Table. 1 Details of cell setups reported in the literature for alkaline water electrolysis with a Zirfon separator and PGM free electrodes

From: Proton exchange membrane-like alkaline water electrolysis using flow-engineered three-dimensional electrodes

Ref.

KOH (wt.%)

Temp. (°C)

Cathode

Anode

Flow (ml·min−1)

Electrode area (cm2)

Transport/contact layer

This work

30%

70

Ni 450 μm foam

Ni 450 μm foam

350–1600

4

3000 μm Ni foam

This work

30%

70

Raney-Ni 450 μm foam

Raney-Ni 450 μm foam

350–1600

4

3000 μm Ni foam

32

30%

80

Raney Ni perforated plates

Raney Ni perforated plates

50

25

Flow field (shape N/S)

70

5%a

80

Stainless steel expanded mesh

Stainless steel expanded mesh

80

10

Serpentine flow field

31

30%

80b

Ni plate with channels

Ni plate with channels

0.048–288

19.63

Flow field (shape N/S)

19

24%

80

Ni foam

Ni perforated sheet

50

25

Flow field (shape N/S)

19

24%

80

Raney Ni perforated sheet

Raney Ni perforated sheet

50

25

Flow field (shape N/S)

33,34

30%

80

Ni foam

Ni foam

450

34.56

Serpentine flow field

33,34

30%

80

Raney Ni foam

NiFe-LDH foam

450

34.56

Serpentine flow field

61

26% (6 M)

70

Raney Ni multimesh

Raney Ni multimesh

Unknown

4

Knitted Ni wire

71

N/S

80

Ni foam

Ni foam

100

5

Serpentine flow field

72

30%

80

Raney Ni foam

NiFe-LDH foam

400

36

Ni foam

73

30%

80

Porous Raney Ni

Porous NiFe-LDH

400

25

Serpentine flow field

24

26% (6 M)

80

Ni foam

Ni foam

50

4

Serpentine flow field

74

30%

80

Raney nickel foam

NiFe-LDH foam

1000

34.56

Porous transport layer

  1. N/S not specified
  2. aNaOH as electrolyte
  3. b30 bar of pressure