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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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7/25/2019 7.44.Session VI EHa and LTr Process Flow and Steam Gathering System v3
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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
7/25/2019 7.44.Session VI EHa and LTr Process Flow and Steam Gathering System v3
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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.php7/25/2019 7.44.Session VI EHa and LTr Process Flow and Steam Gathering System v3
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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!
VISIT GEOELEC.EU