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Prof. Dr. techn. G. Scheffknecht Institut für Feuerungs- und Kraftwerkstechnik INTRODUCTION AND OVERVIEW OF OXYFUEL COMBUSTION FOR POWER PLANT WITH CCS Oxyfuel Combustion Capacity Building Course Wuhan, China 27 th October 2015 by Joerg Maier Contact: [email protected]

INTRODUCTION AND OVERVIEW OF OXYFUEL COMBUSTION FOR …ieaghg.org/docs/General_Docs/5oxy presentations/Capacity Building... · compression Oxygen CO 2 O 2) Air Separation unit (ASU)

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Page 1: INTRODUCTION AND OVERVIEW OF OXYFUEL COMBUSTION FOR …ieaghg.org/docs/General_Docs/5oxy presentations/Capacity Building... · compression Oxygen CO 2 O 2) Air Separation unit (ASU)

Prof. Dr. techn. G. Scheffknecht

Institut für Feuerungs- und Kraftwerkstechnik

INTRODUCTION AND OVERVIEW OF OXYFUEL COMBUSTION FOR POWER PLANT WITH CCS

Oxyfuel Combustion Capacity Building Course

Wuhan, China

27th October 2015

by

Joerg Maier

Contact:

[email protected]

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History of 6th Oxy-fuel Course

1. KEPRI, Deojeon, Korea, 2009

2. Tshinghua, Beijing, China, 2010

3. OCC2, Yeppon, Australia, 2011

4. Institute of Technology, Tokyo, Japan 2012

5. OCC3, CUIDEN, Ponferrada, Spain, 2013

6. Huazhong University, Wuhan, China, 2015

J.Maier, Wuhan 2015

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Background: Global Drivers why CCS

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• By 2050, global population will rise from 7 to 9 billion

people

• World energy demand is expected to increase by

50% over the next 20 years Fossil fuels (coal, gas and oil) represent 80% of the global energy mix

• Renewables could make

up 30% of the global

energy mix* by 2030

Background: Global Drivers why CCS

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Capture CO2 capture,

purification und compression

Transport Pipelines, Ships,

Trucks Projects:

ROAD (NL) COCATE (EU), IMPACTS (NO), Compostilla

(ES)

Storage/

Utilization Geological

formations, saline aquifers, EOR, etc. Projects: Sleipner (NO),

Hammerfest (NO)

Background – CCS Technology

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•CO2 captured from flue gas. Post-

combustion

•Fuel converted into H2 und CO2. •Capture of CO2. •H2 used as fuel.

Pre-combustion

•Oxygen separated from air. •Combustion of fuel using O2 instead of air. •Flue gas composition is mainly CO2 und

H2O.

Background – CCS capture processes

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Ash removal /

cooler /

condenser / FGD

Steam

Fuel

Power

CO2 –rich

Flue Gas

Conc.

Stream

of CO 2

Boiler or

Gas Turbine

Steam

Turbine

Purification /

compression

Oxygen

CO2 (SO2)

Air

Separation

unit (ASU)

Air

Recycled Flue Gas (RFG)

Nitrogen

Vent

Front end Back end

Wall, T. et al (2009) An overview on oxyfuel coal combustion: State of the art research and technology development.

Oxy-fuel Technology overview

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Road Map Vattenfall

Source: Vattenfall IEA Cottbus 2009

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Research Oxy-fuel

Research

areas

Pollutant

formation and removal

Corrosion

Gas and particle radiation

modelling

Air Separation

CFD & Process Simulation

Oxy-fuel combustion

CO2-Compression

Slagging and fouling

Operation control & automatisation

J.Maier, Wuhan 2015

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Research Institutes supporting Oxy-Developments

J.Maier, Wuhan 2015

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Source: Stanley Santos

Historical Progression of Oxyfuel

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Vattenfall 30MWth,

Germany

Cuiden 20MWth PC

30MWth CFB,

Spain

Callide 30MWe,

Retrofit,

Australia

Industrial Oxyfuel Power Plant Pilots

J.Maier, Wuhan 2015

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Notes:

No S removal

Slip stream for partial CO2 recovery

Primary gas has cooler/condenser to dry gas, which

removes some SOx

Hg removed in fabric filter?

Callide Process schema

source: C. Spero, Ponferada 2013

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White Rose 448 MWe Oxy-coal power plant

426MWe oxyfuel combustion

90% capture, 2MT CO2

annually

75km onshore pipeline

potential to transport 100MT

CO2 annually

Deep saline aquifer in South

North Sea

Approx. 2 billion investment,

€300 NER300 funding

awarded.

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• The US oxy-fuel project FUTUREGEN 2.0 did not receive funding from the US government.

• In Europe, Endesa’s 300MW CFB Compostilla project and Jänschwalde 250MW are not being progressed.

In UK the White Rose project is being progressed (feasibility study).

Total’s oxy-natural gas pilot plant at Lacq (30 MW) finished first, monitoring of the reservoir ongoing.

• In China, the Shenmu-Shanxi (200 MW) feasibility study

• Korea, Young Dong (100 MW) project changed to Biomass

• In Australia, the Callide Oxyfuel Demonstration successfully finished

operative trials.

Status ongoing activities

J.Maier, Wuhan 2015

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SaskPower’s Boundary Dam- 139 MW CCS Project

First Coal-fired power plant to employ full-scale postcombustion CCS

Location: Estevan, Saskatchewan, Canada

Budget: 1.4 billion dollars

Capture: approx. 1 million metric tons of CO2

(90% of emissions from Unit 3)

Process: Amine based for CO2/SO2 capture

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Coal power39.6%

Gas Power

8.4%Cement

5.3%

Chemicals

3.3%

Iron and steel10%

Gas Processing4.3%

Natural gas synfuel

4%

Biomass synfuel20.2%

Biomass power5%

CO2-Anthropogenic sources

Transfer of Oxyfuel Technology

J.Maier, Wuhan 2015

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Energetic

efficiency

Renewable

energies

CO2 Capture and

Storage (CCS) + +

“CCS is an essential part of the portfolio of

technologies

needed to achieve substantial global emissions reductions.”

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Thank you for your attention!

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