7.44.Session VI EHa and LTr Process Flow and Steam Gathering System v3

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  • 7/25/2019 7.44.Session VI EHa and LTr Process Flow and Steam Gathering System v3

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    Process flow and gathering

    system

    Session VI

    Eln Hallgrmsdttir and Lilja TryggvadttirMannvit Strasbourg, Nov.8, 2012

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    Presentation overview

    Presentations reviewing different work cycles

    Main concept of the gathering system

    Calculated example showing methods usedwithin geothermal steam gathering system

    design

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    Geothermal in Iceland

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    Process flow

    A review of thermodynamic cycles used in

    geothermal energy production with emphasis

    on electricity generation

    Flash steam cycles with single flash and

    double flash as well as different binary cycles

    as ORC and Kalina Cycle are introduced and

    compared

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    Back Pressure Steam Power Plant

    Steam

    separator

    Turbine Generator

    G

    Production wells Reinjection wells

    Phigh

    Plow

    2 phase flow Vapor

    Liquid

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    Back pressure unit - layoutSeparator

    Machine Hall

    Electrical cabinets &

    Control room

    Asphalted area for installation and maintenance purposes

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    0

    100

    200

    300

    400

    500

    600

    700

    00,20,40,60,811,2

    TurbinePower[kJ/kg]

    Turbine outlet pressure [bara]

    Calculated examples

    Different turbine outlet pressure

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    G

    Production wells

    Geothermal

    fluidSteam

    separator

    Turbine

    Condenser

    SteamGenerator

    Silencer

    Mist

    eliminator

    Water

    Condensate

    Condensate

    Cooling tower

    Reinjection wells

    Gas Extraction System

    Steam Power Plant with Condenser

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    Steam Power PlantDouble Pressure

    G

    Production wells

    Two phaseflow Turbine - generatorHP steam

    LP steam

    Reinjection wells

    Condenser Tcw

    Cooling system

    Steamseparator

    LP Steam

    separator

    Two

    phase

    flow

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    SvartsengitheOctopus

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    Steam Power PlantDouble Flash

    Production wells Reinjection wells

    G

    Steam supply systemTurbine - generator

    Primary steam

    Secondary steam

    Condenser Tcw

    Cooling system

    G

    LP Turbine - generator

    Tcw

    Cooling system

    Steam

    separator

    LP Steam

    separator

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    Hellisheiilow pressure unit

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    Steam Power Plant w. District Heating

    G

    Production wells

    Steam supply system Turbine - generatorPrimary steam

    Reinjection wells

    Condenser

    Tcw

    Cooling system

    Steam

    separator

    District

    heating

    system

    Freshwater wells

    To district

    heating

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    District heating plant

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    25. 02. 2008

    Production wells

    Two phase flow

    Steam separators

    Geothermal water

    Steam

    Well head silencers

    Re-injection wells

    Pressure

    regulation

    Geothermal water

    emergency exhaust

    Turbines

    Generators

    Mist separators

    Cooling

    towers

    Hot water tank

    Cold water pump

    Condensers

    Heat exchangers

    De-aerators

    De-aerators

    Condensers

    Process Flow Diagram

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    GTsource

    Tdischarge

    Phigh

    Plow

    Condenser

    Turbine Generator

    Circulation pump

    Evaporator

    Tcw

    Cooling system

    Binary Cycles

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    GTsource

    Tdischarge

    Phigh

    Plow

    TcwCondenser

    Turbine Generator

    Circulation pump

    Evaporator

    Recuperator

    Cooling system

    Binary Cycleswith Recuperation

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    Binary Plant BerlinEl Salvador

    LaGeo

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    G

    Separator

    High temp

    recuperator

    Low temp

    recuperator

    Condenser

    Evaporator

    TurbineGenerator

    Tsource

    Tdischarge

    Tcw

    Circulation pump

    Cooling system

    Binary CyclesKalina

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    Hsavik Kalina plant

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    20 02 5 03 0 035 040 04 5 05 0 055 0

    2 0

    4 0

    6 0

    8 0

    1 0 0

    1 2 0

    1 4 0

    Heat transfer

    Temper

    ature

    0 0 , 2 0 , 4 0 , 6 0, 8 1

    5 0

    6 0

    7 0

    8 0

    9 0

    1 0 0

    1 1 0

    1 2 0

    Heat Transfer

    Temperature

    ORC Kalina

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    G

    Tsource

    Tdischarge

    Coolingsystem

    Binary CyclesKalex

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    Work Cycle Comparison

    Specific Power

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    0

    2

    4

    6

    8

    10

    12

    80 85 90 95 100 105 110 115 120 125 130

    /W

    Inlet Temperature [C]

    Kalina

    Kalex

    ORC

    Work Cycle Cost Comparison

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    G

    G

    G

    Steam supply system Turbine - generator

    Primary binary

    turbine - generator

    Evaporator

    Secondary binaryturbine - generator

    Cooling system

    Cooling system

    Production wells Reinjection wells

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    Demonstration of model

    Turboden ORC model:

    http://www.turboden.eu/en/rankine/rankine-

    calculator.php

    http://www.turboden.eu/en/rankine/rankine-calculator.phphttp://www.turboden.eu/en/rankine/rankine-calculator.phphttp://www.turboden.eu/en/rankine/rankine-calculator.phphttp://www.turboden.eu/en/rankine/rankine-calculator.phphttp://www.turboden.eu/en/rankine/rankine-calculator.phphttp://www.turboden.eu/en/rankine/rankine-calculator.phphttp://www.turboden.eu/en/rankine/rankine-calculator.phphttp://www.turboden.eu/en/rankine/rankine-calculator.phphttp://www.turboden.eu/en/rankine/rankine-calculator.phphttp://www.turboden.eu/en/rankine/rankine-calculator.phphttp://www.turboden.eu/en/rankine/rankine-calculator.php
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    Gathering System

    This session will present an overview of the

    design process of a geothermal gathering

    system with emphasis on particularities of the

    geothermal fluid.

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    Two phase flowSteam separators

    Geothermal

    water

    Steam

    Re-injection wells

    Pressure

    reliefProduction wells

    Turbines

    GeneratorsMist separators

    Cooling

    towers

    Condensers

    Steam Supply - Preliminary P&ID

    emergency exhaust

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    Nesjavellir Power Plant

    Separation

    station

    Steam vent

    station

    Steam

    pipelines

    Two phase

    flow

    PowerPlant

    Production

    Well

    Cooling towers

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    Gathering system- Design

    Design standards

    Standards i.e.

    Pressure directive

    97/23/EC Pressureselection

    Chemical constraints

    Power generation

    Productivity curves

    0

    200

    400

    600

    800

    1000

    1200

    1400

    1.00 10.00 100.00

    SiO2(m

    g/kg)

    Pressure (bar-a)

    quartz solubility (F&P82)

    amorphous silica solubility (F77)

    330 C

    300 C

    270 C

    240 C

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    Chemical constraints

    Scaling

    Corrosivity

    Radioactivity

    Mitigation:

    Pressure control / closed loop system

    cleaning of the steam

    Inhibitors

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    h = 1600 kJ/kg

    h = 1800 kJ/kg

    h = 2000 kJ/kg

    h = 2200 kJ/kg

    0

    50

    100

    150

    200

    250

    300

    350

    400

    450

    500

    0 2 4 6 8 10 12 14 16 18 20

    Turbinep

    ower[kJ/kg]

    Separator pressure [bara]

    Assumptions:

    Total turbine efficiency: 0,8

    Power generation

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    Typical productivity curves

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    Well PumpLow Enthalpy

    Type

    Submersible pump

    Line shaft pump

    Selection and operation Depth

    Temperature

    Scaling

    Bubble point

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    Gathering SystemDesign load

    Constant load Weight

    Pressure

    Variable load (depending on location) Wind load

    Snow load

    Earthquake

    Frictional load Thermal expansion

    Friction

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    Gathering System - Pipelines

    Pipe laying

    Under ground

    Above ground

    Material selection

    Pipe size

    Pressure/temperature

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    Steam Supply SystemPipelines

    300

    400

    500

    600

    700

    800

    900

    1000

    0 20 40 60 80 100 120 140 160

    Pipediamete

    r[mm]

    Flow [kg/s]

    7 bar-a

    20 bar-a

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    Gathering systemroute selection

    Public safety

    Environmental impact

    Restriction on land

    Cost efficiency

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    Steam pipelines

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    Steam Supply - Layout

    Central separation station Satellite separation stations

    Individual separators

    Central Satellite Individual

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    Power plant layout

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    Steam Supply - Separators

    Cyclone separators

    Gravity separators

    Efficiency

    Steam separator and moisture separator

    should together achieve 99,99 % bw.liquid removal or better

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    Calculated example

    The presenter will go through a calculated

    example to show methods used for basic

    engineering within steam gathering system

    design. The example taken will be connectedto the special conditions encountered in

    geothermal energy.

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    Example

    Example for 1200 kJ/kg well enthalpy 40-50C condensing temperature

    Back pressure

    Objective

    Maximize the power production

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    Assumptions

    We know the reservoir enthalpy

    We know the condenser temperature

    Separation pressure does not influence the well

    flow

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    Example, condensing unit

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    Example, condensing unit

    The maximum power will be 12,4 MW

    Entalpy = 1200 kJ/kg

    Condensing pressure 0,075 bara / temperature

    40C

    Separation pressure 6 bara

    Flow 100 kg/s

    What if we selected backpressure instead?

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    Example, back pressure

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    Example, back pressure

    The maximum power will be 6,4 MW

    Entalpy = 1200 kJ/kg

    Separation pressure 12 bara

    Flow 100 kg/s

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    Example

    Optimum separation pressure is 6 bara, is thatok?

    Saturation temperature for 1200 kJ/kg is 273C

    0

    200

    400

    600

    800

    1000

    1200

    1400

    1.00 10.00 100.00

    SiO2

    (mg/kg)

    Pressure (bar-a)

    quartz solubility (F&P82)

    amorphous silica solubility (F77)

    330 C

    300 C

    270 C

    240 C

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    Thank You!

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