olga tar removal

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www.ecn.nl OLGA Flexible tar removal for high efficient production of clean heat & power as well as sustainable fuels & chemicals

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2009Chicago Olga Tar Removal

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Page 1: OLGA tar removal

www.ecn.nl

OLGA

Flexible tar removal for high efficient production of

clean heat & power as well as sustainable fuels & chemicals

Page 2: OLGA tar removal

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TCBiomass2009

September 16th 2009

Chicago

Content of the paper

• The tar problem

• The OLGA technology

• The development

Step 1: Demonstration of high-efficient production of clean heat and power

Step 2: Developing high-efficient production of sustainable fuels & chemicals

Step 3: Demonstrating the flexibility of the OLGA tar removal technology

• Commercial gasification projects

• Conclusions and outlook

• References

Environmental progress & sustainable energy / October 2009 / Volume 28 / Number 3

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TCBiomass2009

September 16th 2009

Chicago

Content of the presentation

• The tar problem

• The OLGA technology

• The development

Step 1: Demonstration of high-efficient production of clean heat and power

Step 2: Developing high-efficient production of sustainable fuels & chemicals

Step 3: Demonstrating the flexibility of the OLGA tar removal technology

• Commercial gasification projects

• Conclusions and outlook

• References

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TCBiomass2009

September 16th 2009

Chicago

Excluded from the presentation

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TCBiomass2009

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Chicago

The OLGA technology: philosophy

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TCBiomass2009

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Chicago

The OLGA technology: principle

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TCBiomass2009

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Chicago

Step 1: Heat and power

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TCBiomass2009

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Step 1: Heat and power

Dioxins

‘Dioxins’ is a common name for

a group of 210 compoundsisomers of

polychlorinated-dibenzo-para-dioxins

and -dibenzofurans (PCDD/Fs)

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TCBiomass2009

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Chicago

Step 1: Heat and power

O

O

ClCl

ClCl

O

1

2

3

4 6

7

8

9

1

2

3

4 6

7

8

9

polychlorinated-dibenzo-para-dioxins

and -dibenzofurans (PCDD/Fs)

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TCBiomass2009

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Chicago

Step 1: Heat and power

• dioxins are toxic at low concentrations

(already at 0.000000001 g/m3)

• I-TEQ = International Toxicity Equivalent

= measure for dioxins toxicity

• European emission limit (flue) =

0.1 ng I-TEQ/mn3 (at 6% O2 in flue gas)

Viktor Yushchenko (Ukraine)

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Chicago

Step 1: Heat and power

• carbon source

– residual carbon on ash

– gas-phase Products of Incomplete Combustion (PICs, TAR)

– (fly) ash/char-adsorbed PICs

• elevated temperature

– 700-900°C gas-phase reactions

– 250-400°C catalytic reactions (surface = wall/ash catalysed)

• chlorine source

– organic/inorganic chlorides

– free Cl2 (e.g. Deacon’s reaction from HCl)

Only a (proper) combination of all three factors yields dioxins...

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Step 1: Heat and power

0

1

2

3

4

5

6

7

8

9

10

RDF A 725°C RDF B 725 °C sewage sludge

750°C

RDF A 820°C sewage sludge

850°C

clean wood

pellets 850°C

PC

DD

/Fs

co

nc

en

tra

tio

n [

ng

I-T

EQ

/m3

]

75 Presented concentrations = raw producer gas

Gasifier = air-blown, direct

Chlorine/ash-rich fuels = increased levels

High conversion temperature = low levels

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Step 1: Heat and power

0

0.05

0.1

0.15

0.2

0.25

0.3

0.35

0.4

0.45

raw prod. gas (upstream OLGA) clean prod. gas (downstream OLGA)

PC

DD

/Fs c

on

cen

trati

on

[n

g I

-TE

Q/m

3]

Fuel = clean wood pellets

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Chicago

Step 1: Heat and power

0

0.05

0.1

0.15

0.2

0.25

0.3

0.35

0.4

0.45

0.5

boiler (no OLGA) boiler (with OLGA) gas engine (with

OLGA)

gas turbine (with

OLGA)

PC

DD

co

nc

en

tra

tio

n [

ng

I-T

EQ

/m3

]

EU emission limit (flue gas):

0.1 ng I-TEQ/mn3 [@ 6% O2]

1.9

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Fischer-Tropsch diesel

Substitute Natural Gas (SNG)

Chemicals

Step 2: Sustainable fuels & chemicals

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Step 2: Sustainable fuels & chemicals

Component Downstream MILENA Downstream OLGA

CO vol% 30.1 30.6

H2 vol% 32.0 32.5

CO2 vol% 19.2 19.4

O2 vol% 0.0 0.0

CH4 vol% 12.2 12.4

N2+Ar vol% 0.1 0.1

C2H2 vol% 0.2 0.2

C2H4 vol% 3.9 3.9

C2H6 vol% 0.2 0.2

C6H6 vol% 1.0 0.5

C7H8 vol% 0.1 0.0

Tar g/mn3 52.1 0.2

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Step 3: Flexibility

WOB BFB at ECN

MILENA Indirect at ECN

BIVKIN CFB at ECN

MILENA Indirect at ECN

PRMe Fixed Bed at Moissannes

BIVKIN CFB in Portugal

MILENA Indirect at HVC

Note that existing lab and pilot

OLGA at ECN hardly changed!

Lab

Pilot

Commercial

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Step 3: Flexibility

High chlorine content together

with high amounts of PE/PP/PB/PS

RDF

Chicken manure (new project)

Formation of a unusual thermoplast

inbetween 150 and 200°C

Upstream chlorine removal applied

OLGA operation without problems

High ash content

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Step 3: Flexibility polar tar

non-polar tar

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Step 3: Flexibility

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Conclusions & outlook

The OLGA technology development started in 2001 and OLGA was

launched to the market by Dahlman in 2007

OLGA always showed to be a very efficient, flexible and reliable gas

cleaning technology. This accounts not only for tar removal, but also for

(dioxin) emission control

Although OLGA can be considered as proven technology for many

applications and downstream different gasifiers, for some applications

(e.g. low temperature gasification or bad feedstock) some additional

testing work on lab and pilot scale at ECN is advised and can be

performed though to ensure successful commercial operation

ECN continues its work on the sustainable production of fuels and

chemicals, with OLGA having shown to be successful as well as

efficient cleaning upstream processes for FT-diesel or SNG production

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References

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References

catalytic cracking

plasma

RPS and ESP

gasreip A to C

OLGA

the tar problem

solved though

remaining an

enduring challenge

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Chicago

Contact information

Robin Zwart

e: [email protected] PO Box 1

t: +31 224 56 4574 NL 1755 ZG Petten

w: www.ecn.nl the Netherlands

publications: www.ecn.nl/publications

fuel composition database: www.phyllis.nl

tar dew point calculator: www.thersites.nl

IEA bioenergy/gasification: www.ieatask33.org

Milena indirect gasifier: www.milenatechnology.com

OLGA tar removal: www.olgatechnology.com

SNG: www.biosng.com and www.biocng.com

Dahlman: www.dahlman.nl and www.renewableenergy.nl