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

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4.1 Mercury cell plants<br />

4.1.1 Overview <strong>of</strong> mercury emission abatement<br />

4.1.1.1 Reduction <strong>of</strong> mercury emissions to air, including hydrogen gas<br />

4.1.1.2 Reduction <strong>of</strong> mercury emissions to water<br />

4.1.1.3 Removal <strong>of</strong> mercury from caustic soda<br />

4.1.1.4 Treatment <strong>of</strong> mercury-containing wastes, including recovery <strong>of</strong><br />

mercury<br />

Chapter 4<br />

{These Sections are proposed to be deleted completely. Rationale: The original chlor-<strong>alkali</strong><br />

BREF concluded that <strong>the</strong> mercury cell technique is not <strong>BAT</strong> and that <strong>BAT</strong> <strong>for</strong> mercury cell<br />

plants is to convert to <strong>the</strong> membrane cell technique. From 1997 to 2010, <strong>the</strong> share <strong>of</strong> <strong>the</strong><br />

mercury cell technique to <strong>the</strong> total chlorine production capacity in EU-27 and EFTA countries<br />

has roughly halfed from more than 60 % to a bit more than 30 % while <strong>the</strong> total production<br />

capacity has remained on <strong>the</strong> same level. This indicates that conversion <strong>of</strong> mercury cell<br />

chlor-<strong>alkali</strong> plants to <strong>the</strong> membrane cell technique is technically and economically viable <strong>for</strong><br />

<strong>the</strong> chlor-<strong>alkali</strong> sector as a whole. Given that techniques to prevent mercury emissions are<br />

available, it is <strong>the</strong>re<strong>for</strong>e not necessary to describe techniques which reduce mercury emissions<br />

during normal plant operation. Never<strong>the</strong>less, techniques to reduce mercury emissions and to<br />

reduce <strong>the</strong> generation <strong>of</strong> mercury-containing wastes are relevant <strong>for</strong> decommissioning. There<br />

description including per<strong>for</strong>mance levels is <strong>the</strong>re<strong>for</strong>e covered by Section 4.1.3.}<br />

4.1.2 Conversion <strong>of</strong> mercury cell plants to membrane cell plants<br />

technology<br />

{Please note that <strong>the</strong> paragraphs <strong>of</strong> <strong>the</strong> original text were reordered to be compatible with <strong>the</strong><br />

current standard 10-heading structure.}<br />

Description<br />

This technique consists in converting mercury cell plants to membrane cell plants. A conversion<br />

to <strong>the</strong> membrane cell technique includes change <strong>of</strong> electrolysers, additional brine purification,<br />

additional brine dechlorination, inclusion <strong>of</strong> a cell room caustic soda recirculation system and a<br />

change <strong>of</strong> trans<strong>for</strong>mers and rectifiers.<br />

Technical description<br />

The conversion <strong>of</strong> mercury cell plants to membrane technology has <strong>the</strong> advantage <strong>of</strong> avoiding<br />

any future losses <strong>of</strong> mercury to <strong>the</strong> environment and reduces <strong>the</strong> energy consumption. To realise<br />

<strong>the</strong> conversion, technical changes are required depending on <strong>the</strong> existing situation. Most<br />

membrane cell operators have ei<strong>the</strong>r built a new 'green field' plant or expanded production<br />

capacity with a new plant alongside <strong>the</strong>ir mercury facilities. Some plants have been completely<br />

WORKING DRAFT IN PROGRESS<br />

converted <strong>the</strong>ir existing plant, but <strong>the</strong>re are also examples <strong>of</strong> partial conversion. Figure 4.1<br />

below shows <strong>the</strong> main changes that need to be carried out to an existing plant when converting<br />

from <strong>the</strong> mercury cell to <strong>the</strong> membrane cell technique technology.<br />

Conversion is technically applicable at all existing mercury cell chlor-<strong>alkali</strong> plants. Economic<br />

feasibility may vary from site to site (see Table 4.8, page 94).<br />

TB/EIPPCB/CAK_Draft_1 December 2011 147

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