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Figure 3. 11. Experimental and predicted pressure drop by HEAM and CFD models for different electrolyte flow rates. The data are for flow fields from the Messaggi’s article. [43] (CFD: Computational fluid dynamics, CP: Carbon paper) ...................................................................... 47 Figure 3. 12. Experimental, and predicted pressure drop by HEAM and CFD models for different electrolyte flow rates. The data are for an IFF flow field with the channel size of 1.59 mm × 1.9 mm from the Aziz’s article. [38] (CFD: Computational fluid dynamics, CP: Carbon paper)...... 48 Figure 3. 13. Experimental, and predicted pressure drop by HEAM and CFD models for different electrolyte flow rates. The data are for a VRFB with IFF with the channel size of 1.59 mm × 1.9 mm from the Aziz’s article. [38] (CFD: Computational fluid dynamics, CP: Carbon paper)...... 49 Figure 3. 14. Experimental and predicted pressure drop for IFFs with different channel dimensions by different models. (Red: 0.79 mm× 1.9 mm- 6 parallel channels, Black: 1.59 mm× 1.9 mm- 4 parallel channels) HEAM is more accurate than Aziz and MacDonald’s models at predicting the pressure drop in both cases. .......................................................................................................... 52 Figure 3. 15. Experimental and predicted pressure drop for IFFs with different channel dimensions by different models. (Blue: 0.25 mm× 0.25 mm- 10 parallel channels) HEAM is more accurate than Aziz and MacDonald’s models at predicting the pressure drop. .......................................... 53 Figure 3. 16. Experimental and predicted pressure drop for IFFs with different channel dimensions by HEAM. (Blue: 0.25 mm× 0.25 mm- 10 parallel channels, Red: 0.79 mm× 1.9 mm- 6 parallel channels, Black: 1.59 mm× 1.9 mm- 4 parallel channels). It predicts correct trends for the change in pressure drop with different channel area for blue and black, and blue and red cases; however, it cannot predict the same relationship for black and red case correctly. ..................................... 54 Figure 3. 17. Experimental and predicted pressure drop for IFFs with different channel dimensions by Messaggi and Aziz models. (Blue: 0.25 mm× 0.25 mm- 10 parallel channels, Red: 0.79 mm× viPDF Image | Analysis of Fluid Flow in Redox Flow Batteries
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