22
Feature
Filtration+Separation
December 2 0 0 5
Dioxin removal:
Adiox
for wet
scrubbers and
dry absorbers
diox is an innovative technology for removing toxic dioxins from
gases. Tower packings, droplet separators and fixed bed fillings
A
can be made of this dioxin absorbing material. Sven Andersson,
Siegfried Kreisz and Hans Hunsinger discuss the use of this
novel technology under wet and dry conditions.
Innttrroodduuccttiioonn I
Addiiooxx:: ccaarrbboonn ffiilllleedd ppllaassttiiccss A
incomplete flue gas burnout. The dioxins
are absorbed in the construction materials
There are a number of technologies available
The background for inventing
Adiox
resulted
of the flue gas cleaning system during the
for removing or destroying dioxins from
from an observation that plastics can absorb
start-up phase, but are desorbed during the
gases, such as baghouse filters and catalysts.
large amounts of dioxins from gases*; these
following period of normal operation. This
The investment and/or running costs of these
can later be desorbed.
desorption can lead to increased emissions
technologies are usually very high.
This absorption/desorption equilibrium is
over a very long time range.
Adiox
(patent pending) is a new dioxin
known as the
Memory Effect
(
see figure 1a
).
Adiox
was developed to avoid the dioxin
removal technology that has established itself
as an efficient and economic way to reduce
A situation where the
Memory Effect
plays
desorption described above*. The
Adiox
dioxin emissions, and is marketed and sold by
an important role is during the start-up of
material consists of a polymer, such as
Götaverken Miljö AB
as material deliveries,
an incineration unit, when large amounts of
polypropylene (PP) - containing carbon
package units or turn key flue gas treatment
dioxins are formed due to unstable
particles. The dioxins are first absorbed in
systems.
combustion conditions characterised by an
the polymer. Then they diffuse to the surface
Figure 1(a): Schematic view of absorption/desorption in plastic
Figure 1(b): Schematic view of absorption/adsorption in Adiox (plastic containing
carbon particles)
Feature
23
Filtration+Separation
December 2 0 0 5
The use of
Adiox
tower packing as a
“police” filter in a scrubber - downstream of
a primary dioxin removal system such as a
baghouse filter - results in additional
security to guarantee low emission values.
In this case,
Adiox
increases the margins in
the case of, for example, carbon dosage
failure, filter leakage or increased dioxin
concentrations during start-up.
Adiox
has been installed in scrubbers with
additional carbon injection (
at AVR Avira,
Netherlands
) as well as in a MercOx-
scrubber, downstream of a baghouse filter
with carbon injection (
at a hazardous
waste incineration facility at Sakab,
Sweden
).
At
Måbjergværket
(
see figure 2 on page 23
),
wet
Adiox
scrubbers in combination with one
electrostatic precipitator (ESP) per line have
Figure 2: Adiox has been in operation as a primary dioxin removal system at Måbjergværket (Denmark)
acted as the main dioxin filter since the fall
since the fall of 2004. All measurements are far below the 0.1 ng TEQ/Nm3.
of 2004. The eleven dioxin measurements
performed so far show that the
concentrations in the stack are permanently
of the carbon particles, where they are
different modifications of
Adiox
to the high
far below the emission limit of 0.1 ng
irreversibly adsorbed (
see figure 1b
). The
dioxin concentration of 8 ng TEQ/m3 (n.,
TEQ/m3 (n., d.g.).
polymer acts as a selective barrier, which
dry gas). The high absorption capacity of
protects the carbon from adsorption by other
Adiox
was thereby demonstrated.
Flue gas condensation for energy recovery is
contaminants such as Mercury (Hg.)
also integrated in the system. The required
Further research was done at a
second
amount of
Adiox
material is typically larger
Several types of components, such as tower
installation in Kolding (Denmark)
, where a
than for a traditional scrubber, and is
packings, demisters (droplet separators) and
pilot
Adiox
scrubber was operated to develop
fixed bed fillings can be produced from
Adiox
and demonstrate the concept of using
Adiox
determined on the basis of the dioxin
material. By applying
Adiox
tower packings in
as the main dioxin filter.
concentration after the electrostatic
existing wet scrubbers (gas-liquid contactor)
precipitator.
The impressive results of this pilot plant
the dioxin emissions are efficiently reduced
have lead to the
first full scale installation
and the
Memory Effect
is almost completely
at Måbjergværket (Denmark)
, using only
avoided.
What are Dioxins?
Adiox
for dioxin reduction (
see below
.)
The dioxin removal capacity of
Adiox
tower
Dioxins, or polychlorinated dibenzo-p-
Adiox
is particularly well suited for removing
packings and demisters is favoured by the large
dioxins and -dibenzo furans
dioxins from gases including municipal solid
(PCDD/Fs), are a group of persistent
specific surface area, selectivity for dioxins and
waste incineration, hazardous waste
and extremely toxic chlorinated organic
high absorption capacity.
incineration, chemical and biomass
compounds. Major emission sources
The expected life time of the
Adiox
material is
industries;
Adiox
has been successfully
are known to be processes like waste
2-4 years, depending on the application. After
installed in all of these application fields.
incineration, metal production, bio-fuel
usage, the dioxins are destroyed by incinerating
incineration and uncontrolled
Another application area is the metal
the loaded material.
combustion. Under stationary effective
industry, where several potential installations
combustion conditions, dioxins are
have been identified and are currently being
355 iinnssttaallllaattiioonnss iinn 44 yyeeaarrss 3
almost completely destroyed during
discussed.
incineration, but are re-formed during
Adiox
has been installed at more than 35 full
the cooling of the flue gas* and during
scale incineration lines within three years,
Addiiooxx iinn wweett ssccrruubbbbeerrss A
dust separation at temperatures above
since its market introduction in 2002. The
200 °C by de-novo synthesis*. A review
Adiox
allows the design of multifunctional
gas flows of these plants range from 5,000 to
of the formation mechanisms involved
wet scrubbers, where HCl, HF, SO
2 and
is given by Tuppurainen et al*.
180,000 m3/h (normal, wet gas).
oxidised Hg as well as dioxins can be
removed simultaneously. Elemental Hg can
Dioxin concentrations are commonly
The first full-scale test installation was
be oxidised and captured in the scrubber
reported as toxic equivalents (TEQ),
performed at the
municipal solid waste
which is the sum of the congener
incineration plant of Thisted (Denmark)
in
using the MercOx process*, which can also
concentrations multiplied by their
2001, where the existing tower packings were
be combined with
Adiox
.
specific TEQ-factors. The extreme
replaced with the
Adiox
material.
Extended energy recovery using
toxicity of 2,3,7,8-Tetra-CDD (also
A constant removal efficiency of 70% was
condensation of the flue gas can be
known as Seveso-dioxin) is the
reference and has a TEQ-factor of one.
maintained for one year, after the limited
integrated into the scrubber as well.
Dioxins and furans with larger numbers
amount of
Adiox
tower packing had been
Adiox
is easy to install in existing wet
of chlorine atoms (including the 2-, 3-,
installed in the existing scrubbers*.
scrubbers. The circulation of the scrubber
7- and 8-positions) have lower TEQ-
A material optimisation program was carried
liquid keeps the material clean from dust
factors.
out in parallel at the plant, by exposing
deposits.
24
Feature
Filtration+Separation
December 2 0 0 5
Using
Adiox
material instead
of carbon pellets would not
have these disadvantages.
The design of the absorber
can be kept simple, since no
material dosing systems are
required. Granular beds
have porosities around 30%.
If the gas contains particles,
parts of the bed may be
clogged, leading to
channelling and increased
pressure drop. Tower
packings, originally designed
for the use in wet scrubbers,
can be used instead. The
porosity is typically 95%,
which reduces the risk for
clogging. Intermittent
rinsing may be used to clean
the surface during operation.
A simple, cost-effective
pollution control system
can be obtained by
Figure 3: A compact state-of-the-art air pollution control system consisting of ESP, wet scrubber and dry Adiox absorber.
combining an ESP, a
multi-functional wet
Adiox
scrubber and a dry
Adiox
A
Addiiooxx iinn ddrryy aabbssoorrbbeerrss
efficiency per installed amount is higher,
absorber (
see figure 3 above
).
since the water film in a wet scrubbing
Using
Adiox
in a dry absorber instead
A dry pilot absorber, using
Adiox
tower
process poses a mass transfer limitation for
would have the effect of making the
packings, was installed
at line 1 of the Renova
the dioxins. Less material is thereby
installation more compact. The initial
municipal waste incinerator in Göteborg
required for the same removal efficiency.
laboratory tests with
Adiox
were performed
(Sweden)
. The flue gas treatment consists of
Fixed bed carbon filters are sometimes used
with dry gas. The full-scale installations
an ESP, two wet scrubbers, reheater and a
as a final dioxin removal stage.
made so far, however, have been carried out
baghouse filter as seen in
Figure 4
.
in wet scrubbers.
There is a risk of fire in these filters, and
The second scrubber is used for enhanced
If
Adiox
is employed in a dry absorber
contaminated dust particles may escape during
energy recovery with flue gas condensation
instead of a wet scrubber, the removal
operation or on handling of carbon pellets.
by cooling the gas from 60 to 40°C using
heat pumps during the cold
season. The gas is reheated
to typically 60-80°C. The
pilot absorber operates with
a fraction of the total gas
flow (approximately 3000
m3/h) extracted after the
reheater. Today, SO
2 and
dioxins are removed in the
baghouse filter.
The pilot experiments
demonstrate the possibility
of removing the dioxins in
a dry
Adiox
absorber instead
of a baghouse filter. In such
a case, SO
2 could be
removed in the wet
scrubbers.
The inlet concentrations
ranged from 0.7 to 2.0 ng I-
TEQ/m3 (n, d.g., 11% O2),
and the clean gas
concentrations ranged from
0.002 to 0.02 ng I-TEQ/m3
Figure 4: Pilot Adiox absorber at the Renova municipal waste incineration plant in Göteborg, Sweden. The dry Adiox absorber is
located downstream of an ESP, wet scrubbers and re-heater. The removal efficiency was higher than 97.5% in all measurements
(n, d.g., 11% O
2). No
with this configuration.
trend of decreasing removal
Feature
25
Filtration+Separation
December 2 0 0 5
efficiency with time could be seen. All
C
Coonncclluussiioonn
*Contact author or the editor for details of
measured particle associated dioxins were
references
Adiox
is very well suited for selective
<<0.1 ng TEQ/Nm3 in this plant.
absorption of dioxins and has a high loading
capacity.
C
Coonnttaacctt
The highest temperature during the tests
Sven Andersson (corresponding author)
was 90 °C Initial tests have been made with
It can be integrated in new or existing wet
Götaverken Miljö AB
glass fibre filled
Adiox
in order to guarantee
scrubbers without the need for additional
Box 8876, SE-402 72 Göteborg
equipment.
dimensional stability of the packings at
Sweden
Tel: +46 31 501960
even higher temperatures.
Using the material in a dry absorber can
Fax: +46 31 229867
decrease equipment sizes due to the higher
One important consideration for the pilot test
E-mail: sven.andersson@gmab.se
efficiency per volume.
Website: www.gmab.se
was to assess the amount of fly ash collected on
It is effective even during start-up and in
the
Adiox
surface during operation. No rinsing
stationary operating conditions, where other
Siegfried Kreisz & Hans Hunsinger
of the tower packings was therefore made
Forschungszentrum Karlsruhe GmbH
technologies may not work optimally. Other
during the test.
advantages are:
ITC-TAB, PO Box 3640
DE-76021 Karlsruhe
After 9 months, the
Adiox
tower packings
• Ease of installation;
Germany
were covered by a thin, porous layer of
Tel: +49 7247 822656
• A reduction (or even avoidance) of the
Fax: +49 7247 824373
particles, which could easily be removed by
Memory Effect
E-mail: info@oea.fzk.de
rinsing with water. No change in pressure
Website: www.fzk.de
• Multifunctional HCl, HF, SO2 removal,
drop or decrease in removal efficiency with
and condensation;
time could be seen during the whole period.
C
Caallll ffoorr PPrroodduucctt RReevviieeww AArrttiicclleess aanndd
• A high porosity - low clogging risk;
F
Feeaattuurreess::
The aim of this pilot installation was to
• Clean handling and no “hot-spots”;
If your company’s products have been
demonstrate how the complete dioxin
tested by an independent, objective
removal can be achieved in a static,
• No final residue (PCDD/Fs are destroyed
source, we may be interested in
by incineration);
compact and robust piece of equipment
publishing the results. Email details to
downstream of a conventional flue gas
• A simple, static system with high
d.hopwood@elsevier.com
cleaning system.
availability.
•
N
E
NANOFILTRATION: PRINCIPLES AND APPLICATIONS
W
!
Published: January 2005
Edited by Andrea Schaefer, University of Wollongong, Australia, Anthony Fane,
and T. David Waite, both of the University of New South Wales, Australia
Hardback
ISBN: 1-85617-405-0
Covering all aspects from materials to non-aqueous applications, this is the only book to
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Pages: 560
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Chapter 10: Water treatment
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Chapter 17: Nanofiltration bioreactors
Chapter 22: Conclusion; Index
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