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Article

Analysis and optimization of the manifolds of the HCCB blanket for CFETR

, , , , , & show all
Pages 979-984 | Received 06 Sep 2017, Accepted 02 Apr 2018, Published online: 25 Apr 2018

Figures & data

Figure 1. Present design of the CFETR HCCB blanket.

Figure 1. Present design of the CFETR HCCB blanket.

Figure 2. Flow schemes of coolant and purge gas.

Figure 2. Flow schemes of coolant and purge gas.

Figure 3. The first coolant manifold design: (a) primary design; (b) optimization design.

Figure 3. The first coolant manifold design: (a) primary design; (b) optimization design.

Figure 4. Mass flow rates of the outlets of the first coolant manifold.

Figure 4. Mass flow rates of the outlets of the first coolant manifold.

Figure 5. Helium streamline with velocity of the first coolant manifold: (a) primary result; (b) optimization result.

Figure 5. Helium streamline with velocity of the first coolant manifold: (a) primary result; (b) optimization result.

Figure 6. The second coolant manifold design: (a) primary design; (b) optimization design.

Figure 6. The second coolant manifold design: (a) primary design; (b) optimization design.

Figure 7. Mass flow rates of outlets of the second coolant manifold.

Figure 7. Mass flow rates of outlets of the second coolant manifold.

Figure 8. Helium streamline of the second coolant manifold: (a) primary result; (b) optimization result.

Figure 8. Helium streamline of the second coolant manifold: (a) primary result; (b) optimization result.

Figure 9. Temperature distribution on FW in radial-toroidal crosssection.

Figure 9. Temperature distribution on FW in radial-toroidal crosssection.

Figure 10. Peak temperature of Li ceramic and Be.

Figure 10. Peak temperature of Li ceramic and Be.

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