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

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Chapter 3<br />

Especially relevant with regard to chlorate and bromate are plants that do not use <strong>the</strong> bleach<br />

produced from <strong>the</strong> chlorine-containing waste gases but and destroy it <strong>the</strong> bleach by means <strong>of</strong><br />

heating to 70 ºC and acidifying it to pH 6 or 7. In this <strong>the</strong>se cases, <strong>the</strong> free oxidants are<br />

converted to decomposed into <strong>the</strong> less reactive chlorate and bromate. A value <strong>of</strong> 4 kg chlorate<br />

per tonne <strong>of</strong> chlorine produced is reported <strong>for</strong> a plant applying <strong>the</strong>rmal bleach destruction, while<br />

bromate was in <strong>the</strong> range <strong>of</strong> 0.22 – 550 g per tonne <strong>of</strong> chlorine produced [ 17, Dutch Ministry<br />

1998 ] [Dutch report, 1998].<br />

<strong>Chlor</strong>ate and bromate are less reactive than <strong>the</strong> free oxidants and have a lower acute toxicity <strong>for</strong><br />

aquatic biota. However, chlorate is classified as toxic to aquatic life with long-lasting effects<br />

(chronic toxicity) and bromate is presumed to have carcinogenic potential <strong>for</strong> humans [ 76,<br />

Regulation EC/1272/2008 2008 ].<br />

3.4.2.3.6 Heavy metals Metals<br />

Brine contains a certain amount <strong>of</strong> dissolved metals: such as nickel, zinc, iron, and copper,,<br />

which originate from salt impurities and metallic equipment (see Table 2.4). depending on <strong>the</strong><br />

salt used. In some cases, <strong>the</strong> The addition <strong>of</strong> an anti-caking agent (ferrocyanides) to <strong>the</strong> solid<br />

salt <strong>for</strong> transport, loading and unloading purposes provides an extra source <strong>of</strong> iron which is<br />

mostly <strong>the</strong> case if vacuum salt is used. Dissolved heavy metals are unwanted compounds in <strong>the</strong><br />

process. In <strong>the</strong> case <strong>of</strong> <strong>the</strong> mercury cell technique, <strong>the</strong>y can lead to <strong>the</strong> release <strong>of</strong> hydrogen in <strong>the</strong><br />

anode compartment (see Section 2.2.1) while in <strong>the</strong> case <strong>of</strong> <strong>the</strong> membrane cell technique, <strong>the</strong>y<br />

negatively affect <strong>the</strong> per<strong>for</strong>mance <strong>of</strong> <strong>the</strong> cells (see Table 2.4).<br />

Part <strong>of</strong> this iron is Dissolved metals are partly removed by <strong>the</strong> bleed purge from brine treatment,<br />

although <strong>the</strong> larger part majority is precipitated as hydroxides (e.g. iron hydroxide, Fe(OH)3)<br />

and are removed during brine filtration. In <strong>the</strong> case <strong>of</strong> membrane cell plants, dissolved metals<br />

are fur<strong>the</strong>r removed from <strong>the</strong> brine during ion exchange and subsequently emitted during<br />

regeneration. Reported values <strong>of</strong> iron releases are about 100 ppb from amalgam plants using<br />

vacuum salt. A decomposition unit <strong>for</strong> to prevent iron complexes may be necessary <strong>for</strong><br />

membrane cell plants. After decomposition, releases <strong>of</strong> iron are about 30 to 40 ppb. {Data were<br />

included in table.} Reported emission concentrations and factors are summarised in Table 3.15.<br />

WORKING DRAFT IN PROGRESS<br />

90 December 2011 TB/EIPPCB/CAK_Draft_1

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