Hydrogen Technology - Fewer References Flashcards

1
Q

Physisorption

Broom and Book 2014

A

Isosteric Enthalpy of Adsorption. Hydrogen Uptake

See 7/7

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2
Q

Physisorption

Ramirez-Vidal et al 2021

A

Gravimetric measure of absolute adsorption. Pore width Hydrogen density

See 7/10

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3
Q

Hydrogen Storage - Porous Materials

Jankowska et al 1991

A

Porous Carbon Turbostratic structure

See 7/21

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4
Q

Yang Xia Mokaya 2007

A

Carbon Zeolitic Framework

See 7/22

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5
Q

Rosi et al 2003

MOF with…

A

Metal Organic Framework with Zinc Oxide and Organic molecular building blocks

See 7/27

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6
Q

Explain Metal Organic Framework

Broom et al 2016

A

Small Particles –> High Surface Area –> Higher Hydrogen wt%

But higher gravimetric density –> lower volumetric density

See 7/31

Gravimetric density above 5.5%
Volumetric density above 40g/L
Use 77K for Liquid Nitrogen.
20,000 MOFs in Cambridge structural database

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7
Q

Broom et al 2019

A

Stepped adsorption isotherms with flexible material

See 7/32

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8
Q

Ahluwala and Peng 2009

A

Cryogenic Adsorption

See 7/39

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9
Q

Thomas 2007 and Sandrock 2008

Graph for Temperature and Weight Capacity

A

Sweet Spot with High wt% and close to ambient temperature

See 7/12 - Porous Materials (and other places)

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10
Q

MgH2 Ball Milling to 20nm

Hirscher 2003

A

Leads to smaller grain size and more grain boundaries. Hydrogen goes in (and comes out) much quicker and at lower temperature.
Smaller size ball milling leads to agglomoration.

See 6/53

Also Niemann (with Catalyst) and Hanada over 5% H wt%

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11
Q

Destabilising MgH2

Zlotea et al 2015

A

Nanoparticles for Hydrogen storage. Chemical crystalisation. Embedded in microporous carbon. Under 2nm particles.
Lower temperatures

See 6/63

Also Orimo and Fuji - Binary phases of Mg with transition metals

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12
Q

Complex Hydrides

Vajo et al 2007

A

Complex Hydrides. Lithium Borohydride. Destabilised intermediary with MgH2.
170 degrees 1 bar.
Reversible.

See A/26

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13
Q

Separation: Grashoff et al 1983

Remember the curled up strip picture?

A

Paladium membrane for hydrogen separation.
Incorporate silver to reduce embrittlement.

See 8/17

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14
Q

Weight of energy storage systems to take a car 500 km

Eberle et al 2009

A

Compressed 700bar
6kg (170L) Hydrogen
125kg (260L) system

Compared with ICE
33kg (37L) fuel
43kg (46L) system

Compared with Lithium
540kg(360L) “fuel” - batteries
830kg(670L) system

See 3/2

Weights and Volumes. ICE Fuel system considerably smaller. Under 50kg?

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15
Q

PEM Fuel Cell - Catalyst functions

A
  1. Gas transmission and distribution to electrolyte boundary layer
  2. Electric current flow
  3. Water (moisture) extraction/transport

Maybe some Oxygen related activity

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16
Q

Fuel Cell vehicle transmission system
Hu and Egardt 2015

“Who has the heart to show tyres on their picture?”

A

Hydrogen tank
PEM? Fuel Cell
Energy Storage (battery)
Auxilliaries
Electric Motor
Transmission

See 3/3. Start with Transmission and work backwards

17
Q

Automotive PEM FC layout
Hu et al 2015

A

Compressor and Humidifier for air.
Control valve for Hydrogen (tank)
Cooling circuit
Recirculation and purge
STACK

Just the PEM - See Hu and Eghardt for Complete System

See 1/33

18
Q

Hydrogen storage mean distances between molecules/atoms

A

1bar ambient: 3.3nm
350bar ambient: 0.54nm
700bar ambient: 0.45nm
Liquid 20K: 0.36nm
Metal hydrides: 0.21nm (atoms) - Westlake

See 3/50 and ??

19
Q

Hydrogen Production techniques

Holladay et al 2009

A

SMR 70-85% Efficient. Commercial
Alkaline electrolyser 50-60%. Commercial
Biomass gasification 35-50%. Commercial
PEM 55-70%. Near term.

See 2/13

20
Q

Current Production and Prices

Vidal 2022

A

Current Hydrogen production:
48% Natural gas
30% Oil
18% Coal
4% Electrolysis and other!

Prices:
Wind: above $4
Solar electrolysis: near $4/kg

Onshore wind electrolysis: under $3/kg

NUCLEAR Electrolysis $2
SMR (with or without CCS): Under $2

21
Q

SMR methods

Enayatizade et al 2019
Shirasaki 2009

A
  1. Desulpherise
  2. Add Steam
  3. Add Heat - Reformer
  4. Shift Conversion (remove water)
  5. PSA Pressure Swing Adsorption - purification

Reforming: CH4 + H2O –> 3H2 + CO (880 °C)
Water Gas Shift: CO + H2O <–> CO2 + H2 (~ 300 °C)

880 = 10 Back to the Futures
300 = Battle of Badr?

Shirasaki 2009 - SMR Membrane Reactor = TUBE with Pd

22
Q

Pressure Swing Adsorption

Cortes et al 2009

A

Passing a gas mixture through a high surface area adsorbent with the ability to adsorb impurity gases

Easily adsorbed to non adsorbed
(eg C3H6) – CO, CH4 – O2 – H2

23
Q

Metal Hydrides

Lototskyy et al 2014

A

Reversible Adsorption/Desorption
Metal or Alloy or Intermetallic Compound (LaNi5 TiFe etc)
and
Structure of Hydride: Parent alloy, Change in crystal volume

See 6/7 and 6/24

24
Q

Metal Hydride
Physics

Schlapbach 1988

A

Hydrogen disocciation and Potential Energy

See 6/10

25
**Lots from Metal Hydrides** | Züttel 2003
Van't Hoff equation LaNi5 and FeTi Reversible! Thomas Sandrock Density graph. High G, v low temperatures | See 6/23 (with Schlapbach 2001) and 6/25
26
Various Heat Exchanger concepts | Broom et al 2016 - Not the graph
1. Conventional Tube Fin 2. Aluminium Honeycomb 3. Carbon Foam 4. Aluminium Foam 5. Compacted and Augments MOF 6. Micro Channel Heat Exchanger (looks like Shivangi's PCM frame) | (Fish, Bee, 2 seas, Frame getting squashed, channel tunnel for ants)