R&D Activities - University of Newcastle · 2014-03-13 · Fundación Ciudad de la Energía...

Fundación Ciudad de la Energía (CIUDEN)

CIUDENCIUDEN´́s CCS large scales CCS large scale R&D ActivitiesR&D Activities

Monica Lupion4th

APP OFWG Oxyfuel Capacity Building Course

Tokyo Institute of Technology, Tokyo, Japan –

September 2nd‐

3rd

, 2012

24th APP OFWG Oxyfuel Capacity Building CourseTokyo Institute of Technology, Tokyo, Japan – September 2nd‐ 3rd , 2012

ContentContent

• Fundacion Ciudad de la Energia (CIUDEN)• CCS large pilot scale facilities: es.CO2

Centre

• OXYCFB300 Compostilla Project

• Concluding remarks


An initiative of the Spanish AdministrationAn initiative of the Spanish Administration

CIUDEN

was

created

by

the

Spanish

Government

in

2006

as

a

R&D institution fully conceived for collaborative research in CCS and CCTs.

An initiative to strength to social, industrial and technological base in Spain and by extension in Europe.


CIUDENCIUDEN’’s Attributess Attributes


CIUDEN’s tecchnological R&D by

creating a Centre for Advanced

Technologies on Clean Coal

A worldwide reference point

for clean coal use activities

Eco‐innovation to prevent

millions of tonnes of CO2

being released into

atmosphere

Clean Coal

Technologies

Actions to support regional

development

Develop and use environmental

recovery techniques in degraded

lands due to mining activityRestoration of the rubble

heaps, in parthnership with the

main local actors: authorities

and civil societyCreating new “green”

jobs, for

the local area, and developing

greening skills also

Energy and

Environmental

Applications

CIUDEN’s regional projects

Reuse of industrial

installations for exhibition,

tourist and social purposes

Conservation of the energy

heritage, scientific

research and dissemination

National Museum of

Energy

Universities, R&D Centers,

Companies (specially from national

energy sector)

Universities, R&D Centers,

Companies (specially from national

energy sector)

In colaboration with the main stakeholders: Companies, City and Regional

Councils, Local Governments

CIUDEN CIUDEN ‘‘s Programmess Programmes


THROUGHTHROUGH

Our overarching objectiveOur overarching objective


ContentContent


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es.COes.CO 22

Centre Centre ‐‐

Basic dataBasic data


Fuels: anthracites, bit & subbit coals, pet coke, sustainable biomassFuels: anthracites, bit & subbit coals, pet coke, sustainable biomass

Pulverized

Coal

20 MWth

Pulverized

Coal

20 MWth

Circulating

Fluidized Bed

30 MWth

Circulating

Fluidized Bed

30 MWth

DeNOX

Dedust

DeSOX

DeNOX

Dedust

DeSOX

CO2

purification and compression CO2

purification and compression

Biomass Gasifier 3 MWthBiomass Gasifier 3 MWth+

OxycombustionOxycombustion

es.COes.CO 22

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Basic dataBasic data


FUEL PREPARATION

BIOMASS

GASIFIER

PC BOILER

20 MWth

CFB BOILER

30 MWthTECHNICAL BUILDINGS

AND CONTROL ROOM

FLUEGAS

CLEANING

FLUEGAS

RECIRCULATION AND

MIXING

CO2

PURIFICATION

CO2

TRANSPORT RIG

es.COes.CO 22

CentreCentre


FUELPREPARATION

SYSTEM

DeNOX

15-30 MWthCFB

BOILER GAS

CLEANINGSYSTEM

COMPRESSIONAND

SEPARATION UNIT

MIX ANDPREHEATING

SYSTEM

20 MWthPC

BOILER

PREHEATINGTRAIN

AIR

FGR1

O2

STORAGEAND

VAPORISATION

O2PREHEATING

FGR2

HIGHEFFICIENCYDeSOXMIXERS

BAG FILTER

STACK

BAG FILTER

CO2

EXPANDER

CPU

FGR2

REC

IRCU

LATION

FGR1

REC

IRCU

LATION

FROM BIOMASSPREPARATION

BIOMASSBIN

GASTREATMENT

BIOMASSGASIFIER

CYCLON

ENGINE

TORCH

PCSILO

es.COes.CO 22

CentreCentre


Raw coal hopper 42 m3

Coal crusher 15 t/h

Crushed coal silos 2 x 120 m3

Bag filter 47,000 m3/h

Ball mill 5 t/h

PC silo 80 m3

Bucket elevator 15 t/h

Dossifiers 4.1‐1.2 t/h

Fuel Preparation SystemFuel Preparation System


COALCRUSHER

15 t/h

CO2INERTIZED BALL

MILL 5 t/h

CLASSIFIER

BAGFILTER

PCSILO

CRUSHEDCOAL SILOS2 x 120 m3

CFBSILO

COALUNLOAD

TO CFB FEEDER

RAWCOAL

HOPPER

COALSAMPLER

BAGFILTER

BUCKETELEVATOR

DOSSIFIERS

TO CFB

PARTIAL RECIRCULATION

TO PCBOILER

TO PC

HOT GASES

CO2INERTIZED

CO2INERTIZED

BAG FILTER

Fuel Preparation SystemFuel Preparation System


Size (m) 24 x 7.6 x 4.5

Burners4 horizontal burners2 vertical burners

Biomass feeding system

Mwth HHV Max oxy mode 20

O2

(kg/h) 6,600

FGR (kg/h) 17,900

Flue gas flow (kg/h) 26,400

Coal flow rate (kg/h) 3,350

Steam (t/h) 25

P(bar) / T (°C) 30 / 420

PC BoilerPC Boiler


PC BoilerPC Boiler


Fuel

Fuel

Fuel

Fuel

Dedust+ SCR

From CFB

CB1To CFB

To CFBCB2CB3

Economizer

Convective Area

RadiantArea

PC BoilerPC Boiler


Furnace Dimensions

(m) 20x2.9x1.7

MWth

maxoxycombustion 30

O2

consumption (kg/h) 8,775

Flue gas recycle (kg/h) 25,532

Flue gas (kg/h) 28,800

Coal consumption (kg/h) 5,469

Limestone feed (kg/h) 720

Steam (t/h) 47.5

P(bar) / T (°C) 30 / 250

CFB BoilerCFB Boiler


CFB BoilerCFB Boiler


Uni

t Cap

acity

(MW

e)

0

100

200

300

400

500

600

1970 1975 1980 1985 1990 1995 2000 2005 2010

Start-Up Year

2015

Pilot Plant Oriental Chem

Lagisza

JEA

Turow 1

VaskiluodonNova ScotiaTri-State

General Motors

AIR-FIRED

CIUDEN TDP

Compostilla

OXY-FIRED

Pilot Plant

Adapted from S Santos, IEAGHG. 2010

Evolution of CFB Unit CapacitiesEvolution of CFB Unit Capacities


FLY ASHSILO

FLY ASHFEEDING SYSTEM

LIMESTONESILO

LIMESTONEFEEDING SYSTEM

SAND SILO

SAND FEEDINGSYSTEM

FUEL SILO

FUEL FEEDING SYSTEM

NATURALGAS

START‐UP

BURNER SKID

BOILER FEED

WATER

FLUE GAS

BOTTOM ASH

FLY ASHSYSTEM

PRIMARYOXIDANT

PRIMARYOXIDANT FAN

OXYGEN

SECUNDARYOXIDANT

SECUNDARYOXIDANT FAN

MIXER

FLY ASH

REC

IRCU

LATION

LIMESTO

NE

SAND

FUEL FEED

AMMONIA

MIXER

MIXER

CB1

CB2

LOOPSEAL

INTREX

CROSSOVER

C

O

N

V

E

C

T

I

O

N

C

A

G

E

CFB Boiler CFB Boiler ‐‐

DiagramDiagram


Technology Bubbling

fluidised bed

MWth

max 3

Oxidant Air

Biomass flow rate (t/d) 15

P(barg) 0.3

T (°C) 800

Efficiency (cold gas basis)

98%(75%)

Footprint ( m2) 90

GasifierGasifier


Block diagram of the CO2

Transport

Experimental Facility3D simulation of CIUDEN´s

Facility

Transportation Test FacilityTransportation Test Facility


Test Activities on OxyCFB CombustionTest Activities on OxyCFB Combustion

• First fire on coal in 3Q/2011• First operation and commissioning on oxyfuel

combustion 4Q/2011• First experimental test runs 1Q/2012• First tests on integrated operation with CPU

start in 3Q/2012 • The CFB pilot is fully booked for testing during

2012-2013


• Local anthracite – Cupo del Bierzo, 34% ash, 1% sulfur

• Petcoke• Bituminous coal• Local lignite

– high ash and sulfur

• Biomass co-firing

Fuel testedFuel tested


Transition (airTransition (air‐‐oxyoxy‐‐air) Flexiair) Flexi‐‐Burn Operation Burn Operation Smooth Transition


Transition (airTransition (air‐‐oxyoxy‐‐air) Flexiair) Flexi‐‐Burn Operation Burn Operation Confirmed Reduction of NOx


ContentContent


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FLEXIBURN CFBFlexible high‐efficiency

CFB combustion technology

OXYCFB300Demo 300Mw CCS oxy‐

CFB power station

RELCOMOxy‐PC firing

MACPLUSAdvanced materials

for oxy‐capture

ECCSEL PPIEuropean distributed and

integrated research

infrastructure

BRISKBiomass gasification

R&DIALOGUESocial perception of CCS

O2GEN2nd

generation

oxy‐fuel

power station

IMPACTSCO2

quality for

transport and storage

OnOn‐‐going R&D Capture and Transport going R&D Capture and Transport ProgrammeProgramme


THE COMPOSTILLA DEMO PROJECT

•

The origin of the EEPR is the global

€200 billion European Economic

Recovery Plan presented by the

Commission on November 2008.

Investment in energy projects was

considered an important tool to

support the economic recovery

•

In July 2009,

the European Council

and the European Parliament

adopted the Commission proposal

for the EEPR. 12 CCS projects

applied for assistance under the

EEPR

•

In December 2009,

the EC granted

financial assistance to six (6)

projects

•

These projects will receive overall

funding of €1 billion

under the

EEPR

BelchatowPost

180 M€

Jaënschwalde

Oxy‐PC180 M€

Rotterdam 2

Post180 M€

COMPOSTILLAOxy‐CFB

180 M€

Hatfield

Pre180 M€

Porto Tolle

Post100 M€

COMPOSTILLA: THE SPANISH EEPR PROJECT

4th APP OFWG Oxyfuel Capacity Building CourseTokyo Institute of Technology, Tokyo, Japan – September 2nd‐ 3rd , 2012 30

BASIC DATA



Oxy Mode

Gross power (MWe) 323

Boiler efficiency (%, LHV) 94.3

CO2

emission (g/kWh‐net) 97

CO2

capture ratio (%) 91

CO2

captured in the first 5 years of operation (Mt) ~ 5


BASIC DATA


OxyCFB APPROACH: FACILITIES

VTT 100 kW

CANMET 1 MW

2008 2010 2011 2012 20152009

CIUDEN 30 MW

Compostilla 300 MWe

Lagisza 460 MWe (AirCFB)



Pilot scale

Technology

Development

Demo scale

Validation of

CCS Technology

2009‐2012 Phase I Technology development

Final Investment Decision

• Reduce economic and technical risks• Enhance experience and technical support

TWO‐PHASES APPROACH



www.compostillaproject.eu

MORE INFO


http://www.compostillaproject.eu/


ContentContent


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CIUDEN’s R&D Experimental facilities:

• Simulation of a wide variety of operational modes and fuels• Maximum efficiency in view of schedule and budget• Small as possible but large enough to be scalable

Strenghts:

• Full integrated process• Flexibility and high experimental capabilities:

• Several burners to investigate flame interaction• PC-CFB comparison (20 + 30 MWth

)• Wide range of fuels: anthracites, bit, sub-bit, pet coke, biomass

• Public R&D institution open for collaboration

Concluding remarksConcluding remarks


Thank youThank youMonica Lupion

External Affairs Director Fundacion Ciudad de la Energia CIUDEN

[email protected]

mailto:[email protected]

Oxidant Preparation Diagram

deSOx

Coal

O2

Air

to

CFB

CB1

CB2

CB3

IDF

FGR2

FGR1

90‐215ºC

30% max

300‐330ºC

40% max

300‐330ºC

70% max

CombustionFlue

Gases

R&D Activities - University of Newcastle · 2014-03-13 · Fundación Ciudad de la Energía...

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