Introduction & Motivation Flashcards

1
Q

Hydrogen production

A
  • Needs to be sourced from low-emission intense sources to be favourable in life cycle balance -> Green Hydrogen
  • has low volumetric density -> needs to be liquified (-253°C)
  • Electrolysis
  • Produced electrochemically from water & renewable electricity; expected to be dominant source
  • through nuclear energy
    • low CO2 Emissions
    • medium environmental impact
    • high cleanliness level of H2
  • through mixture of sources (FF & RE)
    • low CO2 Emissions
    • medium environmental impact
    • high cleanliness level of H2
  • through renewable sources
    • low CO2 Emissions
    • low environmental impact
    • high cleanliness level of H2
  • Thermochemical water splitting
  • produced thermochemical with help of a redox material directly employing concentrated sunlight
    • produced by concentrated solar energy
    • low CO2 Emissions
    • low environmental impact
    • high cleanliness level of H2
  • -> both energy intensive processes
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2
Q

location dependency of H2 production

A
  • renewable electricity generation at scale required
    • highest potential for cost-effectiveness in high wind/solar regions
    • capacity needs to be drastically increased -> rising demand
  • location of hydrogen use may be characterised by non-ideal production conditions -> logistical efforts of supply & distribution
  • fundamentally different properties, production pathways & supply chains -> radical developments required
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3
Q

benefits of Hydrogen fuels

A
  • short & efficient process chain -> high production efficiency
  • lower minimum fuel selling price
  • lower global warming potential -> improved local air quality through reduced high altitude climate impact
  • opportunity for reduced high altitude climate impact -> improved local air quality
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4
Q

Fuel Cell basics

A
  • type of energy converter, allows direct harvest of chemical energy stored in a fuel through an electrochemical process
  • works through Redox reaction with fuel & Oxygen:
    • Oxidation: H2 -> 2H+ + 2e-
      • Hydrogen Oxidation Reaction (HOR)
    • Reduction: 0.5 O2 + 2H+ -> H2O
      • Oxygen Reduction Reaction (ORR)
  • electrons travel through the external circuit & power electrical devices
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5
Q

Electrochemical conversion in fuel cells

A
  • chemical Energy -> electrical energy -> mechanical energy
  • high exergy content in electrical energy
  • practically through limited mass transport, sluggish kinetics lead to a significant inner resistance of the fuel cell
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6
Q

Fuel cells in Aviation

A
  • very challenging application
  • High specific power requirements
  • High durability requirements
  • large system size
  • drastic change of ambient conditions
  • -> interdisciplinary skills required for optimisation
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7
Q

Kinds of Fuel Cells

A
  • Polymeric types
    • Polymer Electrolyte Fuel Cell PEFC
      • state of the art for mobile applications (esp cars)
    • High Temperature Polymer Electrolyte Fuel Cell HT-PEFC
  • Ceramic type
    • Proton Ceramic Fuel Cell PCFC
    • Solid Oxide Fuel Cell SOFC
      • state of the art for stationary application
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8
Q

Fuel Cell efficiency

A

𝜂 = output electrical energy / theoretical energy released upon full fuel combustion (= Heating value of fuel)

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9
Q

Polymer Electrolyte Fuel Cell

A
  • 𝜂 ≈ 80%, with HHV
  • operating temperature 60 - 95 °C, typically 80°C
  • load response < 1s
  • operating pressure range: 1-3 bar
  • no fuel flexibility
  • high technological maturity
  • membrane made of perfluorosulfonic acid PFSA
  • Challenges
    • requires humidification/water management
    • significant amount of heat dissipated for low ΔT to ambient
    • use of expensive Nobel-metal catalysts bc of sluggish kinetics at 80°C
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10
Q

High-Temperature Polymer Electrolyte Fuel Cell

A
  • 𝜂 ≈ 77-79%, with HHV
  • operating temperature: 100-220°C
  • intermediate technological maturity
  • rest like PEFC
  • Challenges
    • durability limited due to high corrosion rates at the higher temperatures
    • limited power densities observed
    • limitations of membranes (made of Phosphoric Acid-Doped Polybenzimidazole (PA-PBI))
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11
Q

Proton Conducting Ceramic Fuel Cell

A
  • 𝜂 ≈ 68-74%, with HHV
  • operating temperature 450 - 700 °C
  • load response ≈ 10s to minutes
  • operating pressure range: 1-3 bar
  • fuel flexibility
  • low technological maturity
  • membrane of Protonic ceramic conductors
  • Challenges
    • high mass/ion-transport associated resistances within the cell -> limited performance
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12
Q

Solide Oxide Fuel Cell

A
  • 𝜂 ≈ 60-70%, with HHV
  • operating temperature 600 - 1200 °C
  • load response ≈ 10s to minutes
  • operating pressure range: 1-8 bar
  • fuel flexibility
  • intermediate technological maturity
  • membrane of Protonic ceramic conductors
  • Challenges
    • sealing at high temperatures
    • thermo-mechanical strain due to different thermal expansion behaviours components -> degradation
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13
Q

Trade offs of Ceramic FC in Mobile applications

A
  • comparatively high fuel efficiency
    • less heat to be dissipated & at higher ΔT to ambient
  • thermal management facilitated
  • comparatively low stack specific power
  • less developed for mobile applications, due to
    • slow load response
    • issues with thermo-mechanical degradation
    • harsher conditions for corrosion & sealing materials
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14
Q

Fuel cell system

A
  • consists of a large number of individual cells
  • connected in series to create stacks -> I = I1; U = ∑Un (balance required)
  • thermal management
  • water management
  • reactant supply
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15
Q

stack performance assessment & enhancement

A
  • properties to govern FC performance
    • electrochemical reactions
    • mass transfer
    • ionic transport
    • electronic transport
    • water management
    • thermal management
  • optimising
    • research to understand processes
    • research & engineering the materials involved
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16
Q

Batteries in Aeronautic applications

A
  • achievable power & energy stored coupled (decoupled for FC)
  • energy stored in battery limits range (FC only converts)
  • active material amount is range limiting factor (for FC hydrogen limits range)
  • aircraft carries both redox partners (only one for FC)
  • aircraft mass does not change during flight (gets lighter for FC)
  • fast response to transient loads
  • achievable efficiency ≈ 95% (≈40-65% for FC)
17
Q

Disadvantages of batteries

A
  • heavy
  • large
  • extensive thermal management needed for them not to over-/underheat
  • not suitable for large aircraft of long transports (only with hybrid-electric approaches investigated)
18
Q

Disadvantages of Hybrid-Electric approaches

A
  • stark range constraints for hybridisation bc of limitations in specific energy of batteries (true even for mild degrees of hybridisaiton)
  • final impact will largely depend on battery development
  • currently, adequate battery performance not in reach
19
Q

Take away message A)

A
  • aviation requires many measures to achieve net-zero carbon emissions
  • green hydrogen as alt. energy carrier
    - high emission reduction
    - used in aviation & other sectors
    - hydrogen as “energy vector”
  • LH2 & kerosene properties differ fundamentally
    - challenges in aircraft design
    - infrastructure adaptions required
  • FC covers energy stored in H2 electrochemically with comp. high efficiency
    - av. FC tech differ in tech. maturity, suitable operating conditions & performance
    - FC fundamentally differ from Batteries
  • aviation represents a challenging field of application for FC
    - innovation & development on cell, system & aircraft level required