part loadTwo Phase Heat Exchanger performance

    modeling

    Where: Then:

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    Solar Efficiency

    =0.042

    Actual plant with parasitic losses

    =0.025

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    Overall Solar to Electric Efficiency

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    Potential Future Markets

    Mid range solar resource areas

    Distributed generation

    Offsets costs at retail price instead of wholesale

    Remote generation (DOE apps)

    Green Power/Renewable Portfolio Standards

    CSP today at 12-14 (14-17)* cents/kWh for centralgenerating

    DOE goal of 5-7 (7-8)* cents/kWh by 2015 with 6 hrs

    storage

    DOE goal of 5 cents/kWh by 2020 with 12-17 hrs storage

    *Greenpeace, the European Solar Thermal Power Industry Association (ESTIA), and the International EnergyAgencys (IEA) SolarPACES Programme have produced this report

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    Questions?