17
Institute of Chemical Engineering: Future Energy Technology Prof. Hermann Hofbauer www.vt.tuwien.ac.at Chemical looping combustion using biomass as fuel Stefan Penthor , Tobias Pröll, Hermann Hofbauer 2nd Oxyfuel Combustion Conference, 12-16 September 2011, Yeppoon, Australia

Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

  • Upload
    others

  • View
    2

  • Download
    0

Embed Size (px)

Citation preview

Page 1: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

Institute of Chemical Engineering: Future Energy Technology Prof. Hermann Hofbauer www.vt.tuwien.ac.at

Chemical looping combustion using biomass as fuel Stefan Penthor, Tobias Pröll, Hermann Hofbauer

2nd Oxyfuel Combustion Conference, 12-16 September 2011, Yeppoon, Australia

Page 2: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

Outline

• Introduction

• Challenges and why biomass

• Solutions

• Modeling

• Results

• Conclusion/Outlook

Page 3: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

What is CLC?

Cooling/

Condensation

Air

Air Reactor

(AR)

Fuel Reactor

(FR)

MeOx-1

MeOx N2, (O2) CO2, (H2O)

H2O

CO2

Steam

Solid Fuel

Unique potential for CCS - air and fuel are never mixed!

Page 4: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

Challenges • Decomposition of fuel

• Conversion of combustible gas species

• Avoiding loss of carbon to air reactor

• Separating ash from oxygen carrier

• Finding suitable oxygen carrier

• Finding suitable reactor concept

Objectives

Page 5: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

Why biomass?

Petroleum coke

South African coal

Woody biomass

Volatiles [%] 10 21.6 80

Moisture [%] 8 8.3 25

Ash [%] 0.5 15.9 1.5

• Reactive char (compared to coal)

• Carbon neutral, low sulfur

• Below zero emission

• Stopover to coal

Page 6: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

Solutions

Page 7: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

Page 8: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

0

100

200

300

400

500

600

700

800

900

1000

1100

0 100 200 300

heig

ht [m

m]

pressure gradient [mbar/m]

0

100

200

300

400

500

600

700

800

900

1000

1100

0 10 20 30 40 50

heig

ht [m

m]

pressure drop [mbar]

Cold flow model tests

Schmid J.C., et al., Int. Conference on Polygeneration Strategies, 2011

Page 9: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

Modeling

Page 10: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

• Mass & energy balance

• Basic char gasification kinetics

• Chemical equilibrium for CO and H2 oxidation

• Solids segregation

Modeling approach

Page 11: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

Solids segregation

φi=mi,out,top

mi,out,bottom i=OC, Ash, Char

OC

AshSolids

Char

Page 12: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

First results

Page 13: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

• Pth = 1 MW

• Ilmenite as oxygen carrier

• • = 1.2

• Steam/Carbon = 0.5

• • OC = 0.05

• • Ash = 0.2

• • Char = 0.1

• •Char = 9 - 20 s

• TLLS = 950 C

Base case

Page 14: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

1

2

3

4

5

6

7

8

900 1000 1100

Reac

tion

Zone

[-]

Temperature [°C]

• TAR = 1015 C

• • sep, CO2 = 92.0 %

• Ash accumulation:

• xAsh,ILS = 37.4 %

• xAsh,LLS = 13.1 %

Fuel feed

Base case

Page 15: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

0

10

20

30

40

0.05 0.15 0.25 0.35

Ash

co

nce

ntr

atio

n [w

t%]

• _Ash [-]

LLS @ 5kg/h OC make up

ILS @ 5kg/h OC make up

LLS @ 10kg/h OC make up

ILS @ 10kg/h OC make up

• Ash variation

Base case

Page 16: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

CLC using biomass as fuel Stefan Penthor

Institute of Chemical Engineering Future Energy Technology

Conclusions/Outlook

• Multistage CFB can be key to solid fuel CLC

• Gas-solid contact and residence time improved

• Selective ash removal possible

• Process model created, validation necessary

• Cold flow model testing

• Build 100 kW pilot plant

Page 17: Chemical looping combustion using biomass as fuel · (FR) MeO x-1 N 2, (O ) MeO x CO 2, (H 2 O) H 2 O CO 2 Steam Solid Fuel Unique potential for CCS - air and fuel are never mixed!

Institute of Chemical Engineering: Future Energy Technology Prof. Hermann Hofbauer www.vt.tuwien.ac.at

Thank you for your attention!

Contact: Stefan Penthor

[email protected] www.chemical-looping.at