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

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Chapter 3<br />

3.4 Emissions and waste generation from all cell plants<br />

Emissions from auxiliary processes<br />

3.4.1 Emissions from <strong>the</strong> storage and handling <strong>of</strong> solids salt<br />

unloading and storage<br />

The salt is normally stored in sealed areas, sometimes equipped with a ro<strong>of</strong>, to prevent it from<br />

blowing <strong>of</strong>f site. Protective systems are installed to prevent contamination <strong>of</strong> <strong>the</strong> brine, in<br />

particular in case <strong>of</strong> rain or if <strong>the</strong> storage is located near to surface waters or ground waters.<br />

{This is covered in Chapter 2.}<br />

Emissions from <strong>the</strong> storage and handling <strong>of</strong> solids include minor dust emissions to air<br />

originating from salt and ancillary materials as well as emissions to water caused by <strong>the</strong> seeping<br />

<strong>of</strong> rainwater and discharge with run-<strong>of</strong>f water. Usually, <strong>the</strong>re is no percolation into <strong>the</strong> soil<br />

because <strong>of</strong> an impermeable layer (sometimes with hardened salt) under <strong>the</strong> salt [ 3, Euro <strong>Chlor</strong><br />

2011 ].<br />

3.4.2 Emissions and waste generation from <strong>the</strong> brine circuit<br />

3.4.2.1 Overview<br />

Table 3.3, page 38, shows <strong>the</strong> different chemical agents which are employed to purify <strong>the</strong> brine<br />

be<strong>for</strong>e electrolysis. The consumption <strong>of</strong> chemicals varies from plant to plant depending on <strong>the</strong><br />

impurities <strong>of</strong> <strong>the</strong> brine and <strong>the</strong> type and sensitivity <strong>of</strong> <strong>the</strong> local environment into which <strong>the</strong> purge<br />

is discharged.<br />

As explained in Chapter 2, brine purification by pH adjustment, precipitation, flocculation and<br />

filtration is required, on a full flow or sidestream basis, to keep impurities at acceptable levels.<br />

Membrane and mercury cells may use recycled brine requiring dechlorination. Specifically <strong>for</strong><br />

membrane technology, brine purification is <strong>of</strong> critical importance to long membrane life and<br />

high efficiency. Thus, impurities need to be removed by ion-exchange resin units which <strong>the</strong>n<br />

require regeneration with caustic soda and acid washing. Some plants use vacuum crystallised<br />

salt, which is <strong>the</strong> most pure salt <strong>for</strong>m (but also <strong>the</strong> most expensive) and <strong>for</strong> this reason have a<br />

simplified brine purification step. {This paragraph contains too many details <strong>for</strong> an<br />

introduction. Some issues are described in Chapter 2.}<br />

Emissions from <strong>the</strong> brine circuit to air include fugitive emissions <strong>of</strong> chlorine and carbon<br />

dioxide. Emissions to water occur via <strong>the</strong> brine purge. Releases The emission levels depend on<br />

<strong>the</strong> purity <strong>of</strong> <strong>the</strong> incoming salt used, <strong>the</strong> cell technique technology used (mercury amalgam,<br />

diaphragm or membrane), <strong>the</strong> techniques used <strong>for</strong> brine purification trade-<strong>of</strong>f (use <strong>of</strong> chemical<br />

agents or direct purge in <strong>the</strong> media) and whe<strong>the</strong>r <strong>the</strong> brine is recirculated or wasted. Brine<br />

sludges which are generated during brine purification are one <strong>of</strong> <strong>the</strong> largest waste streams <strong>of</strong> <strong>the</strong><br />

chlor-<strong>alkali</strong> industry.<br />

WORKING DRAFT IN PROGRESS<br />

3.4.2.2 Emissions to air Air emissions<br />

Emissions to air from <strong>the</strong> brine circuit include mainly emissions <strong>of</strong> carbon dioxide and chlorine.<br />

The fugitive emission <strong>of</strong> carbon dioxide is possible from all three chlor-<strong>alkali</strong> technologies.<br />

Carbon dioxide is emitted from <strong>the</strong> brine acidification tanks due to <strong>the</strong> decomposition <strong>of</strong><br />

carbonate and hydrogen bicarbonate ions into water and carbon dioxide. The carbonate and<br />

hydrogen bicarbonate stem are from <strong>the</strong> auxiliary chemicals used in <strong>the</strong> brine purification step<br />

(see Table 3.4). The carbon dioxide ei<strong>the</strong>r escapes from <strong>the</strong> brine and is emitted to <strong>the</strong><br />

atmosphere or is led to <strong>the</strong> chlorine destruction unit, depending on <strong>the</strong> presence <strong>of</strong> chlorine in<br />

<strong>the</strong> brine. The concentration <strong>of</strong> (hydrogenbi) carbonate is expected to be lower when <strong>the</strong><br />

82 December 2011 TB/EIPPCB/CAK_Draft_1

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