Encyclopedia of Environmental Science and Engineering, Volume I and II

(Ben Green) #1

202 DESALINATION


temperatures and pressures. Thus, water alone is vaporized,
which is the main product, and the dissolved solids remain
in the residual liquid, the brine.
In the chemical industry, when an evaporation process
is applied, the water vapors are usually discarded and the
emphasis is given to the recuperation of the dissolved solids.
In desalination the term “distillation” predominates over
the correct term “evaporation.” The process is performed in
evaporators, where heat is supplied to the solution, to change
phase.
The productivity is expressed either as the net evapo-
ration or “gain output ratio” (GOR), i.e., the kilos of pro-
duced distilled water per kilo of boiler steam used, (kg/kg)
or as performance ratio R. It is usually prefered, instead of
the GOR, to use the term performance ratio which defines
the mass of distillate produced per 2326 kJ (gal/1000 BTU)
of heat input to the brine heater in case of MSF distilla-
tion or to the first effect in case of multiple-effect evapo-
rators. The latter definition is thermodynamically more
accurate, as it refers to the enthalpy of the steam instead to
the mass.
Thermodynamic considerations lead to a common char-
acteristic of all distillation process, that the percentage of
evaporated water with respect to the circulating seawater is
as much larger as is the difference between the maximum
and minimum temperature of the saline solution. As the
minimum temperature is defined by the temperature of the

incoming seawater, enlarging of the temperature difference
can only be obtained by increasing the initial maximum
temperature of the salt water feed. Limitations due to the
appearance of phenomena like scale formation and corro-
sion, which are becoming more important at higher tempera-
tures, define an allowable maximum temperature for each
distillation process. An appropriate pretreatment of the salt
water is necessary to make an increase of the feed water tem-
perature possible.
The economics of the distillation process might be
affected by the following parameters:


  • The chemical additives for feed water pre-
    treatment

  • Scale formation which decreases performance

  • Increase of maintenance costs due to corrosion


Corrosion may increase fixed changes, when more
expensive materials of construction must be used.

Multiple-Effect Distillation (ME)

Theoretically, in single-effect distillation 1 kg of distillate
will be produced for every kg of steam consumed and the
gain output ratio of the plant will be 1. In fact, despite pre-
heating of the feed, a large part of the enthalpy of the vapors,

FIGURE 4 The first historically known solar distillation equipment, according to Giovanni
Batista De La Porta. The sun evaporates the water inside the glass vessels and distilled water is
collected beneath the vessels. “De distillations,” Libri IX, Rome 1608.

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