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Performance Improvement Options for the Supercritical Carbon Dioxide Brayton Cycle

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Performance Improvement Options for the Supercritical Carbon Dioxide Brayton Cycle ( performance-improvement-options-supercritical-carbon-dioxide )

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| | Hot side flow rate | | | Cold side temperature inlet | | | Cold side temperature outlet | | | Cold side pressure inlet | | | Cold side pressure outlet | | | Cold side flow rate | | | Effectiveness | | | Metal mass | | | Cost | | | CO2 mass | |---------------|------------------------------|----------|-------|-----------------------------------| | Low | Temperature | Recuperator | | | | | | | | | | | | | | | | | | | | | | | | | | | | | | | |---------------|------------------------------|----------|-------|-----------------------------------| | Cooler | | | | | | | | | | | | | | | | | | | | | | | | | Type | Quantity | Heat transfer capacity | Heat transfer area | Unit width | Unit height | Unit length | Heat transfer length | Channel diameter | Channel pitch | Plate thickness | Plate material | Number of plates | CO2 side number of channels | CO2 side channel length | CO2 side channel angle | H2O side number of channels | PCHE | | 48 | | 3.03 | MWt | 199.2 | m2 | 1.500 | m | 0.600 | m | 0.593 | m | 0.373 | m | 2.0 | mm | 2.4 | mm | 1.66 | mm | SS316 | | 170 | | 432 | | 0.528 | m | 90.0 | deg | 529 | | 0.431 | m | 90.0 | deg | 35.0 | % | 90.3 | C | 32.79 | C | 7.629 | MPa | 7.621 | MPa | 20.3 | kg/s | | | All parameters below are per unit | | Type | | Quantity | | Heat transfer capacity | | Heat transfer area | | Unit width | | Unit height | | Unit length | | Heat transfer length | | Channel diameter | | Channel pitch | | Plate thickness | | Plate material | | Number of plates | | Hot side number of channels | | | | All parameters below are per unit | | Hot side channel | Hot side channel | Cold side number | Cold side channel length | | Cold side channel angle | | Void fraction | | Hot side temperature inlet | | Hot side temperature outlet | | Hot side pressure inlet | | Hot side pressure outlet | | Hot side flow rate | | Cold side temperature inlet | | Cold side temperature outlet | | Cold side pressure inlet | | Cold side pressure outlet | | Cold side flow rate | | Effectiveness | | Metal mass | | Cost | | CO2 mass | 2.0 | SS316 | 141 | 218 | 0.670 | 60.0 | 178 | 0.820 | 90.0 | 18.5 | 191.1 | 90.3 | 7.690 | 7.629 | Each side Per plate Heat transfer From channels | H2O side channel | H2O side channel | Void fraction | CO2 temperature inlet | CO2 temperature outlet | CO2 pressure inlet | CO2 pressure outlet | CO2 flow rate | | | | Each side | Per plate | Heat transfer | | Per plate | Heat transfer | | From channels | | | | | | | | | | region | | | region | | | | | | | | length | angle | of channels | Per plate Heat transfer length angle 21.5 | kg/s 175.6 | C 323.4 | C | | | | | | | | | | | | | | 19.960 | MPa 19.907 | MPa 21.5 | kg/s 91.7 | % 3.291 | tonnes| 197.5 | K$ | At $60/kg | Dry | 9.7 | kg | Operating conditions | PCHE | 128 | 1.30 | MWt 79.4 | m2 0.600 | m 0.600 | m 0.800 | m 0.580 | m 1.5 | mm 2.3 | mm mm m deg | | | | | | | | | | | | | | | | | | | | | | 10.7 | kg/s 84.4 | C 172.2 | C 20.000 | MPa 19.960 | MPa 12 7.6 | kg/s 94.5 | % m deg % C C MPa MPa 1.817 | tonnes| 109.0 | K$ | At $60/kg | | | | | | | Semi-circular channel | | | | | | region | | | region | | | | | | | | | | | | | | | | 10.0 | kg | Operating conditions | Dry | | | | | | | Semi-circular channel | | | | | | | | | | | | |

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