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Introduction
For every tonne of phosphoric acid as P2O5 produced using
the wet process, from 4.5 to more than 5.5 tonnes of phosphogypsum are
generated, depending on the quality of the phosphate rock. It is estimated
that more than 22 million tonnes of phosphoric acid (as P2O5) are produced
annually worldwide*, generating in excess of 110 million tonnes of gypsum
by-product. The free water in the gypsum cake off the filters is highly
acidic, having a pH as low as 1.0. While commercial uses, in agriculture
and in manufacturing gypsum board and Portland cement, consume less than a
few percent of this by-product, the vast majority is disposed of on land
in gypsum stacks or is discharged into water bodies.
Properties of Phosphogypsum
Physical Properties
Depending on the reaction temperature used to produce
phosphoric acid, calcium sulfate in either the dihydrate (CaSO4.2H20) or
the hemihydrate (CaSO4.½H20) form is generated as a by-product filter
cake. The gypsum cake, after filtration, usually has a free moisture
content between 25 and 30 percent. Hemihydrate, in the presence of free
water will, fairly rapidly, convert to dihydrate (gypsum) and in the
process, if left undisturbed, will set up into a relatively hard cemented
mass.
Dihydrate consists of relatively soft, principally
silt-size (<0.075mm) aggregates of crystals, the morphology of which
depends on the source of the phosphate rock and the reactor
conditions.
Typical engineering properties of phosphogypsum can be
found in Wissa , . Properties, such as density, strength, compressibility
and permeability (hydraulic conductivity), are not only controlled by the
rock source and reaction process, but also by the method of deposition,
age, location and depth within the landfill or stack in which the gypsum
is placed. The deeper the gypsum is within a stack and the older the
stack, the higher its density and strength and the lower its
compressibility and permeability, provided solution channels and cavities
have not developed in the stack as a result of rainfall
infiltration**.
Chemical Properties
Phosphogypsum consists primarily of calcium sulphate
dihydrate with small amounts of silica, usually as quartz, and unreacted
phosphate rock. Radium and uranium, as well as minor amounts of USEPA
toxic metals, namely, arsenic, barium, cadmium, chromium, lead, mercury,
selenium and silver and phytotoxic fluoride and aluminum are also present
in phosphogypsum and its pore water. The concentrations of the heavy
metals and radionuclides depend on the composition of the phosphate rock
feed. The concentrations of constituents in phosphate rock, phosphogypsum
and process water ( i.e., free water in gypsum stacks and cooling ponds)
from Central Florida have been reported by Garlanger .
Environmental concerns, more perceived than real, have
developed in the last ten years because of the presence of the trace toxic
metals and radionuclides in phosphogypsum and its pore water. As a result,
its usage, transportation and storage, as well as that of the associated
ponds which contain process water at pH values below 2, are now in the
U.S.A. regulated by state agencies such as the Florida Department of
Environmental Protection (FDEP) and/or the U.S. Environmental Protection
Agency (USEPA) .
Disposal Options
Worldwide, four methods are being used by the phosphate
industry to dispose of surplus phosphogypsum, namely: (i) discharging to
water bodies; (ii) backfilling in mine pits; (iii) dry stacking; and (iv)
wet stacking.
The term "dry stacking" (as it applies to conveying or
hauling and stacking) means that the gypsum is transported and stacked at
the same moisture content as when it discharges from the filter. The term
is somewhat misleading since the actual moisture content is typically
between 20 and 25%*. "Wet stacking" involves pulping the cake with
additional water to form a slurry that can be pumped or hydraulically
transported to a disposal area. For the sake of completeness, all four of
the methods are described in the following sections even though only
environmental aspects of the dry and wet stacking options will be
addressed.
Discharging to Water Bodies
A relatively small number of phosphoric acid chemical
plants discharge their phosphogypsum directly to a receiving water body.
These include major producers in Morocco, where the gypsum cake is
slurried with sea water and discharged into the Atlantic Ocean. While
discharging waste gypsum as a dilute slurry into very large open water
bodies with strong currents and tides off uninhabited coasts is the most
economical disposal option, and may be politically and environmentally
acceptable, discharging gypsum into rivers and smaller bodies of water,
such as the Mediterranean Sea, is no longer politically acceptable.
Most existing phosphoric acid plants, and those currently
under construction or in the planning stage, are not located near suitable
water bodies to allow for disposal of their gypsum by-product in the sea,
and disposal on land is the only economically viable option. Therefore,
this paper will be limited to the environmental aspects of land
disposal.
Gypsum-Tailings Blending
The pits created from mining phosphates at PCS Phosphates
in North Carolina, USA, are being reclaimed by backfilling with a blend of
phosphatic clay tailing from the rock beneficiation process and
phosphogypsum obtained directly off the phosphoric acid plant filters.
This is environmentally acceptable because the high calcareous content of
the clay in the ore at that mine neutralizes the acid remaining in the
gypsum cake after filtration. PCS Phosphates has a unique set of
hydrogeologic conditions that are not likely to be present anywhere
else.
Phosphogypsum, because of its relatively high solubility,
high compressibility and radioactivity, is generally not recommended as
structural fill for land reclamation, especially if the land will be used
for housing.
Wet Stacking |
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Wet stacking is by far the most popular phosphogypsum
land disposal method. This method involves pulping the gypsum cake as it
comes off the filter with either fresh or sea water and pumping the slurry
through a pipeline to a gypsum disposal area where the solids are allowed
to settle out (Figure 1). Clarified excess water is decanted, and in the
case of a fresh water system, pumped back to the plant for re-slurrying
gypsum and reuse in the process. With time, the recirculated process water
usually reaches an equilibrium pH between 1.3 and 2.0, depending on the
process and climatic conditions. The soluble P2O5 content of the acidic
process water is typically between 10,000 and 15,000 mg/liter (mg/l), but
can be as high as 20,000 mg/l.
When sea water is used to slurry the gypsum, the
clarified sea water is not returned to the plant for reuse, but discharged
back to the sea. When sea water is the carrier, the slurry is usually very
dilute (about 5% solids by weight), and the pH of the water being
discharged is above 2.0. Several plants, namely in Greece, Spain, Mexico
and Tunisia, have considered or are considering eliminating the use of sea
water and converting to closed-circuit fresh water systems. Slurry
concentrations between 20% and 30% by weight are commonly used in
closed-circuit water systems. It should be noted that when a gypsum stack
is converted from a sea water to a fresh water system, unless special
provisions are taken to reduce contamination, the return water to the
plant from the stack will be, at least initially, high in chlorides due to
leaching of the old gypsum. This can cause corrosion problems. |
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