Supercritical carbon dioxide power generation system and operation method
A power generation system, carbon dioxide technology, applied in the direction of machines/engines, steam engine devices, mechanical equipment, etc., to achieve the effect of improving energy utilization, simple system, and strong adaptability
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Embodiment 1
[0049] figure 1 The structure of the supercritical carbon dioxide power generation system in Example 1 is schematically shown. like figure 1 As shown, in a supercritical carbon dioxide power generation system provided by this embodiment, m=2, n=3.
[0050] Specifically, the heater system includes a primary heat exchanger 11 , a secondary heat exchanger 12 and a tertiary heat exchanger 13 . The turbine system includes a primary turbine 21 and a secondary turbine 22 . The regenerator system includes a primary regenerator 31 and a secondary regenerator 32 . The precooling system includes a precooler 4 . The compression system includes a compressor 5 . The routing system 6 includes a main pipeline 61 , a branch pipeline 62 , a flow divider 63 , a collector 64 , and a pipeline 65 that connect each system. The power generation system may include a discharge machine. In this embodiment, the primary turbine 21 , the secondary turbine 22 , the compressor 5 and the generator 7 ar...
Embodiment 2
[0057] figure 2 The structure of the supercritical carbon dioxide power generation system in Example 2 is schematically shown. like figure 2 As shown, in a supercritical carbon dioxide power generation system provided by this embodiment, m=3, n=4, the system can adapt to waste heat with a higher temperature level. The specific connection and operation modes are similar to those in Embodiment 1, and will not be repeated.
Embodiment 3
[0059] image 3 The structure of the supercritical carbon dioxide power generation system in Example 3 is schematically shown. like image 3 As shown, in a supercritical carbon dioxide power generation system provided by this embodiment, m=2, n=2, the system can be adapted to waste heat with a lower temperature level. The difference from Example 1 is that after the secondary heat exchanger 12 and the secondary regenerator 32 are heated respectively, they are no longer collected, but the outlet of the secondary heat exchanger 12 is directly connected to the inlet of the secondary turbine 22. The outlet of the heat-absorbing side of the first-stage regenerator 32 is directly connected to the inlet of the first-stage turbine 21, and the other connection and operation modes are similar to those in Embodiment 1, and will not be repeated.
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