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Institute of Chemical Engineering page 1 Achema 2012 Chemical Process Engineering Reaction Engineering & Combustion Reaction Engineering & Combustion Contact: [email protected]

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Page 1: Reaction Engineering & Combustion - TU Wien100 120 140 160 0 50 100 150 200 250 300 350 400 450 500 time [s] [ppm] NO HCN NH3 devolatilization char combustion Combustion Kinetics and

Institute of Chemical Engineering page 1Achema 2012

Chemical Process Engineering

Reaction Engineering & Combustion

Reaction Engineering & Combustion

Contact: [email protected]

Page 2: Reaction Engineering & Combustion - TU Wien100 120 140 160 0 50 100 150 200 250 300 350 400 450 500 time [s] [ppm] NO HCN NH3 devolatilization char combustion Combustion Kinetics and

Institute of Chemical Engineering page 2Achema 2012

Chemical Process Engineering

AIM:

Research (experimental and modelling) and lectures:

-) gas – solid flow

-) heat- and mass transfer

-) chemical reactions

for

-) reactor design

-) process development

-) process optimization

in the areas of

=> energy technology (combustion, devolatilization)

=> environment technology (NOx, SO2, CO2, CO, HCl, Asche)

=> metallurgical industry (iron ore reduction, blast furnace, sinter process)

=> chemical industry (oxy-chlorination, catalysis)

Reaction Engineering & Combustion

Page 3: Reaction Engineering & Combustion - TU Wien100 120 140 160 0 50 100 150 200 250 300 350 400 450 500 time [s] [ppm] NO HCN NH3 devolatilization char combustion Combustion Kinetics and

Institute of Chemical Engineering page 3Achema 2012

Chemical Process Engineering

Verweilzeit

Red

uktio

nsgr

ad

H2-reiches Reaktionsgas

CO-reiches Reaktionsgas

pressurized lab-scale reactor

partly converted particle

Reaction Kinetics at High Temperatures and High Pressures

Conversion with time

Page 4: Reaction Engineering & Combustion - TU Wien100 120 140 160 0 50 100 150 200 250 300 350 400 450 500 time [s] [ppm] NO HCN NH3 devolatilization char combustion Combustion Kinetics and

Institute of Chemical Engineering page 4Achema 2012

Chemical Process Engineering

Urban Mining, the City as Resource

lab-scale reactor

Page 5: Reaction Engineering & Combustion - TU Wien100 120 140 160 0 50 100 150 200 250 300 350 400 450 500 time [s] [ppm] NO HCN NH3 devolatilization char combustion Combustion Kinetics and

Institute of Chemical Engineering page 5Achema 2012

Chemical Process Engineering

Recovery of Phosphate from Sewage sludge ash

(Sewage sludge plant)

(Sewage sludge -dried)

(Sewage sludge ash)

Page 6: Reaction Engineering & Combustion - TU Wien100 120 140 160 0 50 100 150 200 250 300 350 400 450 500 time [s] [ppm] NO HCN NH3 devolatilization char combustion Combustion Kinetics and

Institute of Chemical Engineering page 6Achema 2012

Chemical Process Engineering

Thermo-chemical Energy Storage

lab-scale reactor

thermodynamics

Page 7: Reaction Engineering & Combustion - TU Wien100 120 140 160 0 50 100 150 200 250 300 350 400 450 500 time [s] [ppm] NO HCN NH3 devolatilization char combustion Combustion Kinetics and

Institute of Chemical Engineering page 7Achema 2012

Chemical Process Engineering

n‐heptane, n‐decane and iso‐octane

0,10

1,00

10,00

100,00

0,8 1 1,2 1,4 1,6

Igni

tion

Del

ay T

ime

[ms]

1000/T [1/K]

Ignition delay times PRF0

13.5 bar experiment 13.5 bar simulation

Global Reaction Mechanism for Ignition

Page 8: Reaction Engineering & Combustion - TU Wien100 120 140 160 0 50 100 150 200 250 300 350 400 450 500 time [s] [ppm] NO HCN NH3 devolatilization char combustion Combustion Kinetics and

Institute of Chemical Engineering page 8Achema 2012

Chemical Process Engineering

0

20

40

60

80

100

120

140

160

0 50 100 150 200 250 300 350 400 450 500

time [s]

[ppm

]

NO

HCN

NH3

devolatilization char combustion

Combustion Kinetics and Pollutants Formation

Fuels

lab-scale reactor

NO, HCN, NH3 formation

Page 9: Reaction Engineering & Combustion - TU Wien100 120 140 160 0 50 100 150 200 250 300 350 400 450 500 time [s] [ppm] NO HCN NH3 devolatilization char combustion Combustion Kinetics and

Institute of Chemical Engineering page 9Achema 2012

Chemical Process Engineering

Foto: Anlage Pecs

www.iea-fbc.org

Int. Energy Agency - Fluidized Bed Conversion Network

Page 10: Reaction Engineering & Combustion - TU Wien100 120 140 160 0 50 100 150 200 250 300 350 400 450 500 time [s] [ppm] NO HCN NH3 devolatilization char combustion Combustion Kinetics and

Institute of Chemical Engineering page 10Achema 2012

Chemical Process Engineering

Further information

ao.Univ.Prof. Dipl.-Ing. Dr. Franz WINTER

Email: [email protected]://www.vt.tuwien.ac.atTel.: +43 1 58801 166301FAX: +43 1 58801 16699