First Wall Thermal Hydraulics Analysis El-Sayed Mogahed Fusion Technology Institute The University of Wisconsin With input from S. Malang, M. Sawan, I.

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First Wall Thermal Hydraulics Analysis El-Sayed Mogahed Fusion Technology Institute The University of Wisconsin With input from S. Malang, M. Sawan, I. Sviatoslavsky, S. Smolentsev, C. Wong Presented by Mohamed Sawan APEX Review Meeting April 7-9, 2003

University of Wisconsin Fusion Technology Institute 2 FW Thermal Hydraulics Analysis  Considered two options with circular and rectangular FW tubes  Assessed improvement resulting from using eccentric Pb tubes in the FW channels  Optimized FW channel dimensions to maintain uniform pressure drop (including MHD pressure drop) and uniform Flibe temperature  Determined FW thermal hydraulics parameters (pressure drop, velocities, temperatures for the reference rectangular FW channels  Considered two options with circular and rectangular FW tubes  Assessed improvement resulting from using eccentric Pb tubes in the FW channels  Optimized FW channel dimensions to maintain uniform pressure drop (including MHD pressure drop) and uniform Flibe temperature  Determined FW thermal hydraulics parameters (pressure drop, velocities, temperatures for the reference rectangular FW channels

University of Wisconsin Fusion Technology Institute 3 Option with Circular FW Tubes

University of Wisconsin Fusion Technology Institute 4 Formulas, parameters, and data used Nu = Pr 0.3 Re 0.9 For Pr>20 The Blasius friction coefficient, f = /Re 0.25 Pressure drop in a vertically moving fluid:  P =  v 2 /2 + f  L v 2 /2d where: Nu is the Nusselt number, Pr is the Prandtl number, Re is the Reynolds number,  is the fluid density, v is the coolant velocity, d is the coolant tube hydraulic diameter, and L is the coolant tube length. Flibe properties at 600 °C density = 2120 kg/m 3 thermal conductivity = 1 W/mK heat capacity = 2380 J/kg K kinematics viscosity = 5.48e-6 m 2 /s Nuclear heating profiles used in analysis Peak neutron wall loading = 5.45 MW/m 2 Peak surface heat flux = 1 MW/m 2 Average OB neutron wall loading = 4.61 MW/m 2 Average IB neutron wall loading = 2.80 MW/m 2 Average OB surface heat flux = 0.95 MW/m 2 Average IB surface heat flux = 0.90 MW/m 2

University of Wisconsin Fusion Technology Institute 5 Impact of using eccentric lead tubes in the FW  Results in larger cooling sub-channels at the front and smaller ones at the back  For the same pressure drop, flow velocity will be larger with higher heat transfer coefficient at front where larger heat load needs to be removed  The eccentric configuration was analyzed and compared to the concentric design with the same pressure drop for circular tubes  Results in larger cooling sub-channels at the front and smaller ones at the back  For the same pressure drop, flow velocity will be larger with higher heat transfer coefficient at front where larger heat load needs to be removed  The eccentric configuration was analyzed and compared to the concentric design with the same pressure drop for circular tubes

University of Wisconsin Fusion Technology Institute 6 Eccentricity increases velocity at front zone with largest heat load For concentric tubes: Velocity is uniform = 7.21 m/s Pressure drop = MPa

University of Wisconsin Fusion Technology Institute 7 Eccentricity enhances Flibe temperature uniformity around the multiplier tube

University of Wisconsin Fusion Technology Institute 8 Eccentricity reduces the maximum interface temperature between FLIBE and steel

University of Wisconsin Fusion Technology Institute 9 Analysis for rectangular FW tubes Design with circular FW tubes is easier to fabricate Mike Friend calculated stresses in a blanket element, taking into account coolant pressure in FW tubes as well as pressure in the large blanket central duct While stresses caused by pressure in FW tube itself are lower for the circular tubes, pressure in central duct leads to higher stresses in FW region compared to the rectangular reference design We optimized the reference rectangular design by using eccentric multiplier tubes and adjusting width of side Flibe channel MHD pressure drop was included using the results of Sergey’s 2-D calculations Optimization performed for both OB and IB FW channels

University of Wisconsin Fusion Technology Institute 10 Optimized OB Rectangular FW tubes Size of the Flibe zones surrounding the Pb tube optimized to maintain uniform pressure drop and temperature rise Total pressure drop is 1.03 MPa Temperature rise is 30 °C

University of Wisconsin Fusion Technology Institute 11 Interface Temperatures with Steel in OB Reference Rectangular FW Tubes  Volumetric flow rate per tube = 9043 cm 3 /s  Average Flibe velocity at midplane = 6.42 m/s  Maximum interface temp. between FLIBE and FW steel = 667 °C  Maximum interface temp. between lead and steel = 680 °C

University of Wisconsin Fusion Technology Institute 12 Optimized IB Rectangular FW tubes Higher magnetic field (~8 T compared to ~4.3 T in OB) Lower heat load compared to OB Smaller velocity for the same temperature rise of 30 °C Total pressure drop is 0.88 MPa

University of Wisconsin Fusion Technology Institute 13 Interface Temperatures with Steel in IB Reference Rectangular FW Tubes  Volumetric flow rate per tube = 6287 cm 3 /s  Average Flibe velovity at midplane = 4.69 m/s  Maximum interface temp. between FLIBE and FW steel = 686 °C  Maximum interface temp. between lead and steel = 652 °C

University of Wisconsin Fusion Technology Institute 14 Summary  Dimensions of FW Flibe channels optimized to maintain uniform pressure drop and temperature rise around the Pb tubes  Total FW pressure drop is 1.03 MPa in OB and 0.88 MPa in IB  Volumetric flow rate per tube is 9043 cm 3 /s in OB and 6287 cm 3 /s in IB  Maximum interface temperature between FLIBE and FW steel is 686 °C (in IB module)  Maximum interface temperature between lead and steel is 680 °C (in OB module)  Dimensions of FW Flibe channels optimized to maintain uniform pressure drop and temperature rise around the Pb tubes  Total FW pressure drop is 1.03 MPa in OB and 0.88 MPa in IB  Volumetric flow rate per tube is 9043 cm 3 /s in OB and 6287 cm 3 /s in IB  Maximum interface temperature between FLIBE and FW steel is 686 °C (in IB module)  Maximum interface temperature between lead and steel is 680 °C (in OB module)