Evaluation of a sequential extraction process used for
determining mercury binding mechanisms to coal combustion
byproducts.
by Noel, James D.^Biswas, Pratim^Giammar, Daniel E.
ABSTRACT
Leaching of mercury from coal combustion byproducts is a concern
because of the toxicity of mercury. Leachability of mercury can be
assessed by using sequential extraction procedures. Sequential
extraction procedures are commonly used to determine the speciation and
mobility of trace metals in solid samples and are designed to
differentiate among metals bound by different mechanisms and to
different solid phases. This study evaluated the selectivity and
effectiveness of a sequential extraction process used to determine
mercury binding mechanisms to various materials. A six-step sequential
extraction process was applied to laboratory-synthesized materials with
known mercury concentrations and binding mechanisms. These materials
were calcite, hematite, goethite, and titanium dioxide. Fly ash from a
full-scale power plant was also investigated. The concentrations of
mercury were measured using inductively coupled plasma (ICP) mass
spectrometry, whereas the major elements were measured by ICP atomic
emission spectrometry. The materials were characterized by X-ray powder
diffraction and scanning electron microscopy with energy dispersive
spectroscopy. The sequential extraction procedure provided information
about the solid phases with which mercury was associated in the solid
sample. The procedure effectively extracted mercury from the target
phases. The procedure was generally selective in extracting mercury.
However, some steps in the procedure extracted mercury from nontarget
phases, and others resulted in mercury redistribution. Iron from
hematite and goethite was only leached in the reducible and residual
extraction steps. Some mercury associated with goethite was extracted in
the ion exchangeable step, whereas mercury associated with hematite was
extracted almost entirely in the residual step. Calcium in calcite and
mercury associated with calcite were primarily removed in the
acid-soluble extraction step. Titanium in titanium dioxide and mercury
adsorbed onto titanium dioxide were extracted almost entirely in the
residual step.
INTRODUCTION
Mercury, once emitted, can remain airborne for 0.5-2.0 yr before
depositing onto soil or surface waters. (1) Once deposited on soils or
water bodies, mercury is persistent and may bioaccumulate in ecosystems.
(2) In the United States, approximately 30% of the total mercury emitted
by anthropogenic sources comes from coal-burning utilities. (3) Although
mercury is a trace metal found in coal varying with rank in the range of
0.01-3.3 parts per million by weight, mercury emission from coal
combustion is substantial because of the large quantity of coal used
every year. (3)
The U.S. Environmental Protection Agency issued the Clean Air
Mercury Rule (CAMR) on March 15, 2005, which will reduce total mercury
emissions from coal burning utilities in the United States through a
market-based cap and trade system. The CAMR will reduce mercury
emissions from 48 t/yr to 38 t/yr by 2010 during the first phase of
implementation and to 15 t/yr by 2018 in a second phase of reductions.
(4) Sorbent addition to coal combustion processes has the potential to
remove mercury and has been shown to effectively capture gaseous
mercury, suppress the fraction in the solid phase, and transform it to
an environmentally benign form. (5,6) Potential sorbents for mercury
capture include activated carbon-based sorbents and inorganic sorbents.
Inorganic sorbents include silica, titania, alumina, aluminosilicates,
and calcium-based compounds. (7-9) Titanium dioxide is an inorganic
sorbent that can capture mercury after photo-catalytic oxidation of
[Hg.sup.0] under ultraviolet (UV) irradiation. (10) When sorbents are
used, the mercury is transferred from the gas phase to solid phases that
are collected with the fly ash or as separate byproducts. Elemental
mercury does not partition significantly to the particulate phase, and
oxidation either in the gas phase or at the particle surface is
necessary for mercury capture (11,12); consequently, this study focuses
on the sequential extraction of mercury (II). The solid-phase speciation
of mercury in combustion byproducts dictates its leachability to the
environment and can be investigated using sequential extraction
techniques. (13)
Sequential extractions furnish information about the origin, mode
of occurrence, bioavailability, and mobility of trace metals in solid
samples. (14,15) The mobility of heavy metals depends on the
characteristics of the solid, the strength of bond between the heavy
metal and the solid matrix, and the composition of the leaching
solution. (16) Sequential extraction is a technique in which a series of
chemical solutions is applied to one solid in succession. Elements
associated with a solid material can be partitioned into specific
fractions by selective extraction with appropriate reagents. (14) Each
sequential extraction procedure is designed to differentiate among
metals bound to different solid phases and mineral fractions. (17) The
materials investigated in this study were goethite ([alpha]-FeOOH),
hematite ([alpha]-[Fe.sub.2][O.sub.3]), calcite (CaC[O.sub.3]), mercury
oxide (HgO), and a titanium dioxide mixture of anatase and rutile
([alpha]-Ti[O.sub.2] and [beta]-Ti[O.sub.2]). These phases, with the
exception of [alpha]-FeOOH, are all found in coal combustion fly ashes.
On a mass basis, iron oxides may comprise as much as 16% of the fly ash,
carbonates such as CaC[O.sub.3] as much as 22%, and titanium comprises
approximately 1% and may be present as Ti[O.sub.2]. (18-20)
[alpha]-FeOOH was investigated to compare mercury binding mechanisms
between different iron minerals. Investigation of mercury binding
mechanisms to mercury-laden materials and titanium dioxide (a potential
inorganic sorbent) yields information about the future mobility of
mercury in the environment and indicates the capability of each material
to sequester mercury.
Each phase can retain heavy metals by mechanisms including ion
exchange, outer- and inner-sphere complexation, precipitation, and
coprecipitation. The potential mechanisms are illustrated in Figure 1.
Precipitation (mechanism 1) involves the formation of discrete
mercury-containing solid phases on the sorbent surface. Chemical
adsorption (mechanism 2) to the surface involves the formation of
chemical bonds between mercury atoms and reactive functional groups on
the sorbent surface. Electrostatic adsorption (mechanism 3) is a form of
physical adsorption in which mercury ions are bound to the surface
through electrostatic adsorption and not through coordination to any
specific sites on the sorbent surface. Encapsulation (mechanism 4)
involves the incorporation of mercury within the solid matrix through
either substitution of mercury for another cation or the formation of
domains of discrete mercury-containing solid phases within the matrix of
another solid. Encapsulation is different from the partitioning of
mercury to surfaces that may be present within the interior of porous
sorbents; such partitioning would occur through a process of surface
precipitation or chemical or physical adsorption. The mercury extracted
in the steps of a sequential extraction procedure can be related to the
targeted mercury fraction and binding mechanisms.
The goal of sequential extraction is to convert the heavy metals
bound to certain phases into soluble forms within the extractant
solution. (16) Careful selection of the extractant solutions is required
to differentiate among phases and binding mechanisms. In each sequential
extraction, extractants are applied in order of increasing
aggressiveness, such that the successive fractions obtained correspond
with metal associations of lesser mobility. Common extractants used in
sequential extraction schemes generally fall into the following groups:
unbuffered salts, weak acids, reducing agents, oxidizing agents, and
strong acids. (16) Two commonly used procedures are the Tessier and the
European Community Bureau of Reference (BCR) (proposed in 1993 by the
European Community's Bureau of References, now called the
Standards, Measurements and Testing Programme) sequential extraction
processes. (14,21) Researchers have made modifications to these
sequential extraction schemes based on the solid material studied, the
phases of interest, and the trace metals in question. (15-17,22-28)
[FIGURE 1 OMITTED]
Both the sequential extraction process and the toxicity
characteristic leaching procedure (TCLP) provide information regarding
the leachability of trace metals. The TCLP is a standard method used to
simulate the leaching of metals from solids within the moderately acidic
environment of a municipal landfill. The TCLP uses a solution of 0.5 M
sodium acetate and 0.5 M glacial acetic acid (pH = 4.9 [+ or -] 0.1),
(22) which is similar to the acid soluble step used in this study.
However, the sequential extraction process provides leachability
information under additional conditions. In particular, the reducing
extraction step simulates the reducing conditions of a municipal
landfill better than the TCLP alone. Sequential extraction processes
warrant further investigation and could supplement the TCLP in
determining the leachability of toxic metals.
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