Technical Challenges of Goethermal Energy...

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Technical Challenges of Goethermal Energy Utilisation Geir Þórólfsson Mechanical Engineer HS Orka Jónas Matthíasson Mechanical Engineer Verkís

Transcript of Technical Challenges of Goethermal Energy...

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Technical Challenges of

Goethermal Energy Utilisation

Geir ÞórólfssonMechanical Engineer

HS Orka

Jónas MatthíassonMechanical Engineer

Verkís

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Hitaveita Suðurnesja Geothermal

Power Plants

• Svartsengi 1: 2 x 1 MWe og 50 MJ/s (decommissioned)

• Svartsengi 2: 75 MJ/s

• Svartsengi 3: 1 x 6 MWe

• Svartsengi 4 7 x 1,2 MWe

• Svartsengi 5: 1 x 30 MWe og 75 MJ/s

• Svartsengi 6: 1 x 30 MWe

• Reykjanes : 2 x 50 MWe

» Total: 324,4 MWe and MJ/s

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Year of historic lava flow

High-temperature system

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Geothermal Power Plant Main

Parts• Geothermal wells

• Well piping

• Separator station

• Steam piping

• Power station

• Steam turbine – Generator

• Cooling system

• Substation, switchyard

• High voltage line

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Design tasks

• Mechanical (in approximate time

sequence)

– Preliminary Design: Concept design, dialogs

between owner, designers and main machine

producer

– Process Flow diagram (PFD): Showing main

equipment, connecting pipelines, valves, and

flowrates

– Process Instrument Diagram (PID): Similar to

PID but with all instuments and their codes for

function

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Design tasks

• Mechanical, continued

– Piping: Pipe dimensions, Pressure ratings,

Design codes and standards, Safety ,

Pressure drop criteria and calculations

– Power station Layout

– Equipment submitted for tendering

– Detail design

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Design tasks

• Electical equipment

– High Voltage

• Single line diagram

• Transformer specifications

• Breakers specifications

• Protection system specifications

– Low voltage

• Distribution cubicles

• Cabling

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Design tasks

• Control system

– Control loops

– Control equipment

• Regulators

• PLC computers

– Remote monitoring

• SCADA system

• Civil engineering

• Architectural drawings

• Landscape design

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Design of a

well

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Geothermal wellsProblems in operation

• Scaling

• Corrosion

• Casing collapse

• Liner break

• Leaks

• Gas

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Two Phase Pipelines

• Avoid slug flow

– Incline two phase pipes down

– Calculate the dimension of condensate pipe

lines to ensure there is space for flash steam

• Keep them anchored

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Rankine Cycle

Boiler

Feedwater

pump

Condenser

Turbinel

Cooling

Condensate

Steam

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Svartsengi – Single Line Diagram

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Equipment design choices

• Separators: Vertical Cyclone or horizontal

gravity?

• Separators on each wellpad or two phase

flow pipeline to a central separator

station?

• Length of main steam pipe?

• Impulse or reaction steam turbine?

• Cooling tower or natural cooling-water?

• Vacuum pumps: Steam ejectors, water

ring pumps, or hybrid?

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Reykjanes Plant

separator

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Reykjanes Principles

• High separator and inlet pressure to reduce

scaling in separators– Steam wetness in low pressure stages is high, danger of erosion

• Double flow reaction turbines– Lower steam velocity reduces danger of erosion

• Seawater cooled condenser– Minumum steam and vapour plumes

• Remote monitoring and control – Lowers operation cost

• Environmentally benign power plant

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Design Principles for Reykjanes

• Independent system for each unit, one

separator, one moisture separator, one cooling

system.

• Easy maintenance

• Ample maintenance space in power station

• Remote operation

• Quality steam

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SCADA system screen: Wellheads, separator , steam and brine controls

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Silbersulfid-Kristalle auf

Chip-Widerstand

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Mynd af lofthreinsikerfi

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Reykjanes Power Station

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Reykjanes condenser

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Inside a

condenser

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Gas exhaust system: Steam

ejectors and intercondensers

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It was difficult to get quality gaskets

when asbestos had been banned

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Hydrogen sulphide can cause cracks in high manganese steel

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50 MW turbine, 80 kg/s, 18,0/0,1 bar

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Drops from silencers are bad for

glass and glossy car surfaces

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GRP (Glass Reinforced Plastic) piping must

be handled with care

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Svartsengi 6 cooling tower. Ice may be a problem.

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Remember

• Preserve exergy

• Avoid scaling

• Silica scaling starts at Tresevoir – 100°C

• Vertical separators can be over-/underloaded

• Direct contact condenser can cause sulfur

scaling in cooling tower and condensers

• Consult operating and maintenance staff

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Everything clear?