Economics

The construction cost of the Savannah River heavy-water plant, built in 1951/1952, is summarized in Table 13.19 [B6]. The unit investment cost of this plant, capable of producing 454 Mg D20/year, then was $163,000,000/454,000 kg/year = $359/(kg/year).

The cost of Atomic Energy of Canada, Ltd.’s 800 Mg/year plant at La Prade, item 21, Table 13.2, was predicted [H5] to be $300 million in 1974, for a unit investment cost of $375/(kg/year), exclusive of escalation and interest during construction.

Heavy water from the Savannah River plant was sold by the U. S. AEC in the 1960s for a price of $61.73/kg. Demand for heavy water subsequently decreased, and two of the three original wings of the plant were shut down. In 1976, when one wing was operating at its full

Table 13.19 Construction cost of Savannah River heavy-water plant

$ million

Process facilities

H2 S exchange units

113

Water distillation plant

2.5

Electrolytic plant

1.5

Steam and electric power plant

31

Water system

8

General facilities

7

$163

Source: W. P. Bebbington and V. R. Thayer, Chem. Eng. Progr. 55(9): 70 (1959).

capacity of 177 MT/year, production costs [J5] were as summarized in Table 13.20. In 1977, when the one remaining wing was operating at reduced capacity, the price charged by U. S. ERDA for heavy water was $245/kg [FI].

Utility requirements reported for heavy-water production by the GS process are as follows:

Heat,

Electricity,

kWht/kg D2 0

kWhe/kg D20

Savannah River [B8]

7800

680

Canada [R2]

6800

700