Use of heavy metal
resistant bacteria in a bioreactor concept (bacteria metal sludge reactor) to
remove bioavailable heavy metals from polluted soils.
D. van der Lelie*, P. Corbisier, S.
Taghavi, M. Mergeay, M. De Smet, L. Hooyberghs, L. Kinnaer, L. Diels (Vlaamse Instelling
voor Technologisch Onderzoek-VITO, Environmental Technology, B-2400 Mol,
Belgium, Tel: +32-14-335166, Fax: +32-14-580523, e-mail: vdlelied@vito.be); N. Spelmans, J. Vangronsveld (Limburgs Universitair Centrum-LUC,
Center for Environmental Sciences, B-3590 Diepenbeek, Belgium); G. Brox (Tekno
Associates, Salt Lake City, USA)
A patented system (Diels et al., 1992), called Bio Metal Sludge Reactor (BMSR) consists of a
continuous stirred tank reactor that is fed with contaminated soil to which
water and nutrients are added. During the start-up period Ralstonia metallidurans CH34 was added to the slurry, which allowed
the contaminating metals to be transferred from the soil particles to the bacterial
cell walls. The bacterium has special properties, which makes that the settling
of the bacteria goes only very slowly compared to the soil organic and clay
particles. This allows the separation between the soil and the metal loaded
bacteria in a settling device. After treatment, the Cd concentration is reduced
from 5 mg/kg dry soil to concentrations below 1 mg Cd/kg soil. The measurement
of bioavailability of the heavy metals gives a reduction of a factor 10.
Historical
emissions of old non-ferrous factories in the neighbourhood of the VITO in the
Kempen lead to large geographical areas (>100 km² with Cd concentrations
higher than 3 mg/kg soil) of contaminated sites. The only possible remediation
methods are based on concentration and subsequent removal. Besides
physico-chemical techniques, biotechnology offers some interesting
possibilities. The solubilization of metals from soil, sludge or solid waste
can be done via autotrophic or heterotrophic leaching, the use of metallophores
or by chemical leaching followed by microbial treatments. Metals displaced in
this way into the water phase or metals already available in wastewater can be
desolubilized via biological induced adsorption, precipitation and
transformation or complexation processes. In this case study, the heavy metal
resistance, bioprecipitation capacity and improved soil flocculation
characteristics of Ralstonia
metallidurans CH34 lead to the development of a bioremediation method for
heavy metal contaminated soils.
Bacterial strains
Heavy
metal resistant bacteria were obtained by selection on Tris-minimal medium
(Schlegel et al., 1961) with one of
the following added metals: 0.8 mM Cd or Cu, 2.0 mM Zn, Ni or Co. The Alcaligenes eutrophus strain CH34, now
called Ralstonia metallidurans, was
used as starter culture for the BMSR reactor. This strain is considered as a
model system for bacterial interactions with heavy metals in the environment
(Taghavi et al., 1997). An
interesting characteristic of strain CH34 is a removal of Cd or Zn ions from
the solution during the late log phase and the stationary phase (Diels, 1990).
This accumulation and precipitation is correlated with the concentration and
kind of carbon source, with the progressive alkalinization of the medium and
appears to be associated with the outer cell membrane. In this way a
crystallisation process is induced on the cells and this will lead to a very
high metal to biomass ratio (between 0.5 and 5.0).
Soil
Slightly contaminated sandy garden soils from the Kempen region in the
north of Belgium were used. The Cd concentrations were in the range between 5
and 20 mg/kg. The soil was sieved to remove coarse materials. As it was
observed that as well the fine as the coarse fraction contained high metal
concentrations the soil was passed in an attrition cell before BMST treatment.
2.3. Soil slurry reactor
The
characteristics and the operation of the BMSR soil slurry reactor were recently
described by Diels et al (1999). The
BMSR concept is presented in Fig. 1.

Fig. 1. General overview of
the BMSR concept.
Heavy metals bioextraction
The
very coarse fraction (larger than 2 mm) of the soil contained very high
concentrations of metals, especially of Cd. This fraction was removed as waste
material. The fractions smaller than 2 mm were pumped into the 450BLA slurry
reactor. The input concentration and output concentrations are presented in
table 1. The concentration in the reactor (MKSR) increased due to the attrition
and the increase in availability from 3.5 mg Cd/l to 5.0 mg Cd/l. The output
metal concentration was measured after the settling of the soil and the removal
of the water, containing the bacteria loaded with heavy metals. After a few
repetitions (MKS06) of the treatment the metals concentration went down to 63
mg Zn/kg, 0.5 mg Cd/kg, 47 mg Pb/kg and 4 mg Cu/kg (Table 1). The Cd
concentration was reduced from 5.0 mg Cd/kg to 0.5 mg Cd/kg dry soil, which is
a 10 times reduction and below the flemish soil remediation standard of 1.0 mg
Cd/kg dry soil.
Table 1. Metals concentration
in the input and output of the BMSR reactor
|
Sample |
Zn |
Cd |
Pb |
Cu |
|
MKSLF |
471 |
8.0 |
384 |
66 |
MKSI
|
278 |
3.5 |
240 |
29 |
|
MKSR |
344 |
5.0 |
215 |
32 |
|
MKSO2 |
194 |
2.8 |
167 |
21 |
|
MKSO4 |
128 |
1.5 |
103 |
12 |
|
MKSO5 |
100 |
1.0 |
67 |
7 |
|
MKSO6 |
63 |
0.5 |
47 |
4 |
Metal
concentrations are expressed in mg metal/kg dry soil. MKSLF: fraction > 2
mm; MKSI: input soil (< 2 mm); MKSR: soil in the reactor; MKSO: output soil.
Water
and biosludge
After
settling of the soil the water with the metal loaded biosludge was removed and
pumped to a decantation tank. Table 2 presents the heavy metal content before
and after flocculation for the process water of MKS06. The flocculation could
reduce the metal concentration with a factor 10. The heavy metals concentration
in the biosludge is presented in table 3.
Table. 2. Heavy metals
concentrations in the process water before and after flocculation.
|
Heavy metal |
Before flocculation |
After flocculation |
Zn
|
3.7 |
0.3 |
|
Cd |
0.06 |
0.00 |
|
Pb |
3.5 |
0.2 |
|
Cu |
0.4 |
0.03 |
Heavy
metals concentrations are presented in mg metal /l process water.
Table
3. Heavy metals content in the biosludge
|
Sludge |
Zn |
Cd |
Pb |
Cu |
|
MKB5 |
4590 |
80 |
2840 |
421 |
|
MKB7 |
4390 |
78 |
3150 |
427 |
|
MKB8 |
4560 |
86 |
3560 |
438 |
Heavy metals
concentrations are presented in mg metal/kg dry sludge.
Heavy
metals bioavailability
Heavy metals
bioavailability was measured with the BIOMET-biosensor (Corbisier et al., 1996; 1999). The availability is
expressed as a signal to noise ratio. An S/N below 2 is recognised as no
bioavailability of heavy metals. The total soil had a S/N of 36.1. The fraction
> 2 mm had a S/N of 50.1 and the fraction < 2mm (fraction added to the
reactor) had a S/N of 25.4. The treated
soil had a S/N between 0.2 and 2.9 which means a reduction of at least 10 times
compared to the input value and a reduction to nearly no presence of
bioavailable Cd or Zn. The
indication of bioavailability by the BIOMET sensor was also supported by plant
and earthworm tests (results not shown). In some cases shortly after the start
of the treatment process an increase in the bioavailable metal fraction is
observed. This is due to the shearing forces and attrition that makes the bound
metals more available. Afterwards the metals are transferred to the bacteria
and in that way removed from the soil.
The
BMSR approach shows a soft soil treatment technology in a way that the soil
treated with bacteria at neutral pH can be reused. The treatment of heavy
metals contaminated soil by Ralstonia
metallidurans CH34 allows the contaminating metals to be transferred from
the soil particles to the bacterial cell walls. The bacterium has special
properties, which makes that the settling of the bacteria goes only very slowly
compared to the soil organic and clay particles. This allows the separation between
the soil and the metal loaded bacteria in a settling device. Once the metal
loaded bacteria are separated from the soil the bacteria can easily be removed
from the water suspension by either flotation or a flocculation process. A
highly contaminated biomass is obtained from the treatment process. The biomass
contains between 8 and 25 g Zn/kg, 3-5 g Pb/kg and 160-250 mg Cd/kg. This
biomass can be incinerated in a pyrometallurgical treatment. A highly metal
loaded ash will be obtained. The metal oxides can be leached for reuse or the
ash can be dumped in a landfill.
The
presented method can be used for the removal of metals from sandy soils.
Removal of metals from clay soils is not successful or worthwhile.
Concentrations of Cd up to 70 mg Cd/kg soil can be removed to below 3 mg Cd/kg.
Simultaneously the metals Zn, Cu and Pb are removed and mostly brought to below
normal standards. The process water contained only very low heavy metals
concentrations (< 0.1 mg Cd/l) and could be recycled in the system.
This
project was supported by the European Fund for Regional Development (EFRO) and
by the Public Authorities of Flanders for Waste (OVAM).
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