Microcombustion: Catalyzed Partial Oxidation of Ethanol in a Heated Nickel Microtube - PowerPoint PPT Presentation

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Microcombustion: Catalyzed Partial Oxidation of Ethanol in a Heated Nickel Microtube

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Title: Microcombustion: Catalyzed Partial Oxidation of Ethanol in a Heated Nickel Microtube


1
Microcombustion Catalyzed Partial Oxidation of
Ethanol in a Heated Nickel Microtube
  • Final Presentation
  • Peter Galie
  • Princeton University
  • Principal Investigator Dr. Steven J. Schneider
  • Glenn Research Center
  • Cleveland, Ohio

2
Introduction
  • The Necessity for Micro-scale Combustors
  • i. MEMS/ Micro-Spacecraft (20-100 kg)
  • ii. Nano-Spacecraft (10-20 kg)
  • iii. Ignition for large-scale rockets

3
Benefits of Micro-scale
  • Size, Weight
  • Currently costs 10,000/kg to put an object
    into Lower Earth Orbit.
  • Versatility
  • Small spacecraft can perform a variety of
    different missions, from global
  • surveying to disaster
  • monitoring of other
  • spacecraft.

4
Limitations of Micro-Combustion
  • As the size of combustion chamber decreases, the
    surface area to volume ratio increases. Heat
    release rate scales with volume, while heat loss
    rate scales with surface areas. Thus, at high
    surface area to volume ratios, heat loss
    dominates.
  • The quenching diameter, the critical distance
    below which a flame cannot propagate and
    combustion is impossible.

5
Catalyzed Micro-Combustion
  • Surface Catalysis
  • The use of a heated catalyst such as platinum
    or palladium can aid in the chemical combustion
    of hydrogen and oxygen as presented in studies by
    Dr. Schneider of NASA and Professor Sung of Case
    Western.

(C. Sung)
6
Why Ethanol?
  • Steam Reforming of 100 Proof Ethanol
  • C2H5OH H2O ? 2CO 4H2
  • Nickel serves as a good surface catalyst for this
    reaction. Performs like platinum or palladium,
    but MUCH cheaper.
  • Ethanol contains more energy per unit mass than
    most other alternative fuels. It is derived
    through biological processes, NOT using fossil
    fuels.
  • Non-toxic

7
Non-Toxic is a RELATIVE term
8
The Initial Experimental Apparatus

(Schneider)
9
Components of the Apparatus
Inlet Thermocouple
Ethanol Inlet
Inlet Pressure Transducer
Inside-Boiler Thermocouple
Boiler Thermocouple
Tube Thermocouple Connections
10
Components of the Apparatus
Digital Controller Input
Bleed Valve
11
Components of the Apparatus
to the Analyzer
Exhaust Pressure Transducer
Electrical Heating Tab
750 sccm N2 Purge (Large flow rate needed for
successful Gas Analyzer Operation)
Voltage across tube
12
Experimental Results
  • Variables
  • Flow Rate, Temperature
  • Measurements
  • Temperature Heater, Inside, Outside
    Hotplate, Inlet to tube, Microtube 1,2, and
    3.
  • Pressure Inlet pressure, Outlet pressure
  • Gas composition HCs, CO, CO2, H2
  • Voltage Power Source, Across tube
  • Flow Rate Nitrogen Purge, Ethanol Flow

LabView
13
Flow Analysis
  • Possibility of Flow Choking, Details of Chemical
    Kinetics calculated by PLUG Component of ChemKin
  • Rayleigh Flow Heat Flux
  • Fanno Flow Friction
  • Hugonoit Flow Pressure Density

14
ChemKin Modeling
  • Ethanol steam reforming chemical kinetics has NOT
    been well studied. Solution? - Model methane on
    nickel as an approximation.

15
Initial Experiment (6/22) Results
  • Chemical Reaction C2H5OH H2O ? 2CO 4H2
  • So we expect the rate of hydrogen production to
    be twice that of carbon monoxide.
  • Moreover, we should see a steep decrease in the
    amount of ethanol analyzed.

16
Initial Experiment (6/22) Results
17
Catalyst Activation Temperature
  • Nickel must reach a certain temperature before it
    can be activated to catalyze the ethanol
    reformation.
  • Looking at the previous graph, one can see that
    the activation temperature is approximately 800
    oF

18
Anomalous Result
  • There was a significant unexpected result.

19
Possible Causes of Anomaly
  • Condensation of Vaporized 100 proof Ethanol

20
Possible Causes of Anomaly
  • Heat Transfer The heat dissipates very quickly
    due to the small diameter of the highly
    conductive copper tubing. Simplified Equations

21
Possible Causes of Anomaly
  • Heat Transfer Analysis Assuming 50 degree
    Fahrenheit difference between vapor and tube
    wall.

22
Midterm Status
  • The ethanol reforming process is an endothermic
    reaction. It cannot sustain itself without
    constant addition of power.
  • Through the addition of gaseous oxygen (GOX), the
    hydrogen from the ethanol could react with the
    oxygen to produce a highly exothermic reaction.
  • This could lead to sustainability, or the heat
    could be used to expand the products through a
    small nozzle, creating a mini-thruster.

23
Changes Made to Apparatus
Heater Tape
24
Changes Made to Apparatus
Oxygen to plenum, then to microtube
Oxygen from Flow Controller
Oxygen to Atmosphere
  • Three-Way Bypass Valve

25
GOX Addition Failure (7/20)
  • Ethanol Flow controller became very instable at
    onset of the test. A large flow passed through
    the tube before resistive heating. This
    saturated the flow analyzer with hydrocarbons.
    Eventually, the tube broke due to the thermal
    stress, before oxygen could be added.
  • In other words this was a BAD day

26
Initial GOX Addition (7/22)
  • First Oxygen Addition
  • Large Temperature Decrease. Catalyst Activation.
    Rapid Deactivation

27
Initial GOX Addition (7/22)
  • Second Oxygen Addition
  • -gt Insignificant Change in Molar Ratios

28
Initial GOX Addition (7/22)
  • Increased Flow Rates
  • -gt Mixing Ratios were increased from 0 to 0.4
  • -gt Brief Periods of Surface Catalysis

29
Initial GOX Addition (7/22)
  • Unexpected Pressure Rise (..again)

30
Initial GOX Addition (7/22)
  • Vacuum Conditions
  • -gt Indicated a large hole inside the microtube.
    Suspicions were confirmed.

31
Initial GOX Addition (7/22)
  • Chemkin Predicted the following..

32
Secondary GOX Addition (7/27)
  • Ethanol Instability
  • -gt Interesting results after the experiment

33
Secondary GOX Addition (7/27)
  • Carbon Soot Formation

34
Support of our Conclusion
  • Reduce Temperature, Reduce Proof
  • Steam Reforming of 75 Proof Ethanol

35
Support of Sooting Theory
  • ChemKin Results

36
Can we solve the Sooting problem?
  • 75 Proof, Low Temperatures
  • What does ChemKin think?

37
Micro-catalyzed EthanolSteam Reforming (7/28)
  • Results

38
Micro-catalyzed EthanolSteam Reforming and
Combustion (7/28)
  • Results

39
Self-Sustainability Attempt (8/9/05)
40
Conclusions
  • Ethanol can in fact be made a dirty fuel.

41
Conclusions
  • The design of the combustor must be changed.
  • The microtube was used for computational
    simplicity. Perhaps a more robust design could
    promote full sustainability.

Swiss Roll?
42
Conclusions
  • BUT!
  • .. under the right conditions, a robust steam
    reformer and combustor can be constructed using
    nickel-catalyzed ethanol as a fuel source.

43
Acknowledgements
  • The New Jersey Space Grant
  • The NASA Academy
  • My Principal Investigator
  • Dr. Steve Schneider
  • Branch Chief
  • Dr. Rich Blech
  • Laboratory Colleague
  • Mr. Roger Scheman
  • Propulsion Engineers
  • Mr. Eric Pencil
  • Mr. Brian Reed
  • Dr. James Gilland
  • Office Colleagues
  • Mr. H.T. Huynh
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