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    Solar & Biomass Hybrid

    5 MW Hybrid Solar Thermal + Biomass Plant

    Neha Energie

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    Technology Overview

    Financial Overview

    Conclusions

    TABLE OF CONTENTS

    2

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    Plant Schematic Hybrid

    Solar Thermal Biomass Plant

    Pump

    Steam

    TurbineGenerator

    Condenser

    Heat

    Exchanger

    Electricity

    Parabolic Troughs

    Biomass Gasifier

    Two-Stage Boiler

    3

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    2800 kJ/kg

    3306 kJ/kg

    498 kJ/kg

    1097 kJ/kg

    20%

    20%

    60%

    x

    xx

    x100

    200

    300

    400

    600 psia isobar

    Superheated steam required to generate useful power

    o Requires almost 80% of the energy from the boiler to reach saturated

    vapor phase.

    o Use solar energy for this purpose.

    Plant Operation Hybrid

    Solar Thermal Biomass Plan

    4

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    Solar & biomass are the only renewable resources that

    make sense in most of the parts of India

    Solar only approach can utilize either PV or solar

    thermalo Both suffer from low capacity factor in India due to tropical

    conditions (high humidity and rain showers)

    Biomass only approach works but supply can be an

    issue, especially in drought conditions.

    o Results in variable O&M costs

    5

    Why Hybrid Solar + Biomass Plant

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    Parabolic trough concentrator

    Biomass Gasifier

    Boiler (producer gas burner)

    Super heated steam turbine

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    Major System Components

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    Parabolic Trough Concentrator

    High efficiency and durable mirror

    film technology

    Temperatures up to 300oC.

    Less thermal losses.

    Modular & scalable.

    Space frame light weight technology

    Ease in construction and tracking.

    Medium Temperature Parabolic Trough (MTPT)

    Fig: MTPT pilot plant at Florida

    ( Source: SET Florida)

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    MTPT - Technical SpecificationsTECHNICAL DETAILS

    Construction Materials Aluminum and Steel

    Reflective Surface Reflective Film

    Reflectivity 0.94Absorber Material Steel

    Selective Surface Cermet

    Absorber Envelope Borosilicate Glass

    Max Wind Speed tolerance 110 mph

    Life Expectancy 20 years

    TROUGH GEOMETRY

    Module Aperture Width 2.74 m 9 ft

    Module Aperture Length 12 m 39.4 ft

    Module Aperture Area 32.9 sq. m 354 sq. ft

    Focal Length 1.49 m 4.9 ft

    Number of modules per Solar Collector Assembly (SCA) 8

    Total SCA length 100 m 328 ft

    Net Aperture Area 263 sq. m 2830 sq. ft

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    Gasifier

    Gasification

    o Thermo-chemical process converts biomassinto a gas.

    o The resulting gaseous compound is called Syngas

    Syngas consists of hydrogen and carbon monoxide (and

    lesser amounts of carbon dioxide and other trace gases)

    under oxygen depleted, high pressure, high-heat and/or

    steam conditions.

    The gasifier is essentially a chemical reactor where various

    complex physical and chemical processes take place.

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    Other System Components

    Boiler

    o Customized to provide superheated steam

    o Designed to burn syngas from gasifier

    o NOx emissions up to 30 ppm

    o Temperatures up to 450 C are achievable

    o Efficiency 88 to92%

    Turbine

    o Multistage impulse, extraction cum condensing

    o Designed to produce 5 MW electricity

    o Working at 450C and 40atm

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    Proposed Plant DetailsSOLAR FIELD

    Total number of modules 960

    Arrangement 3 loops in series & 20 strings in parallel

    Mass flow rate 5 kg/s

    Working Fluid Therminol VP-1

    Energy contribution from solar field annually at 1000W/m2 18%

    TURBINE

    Inlet temperature 450 C

    Total thermal energy input for the steam turbine 16.67MW

    Net electric output of the steam turbine 5MW

    BIOMASS GASIFIER

    Arrangement 3 numbers in parallel

    Model Ankur Scientific gasifiers ( WBG-2200)

    Rated gas flow 4,950 Nm3/hr

    Average gas calorific value 1100 Kcal/Nm3

    Rated thermal output 54,45,000 Kcal/hr

    Maximum biomass consumption Maximum 1980 Kg/hr

    Moisture content < 20% (Wet Basis)

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    Proposed Plant Operation

    When Solar Radiation is available

    Solar field heats the working fluid (Therminol) from an input temperature

    of 1200C to 250oC at 40atm saturated vapour.

    The working fluid passes through the biomass boiler to reach the steam

    turbine at input temperature of 4500C 40atm super heated.

    One gasifier only runs at 50-70% capacity and the others get turned off.

    When Solar Radiation is not available

    Therminol bypasses the solar field and is completely heated in the

    boiler.

    All gasifiers run at full capacity to provide required thermal input of

    16.67MW/H.

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    Expected Plant Performance Expected energy output

    o

    Solar - 67,01,400 kWh (18%)

    o Biomass - 3,05,28,600 kWh (82%)

    o Total - 3,72,30,000 kWh

    Annual Energy contribution from solar - 18% @ DNI: 5.4

    Daily Biomass consumption - 116 tonnes

    Annual Biomass consumption - 36,000 tonnes

    Total biomass savings (approx) - 7500 tonnes a year

    Assumptions:-

    Plant uptime : 85%

    Boiler efficiency : 90%

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    Technology Overview

    Financial Overview

    Conclusions

    TABLE OF CONTENTS

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    Important AssumptionsASSUMPTIONS

    Plant Capacity 5 MW

    Plant Load Factor 85%Energy Generation in Units 37.23 million units

    Auxiliary Consumption 8%

    Tariff INR 7.50

    Biomass Consumption 36,000 tonnes per annum

    Biomass Cost including transportation INR 2,500 per tonneTotal Project Cost including IDC INR 933.6 million

    Debt Equity Ratio 70:30

    Term Loan interest rate 13%

    Working Capital interest rate 13%

    Repayment of debt 1 year moratorium + 9 yearsO&M cost INR 2 million / MW

    Escalation of Biomass rate 5% per annum

    Escalation of O&M cost 5% per annum

    Power Tariff Increase 2% per year

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    Plant and Machinery Break UpPLANT COST BREAK UP

    LAND AND SITE DEVELOPMENT 49.50

    PLANT AND MACHINERY 699.1

    Boiler & Auxiliary 10.0

    Turbine & Auxiliary 55.0

    Solar Field 510.0

    Gasifier 41.4

    Civil Works For Boiler, Turbine & Other Equipment 30.0Power Evacuation & Distribution System 20.0

    Fuel Handling System 10.0

    Others 22.7

    EPC CHARGES 45.0

    PREOPERATIVE EXPENSES INCLUDING IDC AND

    CONTINGENCIES 117.22

    TOTAL PLANT COST INCLUDING WC MARGIN 933.6

    All figures in INR million

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    Important RatiosIMPORTANT RATIOS

    DSCR

    - Average 1.50- Minimum 1.01

    - Maximum 21.39

    IRR 14.67%

    Equity IRR 17.43%

    Payback Period 7thyear from COD

    LEVELIZED COST OF ELECTRICITY

    Assumed Return on Equity 15%

    Levelized Variable Cost INR 3.49

    Levelized Fixed Cost INR 4.41

    LEVELIZED COST OF ELECTRICITY INR 7.90 PER UNIT

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    Technology Overview

    Financial Overview

    Conclusions

    TABLE OF CONTENTS

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    THANK YOU!

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