A. Bick et G. Oron, Desalination technology for optimal renovation of saline groundwater in a natural reservoir, DESALINATN, 131(1-3), 2000, pp. 97-104
Huge amounts of water are currently diverted down-stream from the Sea of Ga
lilee (Lake Kinneret) to the rift valley, Israel. Part of the non-utilized
water is saline (around 2000 mg/l chlorides) originated in the northern sec
tion of Lake Kinneret and separated from the bulk high quality water (betwe
en 200 mg/l and 250 mg/l chlorides). The flow rate of the saline water is v
ery much affected by the level of the water in the lake that serves as the
prime natural storage reservoir for water supply in Israel. The wasted amou
nt of the diverted water can be shared, after adequate treatment, for use i
n the Rift Valley primarily for agricultural irrigation in the Kingdom of J
ordan and the State of Israel for their mutual benefits. A management model
was defined and tested towards optimal treatment of the saline water. The
two major purposes of the model are (i) to delineate a methodology for econ
omic assessment towards optimal use of membrane technology, and; (ii) to pr
ovide guidelines for optimal membrane selection in regards to the pretreatm
ent stage. The linear model defined takes into account the cost of the feed
saline water, the desalination stage, based on the reverse osmosis (RO) pr
ocess, and the brine disposal. Technological constraints refer primarily to
the longevity of the membrane, their performance and time dependent change
s in flow-rates, Eight different saline water qualities, subject to various
pretreatment options, for a tentative desalination plant for a capacity of
30,500 m(3)/d close to Lake Kinneret were examined, The final treated unit
water cost, which is expressed by the objective function, includes investm
ent, operation and maintenance, water intake, pretreatment, RO components,
post treatment, brine removal and incentive for permeate low salinity. Anal
yzing various scenarios allows optimal selection of the membrane and the re
lated pretreatment method. The cost range of the desalinated water accordin
g to the model is between $0.39/m(3) and $0.45/m(3).