 |
|
 |
|
|

Fluorides removal plant
Within the frame of the wastes pollution control upgrading programs, more stringent
regulations now apply with reference to fluorides content. The maximum fluoride
content in the treated water may be nowadays as low as 3ppm. In order to meet
such design parameters the standard chemical physical process is not sufficient
and a double step process has to be designed.
PROCESS DESCRIPTION
First step: physical-chemical treatment
The target of this treatment step is to eliminate most of F- ions by precipitation
of calcium fluoride. To this purpose, the treatment scheme is consisting of 4 sections:
- Acidification
- Precipitation
- Flocculation
- Clarification/Settling
The composition of the clarified water is in equilibrium whit the precipitated
Calcium Fluoride, thus being in the range of 15÷20 ppm F-.
The involved reactions are the following
Ca(OH)2 + 2H+ Ca2+ + 2H2O
Ca2+ + 2F- CaF2
Al3+ + 3OH- Al(OH)3
Second step: polishing treatment
Purpose of the second treatment step is to reduce the fluoride residual down to 3 ppm.
To this purpose, the treatment scheme is consisting of 2 sections:
- Filtration
- Unifluor A adsorption
Filtration
The clarifier effluent is released to the filtration step
consisting of pressure media filters.
The purpose of this treatment stage is to remove any fine suspended matter
from the treated water, to prevent any clogging effect on the following activated
alumina fine filters.
Fluoride removal by activated alumina filters
The filtered stream is then fed, after pH conditioning, to the Unifluor A filters
where the ultimate removal of Fluoride ions is finally achieved by an adsorption process.
The term adsorption means the physical chemical process by which a porous solid
(in our case Unifluor A, which is a particular type of activated alumina) is able
to adsorb on its surface molecules of an element or of a compound (in our case F-)
present in the fluid (water) which is percolated through it.
This phenomenon is affected by the concentration of the compound to be removed
both in the liquid and in the adsorbing material. Being the adsorption mainly a
surface phenomenon, it is also of great importance the ratio surface/volume of
the adsorbing material.
All the wash and waste waters originated from filters backwash and Unifluor A
regeneration are recycled back to the treatment so that the only by-product of the
entire treatment is the sludge cake to be disposed off.
top
|
|
|
|