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(BAT) Reference Document for the Production of Chlor-alkali ...

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Chapter 4<br />

Example plants<br />

Kemira in Joutseno (Finland), chlorine capacity 75 kt/yr.<br />

<strong>Reference</strong> literature<br />

[ 57, EIPPCB 2011 ], [ 209, COM 2007 ]<br />

4.3.6.5 Techniques to reduce emissions <strong>of</strong> halogenated organic<br />

compounds<br />

Description<br />

These techniques consist in reducing <strong>the</strong> levels <strong>of</strong> organic contaminants in <strong>the</strong> brine in order to<br />

diminish <strong>the</strong> <strong>for</strong>mation <strong>of</strong> halogenated organic compounds.<br />

Technical description<br />

The <strong>for</strong>mation <strong>of</strong> halogenated organic compounds in <strong>the</strong> brine system can be reduced by:<br />

careful selection and control <strong>of</strong> salt and ancillary materials with respect to organic<br />

impurities;<br />

water purification by using techniques such as membrane filtration, ion exchange, UV<br />

irradiation and adsorption on activated carbon;<br />

careful selection <strong>of</strong> equipment such as cells, pipes, valves and pumps to reduce <strong>the</strong><br />

potential leaching <strong>of</strong> organic contaminants to <strong>the</strong> brine.<br />

The levels <strong>of</strong> organic contaminants in <strong>the</strong> brine system are usually kept low in order to meet <strong>the</strong><br />

specifications <strong>of</strong> <strong>the</strong> equipment. This is especially true <strong>for</strong> <strong>the</strong> membrane cell technique where<br />

<strong>the</strong> concentration <strong>of</strong> total organic carbon is usually required to be in <strong>the</strong> range <strong>of</strong> 1 – 10 ppm<br />

(see Table 2.4).<br />

End-<strong>of</strong>-pipe techniques to reduce emissions <strong>of</strong> halogenated organic compounds are very rarely<br />

used.<br />

{Please TWG provide more in<strong>for</strong>mation.}<br />

Achieved environmental benefits<br />

The achieved environmental benefit <strong>of</strong> <strong>the</strong>se techniques is a reduction <strong>of</strong> emissions <strong>of</strong><br />

halogenated organic compounds.<br />

Environmental per<strong>for</strong>mance and operational data<br />

Current emission levels <strong>of</strong> halogenated organic compounds at <strong>the</strong> outlet <strong>of</strong> <strong>the</strong> electrolysis unit<br />

are presented in Section 3.4.2.3.7.<br />

Cross-media effects<br />

A change <strong>of</strong> <strong>the</strong> salt source may lead to higher overall energy consumption and emissions if <strong>the</strong><br />

transport distance increases. Additional purification steps <strong>for</strong> salt, water or ancillary materials<br />

may lead to additional consumption <strong>of</strong> energy and ancillary materials and to generation <strong>of</strong><br />

additional waste.<br />

WORKING DRAFT IN PROGRESS<br />

Technical considerations relevant to applicability<br />

Generally, <strong>the</strong>re are no technical restrictions to <strong>the</strong> applicability <strong>of</strong> <strong>the</strong>se techniques.<br />

Economics<br />

{Please TWG provide in<strong>for</strong>mation.}<br />

Driving <strong>for</strong>ce <strong>for</strong> implementation<br />

The driving <strong>for</strong>ces <strong>for</strong> implementation <strong>of</strong> <strong>the</strong>se techniques include:<br />

250 December 2011 TB/EIPPCB/CAK_Draft_1

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