Environ. Sci. Technol. 1999, 33, 1110-1115
draining and evaporation. The main chemical reactions
Municipal Solid Waste Incineration
Bottom Ash: Characterization and
Kinetic Studies of Organic Matter
involved in the transformation of MSWI bottom ash inorganic
matter are the oxidation of scrap iron (highly exothermal),
the hydroxylation of metals, the carbonation of alkaline and
alkaline earth metals, and the dissolution of lime and calcium
sulfate (3). Few published studies (5) have dealt with changes
in organic matter during aging, as well as the role of
microorganisms, even though the MSWI bottom ash milieu
S . D U G E N E S T , * , † J . C O M B R I S S O N , ‡
†
H . C A S A B I A N C A , A N D
M . F . G R E N I E R - L O U S T A L O T
(
water, temperature, pH, organic matter) seems able to
†
support bacterial development. The presence of metals can
also preferentially favor the growth of some bacterial species.
Microorganisms could thus act on the MSWI bottom ash,
particularly on the organic matter via oxidation or dehy-
drogenation reactions of organic components (6).
Service Central d’Analyse, Centre National de la Recherche
Scientifique, USR 059, BP 22, 69390 Vernaison, France, and
Laboratoire d’Ecologie Microbienne du Sol, UMR-CNRS 5557,
Universit e´ Claude Bernard-Lyon I, 69622 Villeurbanne, France
Consequently, we investigated changes in organic matter
related to the development of microorganisms in the milieu
during aging. Two conditions of aging were tested: in
conditions existing at the industrial scale (open pile of 300
tons) and in controlled conditions at the laboratory scale
Bottom ash is the main solid residue (in weight) which is
produced by municipal solid waste incineration (MSWI)
facilities. To be reused in public works, it has to be stored
previously a few months. This material is composed
primarily of a mineral matrix but also contains unburnt
organic matter. The mineral content and its change in the
course of aging are relatively well-known, in contrast
with the organic content. So in order to detect the phenomena
responsible for changes in organic matter and their
effects during aging, the concentrations of the main organic
compounds previously characterized, the number of
microorganisms, and the release of carbon dioxide were
followed kinetically (over 13 months) in model laboratory
conditions (mass, particle size, humidity, temperature,
aerobiosis). The results showed that the aging process
led to the natural biodegradation of the organic matter
available in bottom ash, composed essentially of carboxylic
acids and n-alkanes (steroids and PAH’s to a lesser
extent), and consequently that it would improve the bottom
ash quality. Furthermore these results were confirmed
by the study of aging conducted in conditions used in the
industrial scale (over 12 months).
(
aerobiosis, temperature 30 or 70 °C, 80 or 160 g samples).
Laboratory simulation of aging for 13 months enabled us to
kinetically follow the concentrations of target organic
compounds, the number of microorganisms, and the release
of carbon dioxide (at 30 °C). The latter is a significant marker
of the oxidation of organic compounds by microorganisms
in MSWI bottom ash during aging. Concerning aging in in
situ conditions, only the kinetics (for 12 months) of organic
compounds could be done.
In both situations of aging, mechanisms involved in
organic matter changes could be suggested.
An analytical methodology was first developed to identify
and quantify organic components of MSWI bottom ash,
involving two extraction techniques: supercritical fluid
extraction (SFE) and hot solvent extraction (Soxtec). The
samples recovered were analyzed by using two state-of-the-
art analytical tools: gas chromatography coupled to a mass
spectrometry detector (GC-MSD) and gas chromatography
with microwave-induced plasma atomic emission detection
(
GC-MIP-AED).
Conventional techniques were used to enumerate mi-
croorganisms in solid media: both direct counting using a
fluorochrome and an indirect plate counting involving
bacterial growth (7).
Introduction
Experimental Section
In France, 37% of the municipal solid waste are eliminated
by incineration with or without energy recovery (1). Municipal
solid waste incineration (MSWI) produces large quantities
of bottom ash (2.7 milliontons/ year) as solid residue. MSWI
bottom ash is composed primarily of silica, metal oxides,
silicates, chlorides, and sulfates, but also contains nonneg-
ligible concentrations of heavy metals including Zn, Pb, Cu,
Ni, Cr, and Cd, and small amounts of unburnt organic matter
MSWI Bottom Ash Sam pling. The nature of MSWI bottom
ash is closely linked to the nature of the solid waste, the type
of incinerator, and the combustion conditions. We have
selected one facility having a high incineration capacity and
consequently producing high amounts of bottom ash.
The facility is located near an urban area. As a result of
the French customs (1), municipal solid waste include paper-
cardboard (30%), fermentable matter (25%), glass (12%), fines
(
2). In some European countries, bottom ash can be used in
(
10%), plastics (10%), metal (6%), textiles (2%), and undefined
road building, but has to be stored a few months before
reuse (1). Published data indicate that the aging process leads
to an overall improvement in the environmental qualities of
MSWI bottom ash (3-5). It has been shown that aging reduces
the leaching of heavy metals and total organic carbon in
parallel to a decrease of pH from highly alkaline to nearly
neutral values (5). This is done by stockpiling large amounts
of MSWI bottom ash in the open air, which allows some
materials (5%) (mean composition). The nature and the
volume of solid waste are relatively constant from day to
day.
The incinerator is one of the most common type of MSWI
system in use today. It has been operated since 1989, and its
rated incineration capacity is 12 tons/ h. Before combustion,
solid waste were not preprocessed to remove materials
including ferrous or nonferrous metals and glass. They were
fed into the combustion chamber via gravity and transported
through the furnace via a system consisting of six rollers
disposed on a slightly inclined plane. Inside the furnace, the
air supply was controlled, and the gas temperature reached
*
Corresponding author phone: 04-78-02-22-55; fax: 04-78-02-
7
1-87.
†
‡
Centre National de la Recherche Scientifique.
Universit e´ Claude Bernard-Lyon I.
1
1 1 0
9
ENVIRONMENTAL SCIENCE & TECHNOLOGY / VOL. 33, NO. 7, 1999
10.1021/es980193e CCC: $18.00
1999 Am erican Chem ical Society
Published on Web 04/01/1999