hydrocarbon utilization

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Plasma Reforming of Carbon Oxides Robert Geiger, Sreekar Parami, David Staack Texas A&M, Mechanical Engineering

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Plasma Reforming of Carbon Oxides Robert Geiger, Sreekar Parami , David Staack Texas A&M, Mechanical Engineering . Hydrocarbon Utilization. CO2. Plasma Dissociation . H=393.5 kJ/mol CO2 H=241 kJ/mol H2O. CO. H2O. Combustion. Combustion Fischer Tropsch Ethanol Hydrogen. CO. H2. - PowerPoint PPT Presentation

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Page 1: Hydrocarbon Utilization

Plasma Reforming of Carbon OxidesRobert Geiger, Sreekar Parami, David Staack

Texas A&M, Mechanical Engineering

 

Page 2: Hydrocarbon Utilization

Hydrocarbon Utilization

CH4 (CxHy)

• Combustion• Fischer Tropsch• Ethanol• Hydrogen

H=393.5 kJ/mol CO2H=241 kJ/mol H2O

H=110 kJ/mol CO2

CO2

H2O

CO H2

CO

1/2

Petrochemicals Higher HydrocarbonsCarbon Oxide Polymers

(Matthias Ballauff, et. al Angew. Chem. Int. Ed. 2004, 43)

Combu

stion

Partial Combustion

Upgrading

Plasma

Polymerization

Plasma Dissociation

Page 3: Hydrocarbon Utilization

Experimental SetupPower Supply:• Vmax ~ 10 kV• Imax ~ 40 mA• Freq ~ 25 – 30 kHz• P ~ 40W-150W

Page 4: Hydrocarbon Utilization

DBD Reactor

Color Variations

Page 5: Hydrocarbon Utilization

Deposition Rate

Page 6: Hydrocarbon Utilization

Increasing FlowFlow appears to change power density distribution

180 sccm 870 sccm 1700 sccm

~ 30W ~50W ~100W

Increasing PowerPower increases deposition rate and film darkness

Gas temperature and surface temperature do not cause the different film colors.

Page 7: Hydrocarbon Utilization

FTIR – Comparison with High Pressure Film

(High Pressure Film FTIR data taken from: Lipp M J et al 2005 Nat. Mater. 4 211)

Page 8: Hydrocarbon Utilization

Film Properties

• C:O ~ 1.5 - 3.5 (XPS)• Solubility

• Water (Hydrates)• Insoluble

• Acetone• Ethanol

Solubility allows for spin coating and layer by layer film growth

Before After

Hydration

C:O ~ 1.9 1.7

Page 9: Hydrocarbon Utilization

Kinetic Model in Development

Still need to add• CO* reactions• C(s) reactions• Surface reactions

McTaggart FK PIasma Chemistry in Electrical Discharges (1967)

Proposed Mechanism for C3O3 Polymer Formation

Simulation

Kinetic Model of Carbon Monoxide Plasma

Page 10: Hydrocarbon Utilization

Emission Spectroscopy

471.5 472 472.5 473 473.5 474 474.50

0.5

1

wavelength (nm)

Inte

nsity

(A.U

.)

Trot = 408K

Tvib = 1962K

FWHM = 0.271nm

RMSE = 1.66%

ExperModel

C2 Swan Fit

Page 11: Hydrocarbon Utilization

Future Work• CO Plasma

– Determine the polymer structures (NMR) and chain length– Characterize polymers and determine their properties– Energy Balances – Complete the kinetic model and compare with experimental– Determine optimum production parameters

• CO2 Plasma– Optical Emmsion for gas temperature and temperature

gradients– Optimize systems

• Residence times• Surface to volume ratios• Specific input power• Power supply efficiencies

– Compare Systems

Page 12: Hydrocarbon Utilization

Conclusion• CO Plasma

– Interesting films can be formed as fast as 1 mg/min at 50W with solely carbon and oxygen atoms

– These films appear similar in structure to high pressure CO polymers not C3O2

– Increased power darkens the film and increases deposition rate

– Color changes do not alter the FTIR– A kinetic model in under development– The C2 swan, CO angstrom and CO Herzberg bands

enables temperature measurements in the visible range• CO2 Plasma

– Micro-glow discharge showed best results– High power density and rapid quenching are thought to be

desirable

Page 13: Hydrocarbon Utilization

References• Lipp M J et al 2005 Nat. Mater. 4 211• V V Brazhkin 2006 J. Phys.: Condens. Matter 18 9643• McTaggart FK PIasma Chemistry in Electrical Discharges

(1967)• P.C.Cosby, J. Chem. Phys. 98,9560(1993).• K.M.D’Amico,and A.L.S.Smith, J.Phys.D: Appl. Phys. 10,261

(1977)

Email: [email protected]