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Arsenic cleanup is a major environmental goal.
This metal is the 20th most abundant element of
the earth’s crust and finds it way into the soil
and into the water supply all around us. There
is no good reason for having arsenic absorbed by
our bodies – it is toxic.
Removal of arsenic from our
environment is essential for good health. Health
effects are dose related and for this reason
standards for acceptable exposure continue to be
lowered. The goal will be the eventual removal
of any detectable arsenic from the water supply.
The WHO guideline Value for
arsenic in drinking water was lowered from 50 to
10 ug/Liter in 1993 and this level is enforced
in the United States by the Environmental
Protection Agency.
All forms of arsenic need to
be removed from the water supply. Advanced water
purification techniques include membrane
systems, coagulation flocculation and other high
technology solutions. No company does as good a
job at removing arsenic as the new technology
being developed by Dynamic Adsorbents. No one is
able to remove all forms of arsenic in a simple
single process such as the design being
evaluated for commercial release like Dynamic
Adsorbents. There is no simpler, more affordable
and heavy duty product available on the market
today.
Essentials of the Chemistry of Arsenic
A review of the chemistry of
arsenic is in order.
Arsenic occurs in
groundwater in two forms:
Arsenite (As033-)
Arsenate (As043- )
These two types of natural
compounds leached from the earth’s crust are
referred to as arsenic (III) and arsenic (V)
species due to the oxidation number of the
central arsenic atom.
Each ion can acquire from
water one or more protons, depending on the
acidity of the water. They then exist as a set
of chemical species:
Arsenic III series
As033- HAs032- H2As03- H3As03
Arsenic V series As043-
HAs042- H2As04- H3As04
At the acidity of drinking
water, the dominant arsenic III species is found
primarily as the neutral compound H3As03 . The
dominant arsenic V species are the ions HAs042-
and H2As04-. However, for both the arsenic III
and V species there is coexistence and rapid
conversion to all of the above forms in this
chemical set.
Arsenic III compounds are 10
times more toxic to the human body than Arsenic
V forms. The proportion of arsenic in ground
water typically ranges between 50 and 90%.
What are the commercially
available technologies for the removal of
arsenic from the water supply?
Oxidation reduction
This technology takes
advantage of reactions that reduce (add
electrons to) or oxidize (remove electrons from)
chemicals, altering their chemical form. These
reactions do not remove arsenic from solution,
but are often used to optimize other processes
utilized for the removal of arsenic from water.
Arsenic removal technologies
are most effective at removing arsenic V, since
arsenic III is non-charged below pH 9.2. For
this reason most treatment solutions provide an
oxidation step to convert arsenite to arsenate.
Oxidation alone does not remove arsenic from
solution, and must be coupled with other removal
processes such as coagulation, adsorption or ion
exchange. Commercially used oxidizing agents
include gaseous chlorine, hypochlorite, ozone,
potassium permanganate and hydrogen peroxide.
Precipitation
This causes dissolved
arsenic to form a low solubility solid mineral
such as calcium arsenate. The solid calcium
arsenate can then be removed through
sedimentation and filtration. When coagulants
are added and form flocs, other dissolved
compounds such as arsenic can become insoluble
and form solids. This is known as
co-precipitation. The solids formed may remain
suspended, or may require removal through
solid/liquid separation processes, typically
coagulation and filtration.
However, coagulation is
unable to lower the arsenic level to the
acceptable low safety range of 10 ug/Liter. Two
of the most commonly used precipitating agents
are ferric chloride (FeCl3) and alum or aluminum
potassium sulfate. Ferric chloride removes
around 80% of arsenic from water while alum
removes 85-92%.
Adsorption and ion exchange
Various solid materials
including iron and aluminum hydroxide flocs have
a strong affinity for dissolved arsenic. Arsenic
is strongly attracted to sorption sites on the
surfaces of these solids and effectively removed
from solution. The finding that activated
alumina removes arsenic from water was
discovered accidentally by Bellack in 1971. The
high surface area and large number of sorption
sites makes activated alumina a superior
adsorption agent.
The mechanism of arsenic
removal is similar to that of a weak base ion
exchange resin. Arsenate removal capacity is
best in the narrow pH range of 5.5 to 6.0, where
the alumina surfaces are protonated. Typically
activated alumina has a point of zero charge (PZC)
below which the surface is positively charged,
and above which the surface bears a negative
charge at pH 8.2 Arsenic removal capacity drops
sharply as the PZC is approached and above pH
8.5 it is reduced to only 2-5% of capacity at
optimal pH. For neutral and basic waters
therefore pH adjustment may be necessary for
effective arsenic removal.
Activated alumina also
removes selenite, fluoride, sulfate and chromate
which may be other undesired contaminants in the
water supply.
Ion Exchange
This is a special form of
adsorption involving the reversible displacement
of an ion adsorbed onto a solid surface by a
dissolved ion. Ion exchange resins are based on
a cross linked polymer skeleton, called the
matrix. Most commonly, this matrix is composed
of polystyrene cross-linked with divinylbenzene.
Charged functional groups are attached to the
matrix through co-valent bonding.
What are the types of
functional groups which can be attached to the
polystyrene?
-
strongly acidic groups,
such as sulfonate
-
weakly acidic groups,
such as carboxylate
-
strongly basic groups,
such as quaternary amines
-
weakly basic groups,
such as tertiary amines Other forms of
adsorption involves stronger bonds and are
less easily reversed
Various strong base anion
exchange resins are commercially available which
can effectively remove arsenate from solution.
Arsenite, being uncharged is not removed.
Therefore, unless arsenic is present exclusively
as arsenate, an oxidation step becomes a
necessary precursor to arsenic removal
Role of Alumina in Arsenic Removal
During coagulation and
filtration using alumina as the metal salt
arsenic is removed through three main
mechanisms:
-
precipitation – the
formation of the insoluble compound Al(As04)
-
co-precipitation – the
incorporation of soluble arsenic species
into a growing metal hydroxide phase
-
adsorption – the
electrostatic binding of soluble arsenic to
the external surfaces of the insoluble metal
hydroxide.
All three of these
mechanisms can independently contribute towards
arsenic removal from source water.
Physical Exclusion
Selectively permeable
synthetic membranes are commercially available
allowing certain dissolved compounds to go
through the membrane while excluding other
compounds.. These membranes can act as a
molecular filter to remove dissolved arsenic,
along with many other dissolved in particulate
compounds. Two classes of membrane filtration
are low pressure membranes such as
microfiltration and ultrafiltration and high
pressure membranes such as nanofiltration and
reverse osmosis. Low pressure membranes operate
at 10-30 psi and have large pore sizes, while
higher pressure systems run at 75 to more than
250 psi and have smaller pore sizes with tighter
membranes. Arsenic removal is independent of pH
and the presence of other solutes in the source
water.
What about the use of metal ions to trap
arsenic?
Iron, copper, manganese,
aluminum, calcium and magnesium as metal ions
have been used in an attempt to trap and remove
arsenic species from drinking water as their
insoluble salts.
The problem is that metal
salts of arsenic III and arsenic V have widely
different solubilities
Arsenic V salts are less
soluble than arsenic III salts – however, recall
that it is the arsenic III compounds which are
the more dangerous
Calcium ions and hydrogen
carbonate ions are abundant in well water. When
well water is exposed to air carbon dioxide is
lose and calcium carbonate precipitates. Iron II
ions are oxidized by oxygen forming iron III
hydroxide which precipitates with calcium
carbonate. Large amounts of aqueous arsenic
species are adsorbed by iron III
hydroxide/calcium carbonate mixtures as they
precipitate. In this setting half of the arsenic
III and nearly all the arsenic V are removed.
Iron and manganese can
result in significant arsenic removal through
coprecipitation and sorption onto ferric or
manganic hydroxides. The mechanism is the same
as coagulation and filtration.
THINK ALUMINA -- THINK DYNAMIC