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ORNL-1771 - Oak Ridge National Laboratory

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Fuel-to-NaK heat exchanger<br />

PERlOD ENDING SEPTEMBER ?O, 7954<br />

TABLE 2.1. TENTATIVE SYSTEM DATA FOR THE CFRE FLUID CIRCUlfS<br />

Temperature drop (or rise), OF<br />

Pressure drop, psi<br />

Flow rate, cfs<br />

Velocity through tube matrix, fps<br />

Reynolds number<br />

Over-all heat transfer coefficient, Btu/hr.ft2*OF<br />

Fuel-to-NaK temperature difference, OF<br />

Moderator cooling system<br />

Temperature drop (or rise) in heat exchanger, OF<br />

Sodium-NaK temperature difference, OF 43<br />

Pressure drop in heat exchanger, psi<br />

Pressure drop in reflector, psi<br />

Pressure drop in island, psi<br />

Pressure drop in pressure shell, psi<br />

Temperature rise in reflector, OF<br />

Temperature rise in island, OF<br />

Temperature rise in pressure shell, OF<br />

Power generated in reflector, kw<br />

Power generated in island, kw<br />

Power generated in pressure shell, kw<br />

Flow rate through reflector, cfs<br />

Flow rate through island and pressure shell, cfs<br />

NaK cooling system<br />

Airflow through NaK radiators. cfrn<br />

Radiator air pressure drop, in. H20<br />

Blower power required, hp (total)<br />

Blower power required, hp (per fan)<br />

Total rodiator inlet face orea, ft2<br />

Shield cooling system<br />

Power generated in lead layer, kw<br />

Power generated in water layer, kw<br />

Pump data<br />

Head, ft<br />

Flow, gpm<br />

Specific speed<br />

Suction specific speed<br />

impeller speed, rpm<br />

Drive, hp<br />

General<br />

3,150<br />

95<br />

2,040<br />

600<br />

210<br />

150,000<br />

24<br />

720<br />

180<br />

72<br />

132<br />

i 4<br />

Circuit<br />

Fuel No Na K<br />

400<br />

35<br />

2.7<br />

8.0<br />

4,600<br />

400<br />

40<br />

12.6<br />

36.4<br />

100 100<br />

7 7<br />

36<br />

32<br />

4<br />

100<br />

72<br />

28<br />

1.35<br />

0.53<br />

50 250 280<br />

600 430 2,600<br />

3,750<br />

13,200<br />

2,700<br />

25 16 200

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