(BAT) Reference Document for the Production of Chlor-alkali ...
(BAT) Reference Document for the Production of Chlor-alkali ...
(BAT) Reference Document for the Production of Chlor-alkali ...
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Chapter 3<br />
KCl are higher than from those using exclusively NaCl. However, emissions do also depend on<br />
o<strong>the</strong>r plant-specific factors and several plants in EU-27 and EFTA countries using exclusively<br />
NaCl show higher emissions to air than those <strong>of</strong> plants using KCl [ 57, EIPPCB 2011 ].<br />
In 1997, mercury emissions from western European cell rooms were in <strong>the</strong> range <strong>of</strong> 0.17-1.93<br />
g/t chlorine production capacity, as reported by Euro <strong>Chlor</strong>.<br />
3.5.6.3 Process exhaust<br />
3.5.6.3.1 Overview<br />
Process exhaust refers to all gaseous streams by which mercury can be emitted to <strong>the</strong><br />
atmosphere, apart from cell room ventilation air and product hydrogen as product. One <strong>of</strong> <strong>the</strong><br />
most significant sources <strong>of</strong> mercury emission is <strong>the</strong> purge <strong>of</strong> inlet and outlet boxes (‘end<br />
boxes’). Today, <strong>the</strong>y are usually connected to a separate ventilation system. The vacuum<br />
cleaning equipment is also a significant mercury source and it is normally also connected to a<br />
ventilation system. The typical streams which may have significant mercury content that require<br />
<strong>the</strong> use <strong>of</strong> a treatment technique include [ 87, Euro <strong>Chlor</strong> 2006 ]:<br />
purge air from cell end boxes;<br />
vents from wash water collection tanks;<br />
exhaust from any vacuum system used to collect spilled mercury (but some portable<br />
vacuum cleaners have <strong>the</strong>ir own mercury absorption system);<br />
hydrogen burnt or sold as fuel (see Section 3.5.6.3.4);<br />
hydrogen emitted to <strong>the</strong> atmosphere (see Section 3.5.6.3.4);<br />
vents from caustic soda pumping tanks (see Section 3.5.6.3.3);<br />
vents from caustic soda filters (see Section 3.5.6.3.3);<br />
exhausts and vents from distillation units <strong>for</strong> mercury-contaminated solid wastes<br />
(see Section 3.5.6.3.6);<br />
vents from storage <strong>of</strong> metallic mercury and waste contaminated with mercury (see<br />
Section 3.5.6.3.5);<br />
vents from workshops where contaminated equipment is handled (see<br />
Section 3.5.6.3.7).<br />
Some streams may be combined prior to treatment while o<strong>the</strong>rs require separate treatment units.<br />
For example, hydrogen streams are usually not mixed with streams containing significant<br />
amounts <strong>of</strong> air, in order to prevent <strong>the</strong> <strong>for</strong>mation <strong>of</strong> explosive mixtures [ 87, Euro <strong>Chlor</strong> 2006 ].<br />
O<strong>the</strong>r streams are likely to contain some mercury, but in such low concentrations that <strong>the</strong>y do<br />
not require treatment [ 87, Euro <strong>Chlor</strong> 2006 ]:<br />
vents from brine saturators (see Section 3.5.6.3.2)<br />
vents from brine filters and treatment tanks (see Section 3.5.6.3.2)<br />
vents from caustic soda stock tanks.<br />
WORKING DRAFT IN PROGRESS<br />
Mercury is mainly removed by [ 1, Ullmann's 2006 ], [ 87, Euro <strong>Chlor</strong> 2006 ]:<br />
adsorption on iodised or sulphurised activated carbon;<br />
scrubbing with hypochlorite or chlorinated brine to <strong>for</strong>m mercury(II) chloride;<br />
adding chlorine to <strong>for</strong>m dimercury dichloride (calomel) which is collected on a solid<br />
substrate such as rock salt in a packed column.<br />
scrubbing with hypochlorite, chlorinated brine or using a calomel reaction, or<br />
using a sulphurised charcoal system.<br />
TB/EIPPCB/CAK_Draft_1 December 2011 115