Carbon Credit_illustration Through HYSYS Simulation

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    CARBON CREDIT- A New Measure to Shed off GHG Emission

    Subhasish Mitra

    M.Tech

    Department of Chemical Engg, IIT Kanpur

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    Combined power cycle: Brief Recap

    Brayton cycle

    Rankine cycle

    Fuel used : Natural Gas

    Plant capacity : 400 MW

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    Power Plant Process Flow Diagram-Base case CCS facility excluded:

    Steam boiler

    Gas Turbine Block

    HP Steam turbine LP Steam turbin

    Steam condenser

    Flue gas disposed tostack GHGs emission.

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    CO2

    Emission A Known Nuisance

    1. CO2 is the ubiquitous Green House Gas and liable for globalwarming.

    2. Fossil fuel powered power plants are the epicenters for CO2

    emission due to voluminous flue gas disposal beside other

    industries, automobiles and residential release.

    3. Major concern is observed in the recent past to reduce CO2

    emission through various measures and policy formulation (e.

    Kyoto protocol).

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    Brief Case Study:

    Govt decided to put mandate on implementing CO2

    capture facility at the power plant site.

    Normal emission limit from power plant : 1.65 to 1.95

    million ton CO2/yr.

    Emission limit posed by EPA is 7% reduction on 1990

    emission figure of 0.479 tons of CO2/MWh generated

    which translates to 1.425 million ton CO2/yr for our plant.

    Plant capacity : 400 X8000 Mwh/yr

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    Where does our plant stand?

    CO2 Emission : 4079 kmol/hr which translates to 1.44million ton CO2/yr.

    The plant exceeds EPA recommended limit by 0.012

    million ton CO2 p.a.

    Since CO2 emission by the plant is more than EPA

    recommendation, so plant decides to invest upon CCS to

    earn CARBON CREDIT.

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    What is Carbon Credit?

    An instrument created to represent one metric ton of CO2 avoided

    or removed by a carbon reducing project.

    Some definitions:

    Key component of national and international attempts to mitigate t

    growth in concentrations of (GHGs). One Carbon Credit is equal to

    one ton of Carbon.

    A "credit" to emit a ton of carbon dioxide (CO2) issued as part of anemissions trading scheme such as the European Emissions

    Trading Scheme.

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    Company adopts this CCS scheme

    NG toPower Plant

    To Oil/Gasreservoir for EOR

    Oil out

    Void oil/gaswell for

    storage

    Amineabsorptionplant

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    Amine absorption plant simplified PFD:

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    CCS Project Feasibility Analysis:

    A Hysys simulation is made to study the feasibility of

    integrating proposed CCS process with the existing plant.

    Major challenge is to provide huge thermal energy to the

    stripper reboiler. Even auxiliary boiler is also reported.

    But simulation shows reboiler demand can be internallymet.

    Around 85% CO2 scrubbing efficiency is obtained from

    simulation.

    With all economic analysis, it turns out that project is

    feasible.

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    Power Plant Process Flow Diagram-Modified case CCS facility included:

    Stripper reboilersteam is supplied

    from the partiallyderated LP steamturbine.

    CCS unit: Fluegas compression,absorption &transportation

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    CO2 absorption unit:

    Steam to stripperreboiler suppliedfrom LP steam

    turbine O/L.

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    CO2 Transportation Unit:

    Transport pump

    Transportcompressor

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    0.55Combined cycle efficiency

    0.284Rankine cycle efficiency

    0.37Gas turbine cycle efficiency

    0.45Overall efficiency

    MW1072.65Heat input by NG@LHV

    MW1.585Condensate pump

    MW283Boiler heat input

    MW136.2Compressor

    MW16.63ST-2 output

    MW65.31ST-1 output

    MW400GT output

    Energy efficiency before CCS

    Energy Efficiency Before Implementing CCS:

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    Energy Efficiency After Implementing CCS:

    %15.56Efficiency reduction

    0.38efficiency

    MW1072.65Heat input by NG@LHV

    MW1.432Transport pump

    MW18.42Transport compressorMW0.102Lean amine pump

    MW0.067Rich amine pump

    MW47.94Flue gas blower

    MW283Boiler heat input

    MW1.585Condensate pump

    MW136.2Compressor

    MW9.869ST-2 output

    MW65.31ST-1 output

    MW400GT output

    Energy efficiency after CCS

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    Important Facts Behind Economic Analysis:

    Price hike in electricity follows yearly compounding,

    i.e. P1 = P(1+i)n and stops at break even point. n = no of years.

    Straight line depreciation model is followed.

    Payback period is calculated as

    Capital Investment/(Carbon Credit Earned + Depreciation/yr)

    ROI = (Net Profit/Capital Investment) x 100

    Credit from injecting CO2

    for EOR not considered.

    Decline in Carbon credit due to escape from sequestration not

    considered.

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    Cooling Utility Cost for CCS:

    4.02 million $Total

    175243.3941043.120.02110Compressor stage-4cooler

    102166.898608.140.0215.83

    Compressor stage-3

    cooler

    102236.996608.550.0215.834

    Compressor stage-2

    cooler

    115275.104686.180.0216.578

    Compressor stage-1

    cooler

    330684.2841968.360.02118.87Precooler

    314737.1351873.440.02117.96

    Stripper column

    condenser

    2884506.25917169.680.021164.6

    Flue gas blower

    aftercooler

    Total coolingcost ($/yr)

    CW flow

    rate (t/hr)

    Cost $/ton of

    CW

    Equipmentcooling duty

    (MW)Cooling cost

    Cooling water Delta T = 80C, Sp. Heat capacity = 4.314 KJ/Kg/K

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    60.34 million $Total

    1266666.6670.091.76Transport pump

    16323555.560.0922.67Total compressor power

    2.68Transport compressor ST-4

    3.97Transport compressor ST-3

    5.83Transport compressor ST-2

    5.88Transport compressor ST-1

    90666.670.090.13Lean amine pump

    59511.110.090.08Rich amine pump

    42604444.440.0959.17Flue gas blower

    Total cost ($)/yrElectricity cost

    ($) / kwhCapacity (MW)Equipment

    Electricity consumption cost for CCS:

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    Raw Material Cost:

    529.5 ton1.72.42688350MEA make up

    10 min

    (assumed)

    Absorption

    loop inventory

    Total cost

    (million $/yr)

    Unit cost

    ($/kg)Qty (kg/hr)

    Raw material cost

    Basis:

    Make up is replacement of degraded MEA

    MEA degradation rate : 2.5 wt% / week

    Absorption loop inventory : 10 min

    *Total Carbon Reduction Cost :

    $ 56.8 million/Ton of CO2

    *5% contingency cost is included.

    Reported CO2 reductio

    cost in literature:$37-74/ton of CO2

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    Expenditure Summary for CCS:

    yrs6.14Payback period

    million $18.62Carbon credit earned/yr

    million $13.44Revenue after Tax deduction

    %10Tax deduction

    million $9.61Taxable revenue

    million $14.4Revenue/yr through electricty

    % pa5Hike in electricity price

    million $4.87Revenue lost/yr

    Mwhr6.76Electricity generation reduced

    million $4.79Depreciation/yr

    million $0Salvage value

    years30Plant life

    million $69.54Annual Carbon reduction cost

    million $14.36Annual loan installment

    %15Bank loan interest rate

    10Loan repayment duration (Year)

    million $143.6

    Investment cost

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    CCS P j b k l i

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    CCS Project break even analysis

    -60

    -40-20

    0

    20

    40

    6080

    100

    120

    Y1 Y2 Y3 Y4 Y5 Y6 Y7 Y8 Y9 Y10

    Production cost

    Revenue after ta

    ROI

    Hike in electricityprice stopped.

    Break even

    point at ~ 6 yrs

    Costfigures

    inmillion$/%

    ROI

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