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
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
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
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)
- Oxidation: H2 -> 2H+ + 2e-
- electrons travel through the external circuit & power electrical devices
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
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
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
- Polymer Electrolyte Fuel Cell PEFC
- Ceramic type
- Proton Ceramic Fuel Cell PCFC
- Solid Oxide Fuel Cell SOFC
- state of the art for stationary application
8
Q
Fuel Cell efficiency
A
𝜂 = output electrical energy / theoretical energy released upon full fuel combustion (= Heating value of fuel)
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
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))
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
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
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
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
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
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