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
Q

Lots from Metal Hydrides

Züttel 2003

A

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
Q

Various Heat Exchanger concepts

Broom et al 2016 - Not the graph

A
  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)