industry and environment - DTIE
industry and environment - DTIE
industry and environment - DTIE
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Chemicals management<br />
Annual energy export is approximately 160 GWh<br />
as district heating <strong>and</strong> 50 GWh as electricity.<br />
The off-air plant<br />
Even very low concentrations of volatiles will<br />
often create unacceptable odours, causing inconvenience<br />
with respect to the internal <strong>and</strong> (if the<br />
odours are strong) external <strong>environment</strong>. To deal<br />
effectively with local emissions of volatiles (e.g.<br />
hydrocarbons from unloading activities, processes<br />
in one of the drum-emptying plants), an “off-air<br />
plant” was established in 1993 (Figure 5).<br />
Eleven sections of the plant area were defined,<br />
including about 50 spots where emissions would<br />
normally occur during operations. The pipe <strong>and</strong><br />
control system from the off-air plant is widely<br />
spread throughout the whole area. Ventilated<br />
volatiles will effectively be sucked by the mediumpressure<br />
fan located near the incinerator plants.<br />
To maintain a constant gas flow, ventilated VOCs<br />
are mixed with ambient air, entering the suction<br />
part as the last input point. The fan distributes the<br />
volatiles further to one of the three SCCs, where<br />
high-temperature incineration takes place.<br />
The closed system is designed for -200 to +400<br />
mBar. It operates with a pressure of -80 to -100<br />
mBar on the suction part <strong>and</strong> +50 to +150 mBar<br />
Figure 5<br />
Off-air plant<br />
VOC - sources<br />
after the fan. The galvanized pipe system is<br />
designed to withst<strong>and</strong> a pressure of 10 bars.<br />
Differences in tank volumes (<strong>and</strong> thereby pressure)<br />
during filling <strong>and</strong> emptying periods are regulated<br />
in such a way that the off-air plant will<br />
ventilate the compressed tank gases in the ratio<br />
25/20 mBar, <strong>and</strong> the inert supply system will add<br />
nitrogen in the ratio 10/15 mBar.<br />
To eliminate potential risk of flame propagation,<br />
the ex-proof system is equipped with more than 50<br />
static flame arresters, redundant monitoring<br />
equipment, etc. The off-air plant is designed to a<br />
minimum velocity of 17 metres/second <strong>and</strong> the<br />
SCC nozzles ensure a minimum velocity of 55<br />
metres/second.<br />
Removal of bromine <strong>and</strong> iodine from<br />
flue gases<br />
When waste containing bromine or iodine is<br />
incinerated, the flue gas will contain these substances,<br />
which are brown <strong>and</strong> purple in colour.<br />
There are no official EU flue gas limits for bromine<br />
<strong>and</strong> iodine. However, due to their colour they cannot<br />
be accepted in the flue gas. Kommunekemi has<br />
therefore installed special bromine/iodine cleaning<br />
columns in all three incineration lines. Bromine/<br />
iodine cleaning works as follows:<br />
-0.7/40 mbar<br />
Br 2 + SO 3<br />
2- + H 2 O → 2Br - + SO 4<br />
2- + 2H + (1)<br />
<strong>and</strong><br />
I 2 + SO 3<br />
2- + H 2 O → 2I - + SO 4<br />
2- + 2H + (2)<br />
From the chemical reaction, it can be seen that<br />
the reduction of bromine/iodine to bromide <strong>and</strong><br />
iodide causes lower pH <strong>and</strong> sodium hydroxide<br />
must therefore be added to keep the pH at approximately<br />
7.5.<br />
Unfortunately the sulphite will also be consumed<br />
by the remaining oxygen (approximately<br />
10 %) in the flue gas:<br />
O 2 + 2SO 3<br />
2- → 2SO 4<br />
2- (3)<br />
This reaction does not cause any change in pH.<br />
However, expensive raw material (sodium sulphite)<br />
is consumed without any useful effect on the<br />
process.<br />
Exactly similar chemical reactions will also take<br />
place in the SO 2 scrubber (i.e. when the concentration<br />
of SO 2 in the flue gas is high enough, there<br />
will be sufficient sulphite to reduce bromine/<br />
iodine to bromide <strong>and</strong> iodide). It can therefore be<br />
concluded that as long as the SO 2 load in the flue<br />
gas is high, there is no need for the bromine/ iodine<br />
stage. However, it is Kommunekemi’s experience<br />
that the sulphur content in hazardous waste has<br />
fallen during the last year, thereby creating a need<br />
for a bromine/iodine stage.<br />
To reduce the amount of “wasted” sulphite, as<br />
described in chemical reaction (3) above, an automatic<br />
analyzing device for bromine <strong>and</strong> iodine has<br />
been installed in clean flue gas lines. When the bromide<br />
concentration exceeds 40 mg/Nm 3 or iodine<br />
exceeds 80 mg/Nm 3 (both levels clearly below the<br />
visible levels), the bromine stage automatically<br />
starts. Immediately afterward, the concentration<br />
of bromine <strong>and</strong> iodine in the cleaned flue gas will<br />
begin to decrease.<br />
SCC SCC SCC<br />
25/20 mbar<br />
Carbon<br />
filter<br />
Off-air plant<br />
10/15 mbar<br />
Typical installation for a tank unit<br />
N2<br />
Notes<br />
1. Directive 96/61. See http://europa.eu.int/<br />
comm/<strong>environment</strong>/ippc/index.htm, <strong>and</strong> (for<br />
Annex) http://eippcb.jrc.es/pages/Directive.htm<br />
#annex<br />
2. See http://eippcb.jrc.es.<br />
3. Kommunekemi a/s was established in Nyborg,<br />
Denmark, in 1971. It collects <strong>and</strong> treats hazardous<br />
waste from industries <strong>and</strong> households. The company<br />
produces <strong>and</strong> delivers almost 100% of the<br />
district heat used in the city of Nyborg <strong>and</strong> 15-<br />
20% of that city´s electricity consumption. ◆<br />
UNEP Industry <strong>and</strong> Environment April – September 2004 ◆ 55