PEM electrolyzer model for Apros dynamic potentials
Transcript of PEM electrolyzer model for Apros dynamic potentials
![Page 1: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/1.jpg)
PEM electrolyzer model for Apros
Jari Pennanen / VTTLotta Kannari / VTT
![Page 2: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/2.jpg)
Contents
• PEM electrolysis– Alkaline electrolyzer PEM electrolyzer
• Case study: Siemens SILYZER 200– Reverse engineering study by Jari Pennanen
• Apros model for SILYZER 200– Model and results by Lotta Kannari
![Page 3: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/3.jpg)
Polymer electrolyte membrane (PEM) electrolysis
• Liquid water only at anode side
• Only H2 at cathode side• Temperature 50-80°C
![Page 4: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/4.jpg)
Input parameters for PEM modelling• The Apros model is based on the SILYZER 200
• Reverse engineering required for all parameters– IV-curve ? from lab. size cell (300 cm2) valid for large cell ?– Number of cells ? estimate from figures = 250– Cell area ? guess + reverse engineering = 35 cm x 35 cm– Dimensions of the stack ? guess + estimate 40 x 50 x 65 cm– Thermal mass ? guess + estimate = 2600 kg steel , 50 l H2O– Operational window ? Web search: 0 2.1 MW– Cooling ? Water circulation assumed, will be removed ? – Flow rates ? fixed temperature assumed flow rate– Temperature related data ? fixed temperature assumed
![Page 5: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/5.jpg)
Input parameters for PEM modelling• We don’t have IV-
curve for SILYZER 200
• This figure from SILYZER 100 presentation.
• But the IV-curve is from laboratory size device where the cell area was 300 cm2
The key assumptions for reverse engineering
• The IV curve is valid also for SILYZER 200• Iave,max 3/cm2 is valid also for large cells• Max Stack Power = 2.1 MW (confirmed)• The total number of cells is 250
![Page 6: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/6.jpg)
SILYZER 200
Max. Stack Power = 2.1 MW
![Page 7: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/7.jpg)
50 cells / stack
Assumption based on figures and data sheet Max 5 m
3.6 m
0.6 m
![Page 8: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/8.jpg)
Reverse engineering results
![Page 9: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/9.jpg)
Reverse engineering results
![Page 10: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/10.jpg)
Reverse engineering results
![Page 11: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/11.jpg)
Reverse engineering results
![Page 12: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/12.jpg)
Operational window
For large cells (Heat production in cell/ the width of the cell) ratio is bigger: cooling is not so effective Pmax / Pnominal is smaller for large cells (?).
For SILYZER Pmax / Pnominal = 2.1/1.25 = 1.68 operational window is smallerCycles 0 % .. 160 % without relevant aging (information from Siemens)
Cell area 300 cm2 ?
![Page 13: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/13.jpg)
The Apros model
Lotta Kannari
![Page 14: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/14.jpg)
Input parameters for Apros model
The following figures are calculated using older reverse engineer-ing results. But that isnot important since we can always change the input parameters.
The results of the Apros model are verified by independent MATLAB based model.For 2.1 MW
Iave=1.89 A/cm2For 1.25 MWIave=1.22 A/cm2
Reverse engineering for SILIZER 200Assuming 500 cells. Cell size 33 cm x 33 cm
![Page 15: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/15.jpg)
10/02/2016 15
APROS PEM-MODEL
![Page 16: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/16.jpg)
10/02/2016 16
Apros Model
![Page 17: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/17.jpg)
10/02/2016 17
Thermal mass
Apros Model
Heat losses to the ambient
![Page 18: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/18.jpg)
10/02/2016 18
Input water and water+O2 circulation
Apros Model
![Page 19: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/19.jpg)
10/02/2016 19
H2 and O2 output
Apros Model
![Page 20: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/20.jpg)
10/02/2016 20
Current
0
500
1000
1500
2000
2500
0 100 200 300 400 500
[A]
I[A]
0
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
1.8
2
0 200 400 600
[A/c
m2]
I_ave [A/cm2]
![Page 21: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/21.jpg)
10/02/2016 21
Power and cell voltage
0
0.5
1
1.5
2
2.5
0 100 200 300 400 500
[MW
]
P [MW]
1.4
1.5
1.6
1.7
1.8
1.9
2
2.1
0 100 200 300 400 500
[V]
U_cell[V]
![Page 22: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/22.jpg)
10/02/2016 22
H2 and O2 produktion
0
1
2
3
4
5
6
0 50 100 150 200 250 300 350 400 450
[mol
/s]
O2_simulated_[mol/s]
H2_simulated_[mol/s]
![Page 23: PEM electrolyzer model for Apros dynamic potentials](https://reader034.fdocuments.in/reader034/viewer/2022042513/586b80cf1a28ab11448b48fd/html5/thumbnails/23.jpg)
Conclusions• Siemens SILYZER 200
– We don’t know a lot. The reverse engineering step is based assumptions which may not be valid for large cells.
– Assume at least 15% margin of error in the production of H2
• Apros model for SILYZER 200– Based on previous alkaline electrolyzer model. Remove one
electrolyte + change IV curve + change cooling system + … – Model works OK, but the final fine tuning round using the
latest reverse engineering results is still needed