Thermal Transpiration-Based Mesoscale / Microscale Combined Propulsion - PowerPoint PPT Presentation

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Thermal Transpiration-Based Mesoscale / Microscale Combined Propulsion

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... is 1/10 of aerogel thickness! Can stage pumps for higher compression ratios Aerogels Typical pore size 20 nm Low density (typ. 0.1 g/cm3) ... – PowerPoint PPT presentation

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Title: Thermal Transpiration-Based Mesoscale / Microscale Combined Propulsion


1
Thermal Transpiration-Based Mesoscale /
Microscale Combined Propulsion Power Generation
Devices
  • Francisco Ochoa, Craig Eastwood,
  • Jeongmin Ahn, Lars Sitzki, Paul RonneyDept. of
    Aerospace Mechanical EngineeringUniv. of
    Southern California, Los Angeles, CA
  • http//carambola.usc.edu/

2
Motivation - fuel-driven micro-propulsion systems
  • Hydrocarbon fuels have numerous advantages over
    batteries for energy storage
  • 100 X higher energy density
  • Much higher power / weight power / volume of
    engine
  • Nearly infinite shelf life
  • More constant voltage, no memory effect, instant
    recharge
  • Environmentally superior to disposable batteries

3
The challenge of micropropulsion
  • but converting fuel energy to thrust and/or
    electricity with a small device has been
    challenging
  • Many approaches use scaled-down macroscopic
    combustion engines, but may have problems with
  • Heat losses - flame quenching, unburned fuel CO
    emissions
  • Friction losses
  • Sealing, tolerances, manufacturing, assembly
  • Etc

4
Thermal transpiration for propulsion systems
  • Q How to produce gas pressurization (thus
    thrust) without mechanical compression (i.e.
    moving parts)?
  • A Thermal transpiration - occurs in narrow
    channels or pores with applied temperature
    gradient when Knudsen number 1
  • Kn ? mean free path ( 50 nm for air at STP) /
    channel or pore diameter (d)
  • First studied by Reynolds (1879) using porous
    stucco plates
  • Kinetic theory analysis supporting experiments
    by Knudsen (1901)

Reynolds (1879)
5
Modeling of thermal transpiration
  • Net flow is the difference between thermal creep
    at wall and pressure-driven return flow
  • Analysis by Vargo et al. (1999)
  • Zero-flow pressure rise (?Pno flow) increases
    with Kn but Mach (M) decreases as Kn increases
  • Max. pumping power M?P at Kn 1
  • Length of channel (L) affects M but not ?Pmax

6
Aerogels for thermal transpiration
  • Q How to reduce thermal power requirement for
    transpiration?
  • A Vargo et al. (1999) aerogels - very low
    thermal conductivity
  • Gold film electrical heater
  • Behavior similar to theoretical prediction for
    straight tubes whose length (L) is 1/10 of
    aerogel thickness!
  • Can stage pumps for higher compression ratios

7
Aerogels
  • Typical pore size 20 nm
  • Low density (typ. 0.1 g/cm3)
  • Thermal tolerance 500C
  • Thermal conductivity can be lower than
    interstitial gas!
  • Typically made by supercritical drying of silica
    gel using CO2 solvent

8
Fuel-driven jet engine with no moving parts
  • Q How to provide thermal power without electric
    heating as in Vargo et al.?
  • Answer catalytic combustion!
  • Can combine with nanoporous bismuth
    (thermoelectric material, Dunn et al., 2000) for
    combined power generation propulsion

9
Theoretical performance of aerogel jet engine
  • Can use usual propulsion relations to predict
    performance based on Vargo et al. model of
    thermal transpiration in aerogels
  • Non-dimensional TFSC of silica aerogel (k
    0.0171 W/mK) only 2x - 4x worse than theoretical
    performance predictions for commercial gas
    turbine engines

Except as noted Hydrocarbon-air, T1 300K, T2
600K, P1 1 atm, L 100 µm, d 100 nm
10
Theoretical performance of aerogel jet engine
  • Membrane thickness affects thrust but not
    pressure rise, specific thrust or efficiency
  • Performance (both power fuel economy) increases
    with temperature

Except as noted Hydrocarbon-air, T1 300K, T2
600K, P1 1 atm, L 100 µm, d 100 nm
11
Multi-stage pressurization
  • Multi-stage pressurization (much better
    propulsion performance) possible by integrating
    with Swiss roll heat exchanger / combustor

12
Feasibility testing
  • Simple (crude?) test fixture built
  • Electrical heating to date catalytic combustion
    testing starting
  • Conventionally machined commercial aerogel (L 4
    mm)

13
Feasibility testing
  • Performance 50 of theoretical predictions in
    terms of both flow and pressure (even with thick
    membrane no sealing of sides)

14
Really really preliminary ideal design
  • Airbreathing, single stage, TL 300K, TH 600K,
    ?P 0.042 atm, 5.1 W thermal power
  • Hydrocarbon fuel, thrust 3.1 mN, specific thrust
    0.36, ISP 2750 sec
  • With nanoporous Bi (ZT 0.39 300K lt T lt 400K)
    could generate 100 mW of power, but with 30
    less ISP 2x weight

15
Really really preliminary ideal design
  • Components
  • Nanoporous membrane 1 cm2 area, 100 µm thick,
    100 nm mean pore diameter, weight 0.00098 mN
  • Catalyst Pt, deposited directly on high-T side
    of membrane (no need for hi-T thermal guard), 1
    µm thick, weight 0.02 mN
  • Low-temperature thermal guard Magnesium
    ZK60A-T5 alloy, 50 µm thick for 4x stress safety
    factor, weight 0.089 mN (less if honeycomb
    limited by strength, not conductivity), k 120
    W/mK
  • Case nozzle 5 mm long, titanium 811 alloy, k
    6 W/mK, weight 0.114 mN for 4x stress safety
    factor hot-side radiative loss 4 even for
    ?aerogel 1
  • Ideal performance
  • Total weight 0.22 mN, Thrust/weight 14
  • Hover time of vehicle (engine fuel Ti alloy
    fuel tank, no payload) 2 hours flight time
    (lifting body, L/D 5) 10 hours

16
Other potential applications
  • Could eliminate need for pressurized propellant
    tanks - mass savings
  • ISP with N2H4 100 sec
  • Combined pump valve (no ?T, no flow)
  • Propellant pumping for other micropropulsion
    technologies
  • Microscale pumping for gas analysis, pneumatic
    accumulators, cooling of dense microelectronics,

Concept for co-pumping of non-reactive gas
17
USC contributions to microthermochemical systems
  • Identified flameless combustion in broad reaction
    zones in heat-recirculating burners
  • Stability of gas-phase catalytic modes
  • Tradeoffs between gas-phase catalytic
    combustion
  • Effect of equivalence ratio (independent of flame
    temperature) on catalytic combustion
  • Effect of wall thermal conductivity
  • Effect of heat losses in 3rd dimension
  • Importance of radiation in scale-down
  • Designs
  • Fin design for thermoelectric power generation
  • Use of SOFC in a Swiss roll
  • Catalytic combustion based thermal transpiration
    propulsion
  • Multi-stage thermal transpiration pumping using
    Swiss roll

18
Conclusions
  • Nanoporous materials have many potential
    applications for microthermochemical systems
  • Thermal transpiration
  • Insulation
  • Best non-vacuum insulation available
  • Probably best insulation per unit weight for
    atmospheric pressure applications
  • Thermoelectric power generation (nanoporous Bi)
  • Catalyst supports
  • Could form the basis of a micro/mesoscale
    jet/rocket engine with no moving parts
  • Aerogel MEMS fabrication development
  • at UCLA
  • NASA-sponsored joint USC/UCLA program
  • to start 10/1/03
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