DESALINATION 221
Large capacity plants usually produce, to some extent,
cheaper water than small capacity plants.
Energy is usually an expensive item. The proposal to use
cheap waste heat from nuclear plants failed, due to many rea-
sons connected to the coupling of the two systems. Today the
problem is reexamined and the trends are in favor of nuclear
desalination. Nevertheless, no large plants have been erected.
The two leading processes of desalination are the MSF
distillation and the reverse osmosis. In Table 3 the costs of
the two processes are compared.
TABLE 3
MSF versus RO seawater desalting costs
Plant capacity m^3 /d (mgd)
3.8(1) 11.4(3) 18.9(5.0) 37.9(10.0)
Total capital cost $ × 103
MSF 8.621 19.737 30.928 54.337
RO 5.887 15.581 24.082 43.01
Total operating $ × 103
MSF 2.064 4.94 7.785 14.401
RO 1.758 4.675 7.404 13.806
Cost of product water
MSF $/m^3 ($/kgallons) 1.65 (6.29) 1.32 (5.01) 1.25 (4.74) 1.15 (4.38)
RO $/m^3 ($/kgallons) 1.41 (5.35) 1.25 (4.74) 1.19 (4.51) 1.11 (4.20)
0
2
4
6
8
10
12
14
16
18
20
1965 1970 1975 1980 1985 1990
YEAR OF OPERATION
CAPACITY INSTALLED, 10
6 m’/d
TOTAL DESALINATION
TOTAL DISTILLATION
MSF DISTILLATION
REVERSE OSMOSIS
ELECTRODIALYSIS
1960 1995
FIGURE 21
C004_001_r03.indd 221C004_001_r03.indd 221 11/18/2005 10:19:02 AM11/18/2005 10:19:02 AM