(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 4<br />
removal <strong>of</strong> conductive components via special adsorption beds in <strong>the</strong> chlor-<strong>alkali</strong> plant<br />
(modified equipment).<br />
Achieved environmental benefits<br />
The achieved environmental benefits <strong>of</strong> this technique include <strong>the</strong> following:<br />
reduction <strong>of</strong> salt consumption;<br />
reduction <strong>of</strong> water consumption;<br />
reduction <strong>of</strong> chloride emissions.<br />
Environmental per<strong>for</strong>mance and operational data<br />
At <strong>the</strong> AkzoNobel plant in Bitterfeld (Germany), approximately 8 % <strong>of</strong> <strong>the</strong> consumed brine is<br />
obtained by neutralising a hydrochloric acid stream from a customer with sodium hydroxide<br />
[ 57, EIPPCB 2011 ]. {Please TWG provide more in<strong>for</strong>mation.}<br />
At <strong>the</strong> Arkema plant in Saint Auban (France), waste water generated during a chlorination<br />
process and containing hydrochloric acid is neutralised with caustic soda and fed back to <strong>the</strong><br />
electrolysis unit after stripping organic contaminants [ 3, Euro <strong>Chlor</strong> 2011 ], [ 33, Euro <strong>Chlor</strong><br />
2011 ].<br />
At <strong>the</strong> Dow plant in Stade (Germany), waste water generated during <strong>the</strong> production <strong>of</strong><br />
propylene oxide is sent back <strong>for</strong> solution mining after biological and physico-chemical<br />
treatment. This results in savings <strong>of</strong> approximately 10 000 000 m 3 /yr <strong>of</strong> fresh water and <strong>the</strong> same<br />
volume <strong>of</strong> waste water not discharged [ 33, Euro <strong>Chlor</strong> 2011 ]. Previously, a total water<br />
consumption <strong>of</strong> 30 000 000 m 3 /yr was reported. Waste water recycling resulted in conservation<br />
<strong>of</strong> 7 000 000 m 3 /yr <strong>of</strong> river water and 600 000 t/yr <strong>of</strong> salt, as well as a 23 % reduction <strong>of</strong> annual<br />
salt discharge [ 129, Euro <strong>Chlor</strong> 2007 ].<br />
At <strong>the</strong> SABIC plant in Bergen op Zoom (Ne<strong>the</strong>rlands), 73 % <strong>of</strong> <strong>the</strong> NaCl leaving <strong>the</strong><br />
polycarbonate production unit is recycled, which is equivalent to vacuum salt savings and<br />
related emissions <strong>of</strong> approximately 72 000 t/yr. Moreover, water consumption is reduced by<br />
225 000 m 3 /yr [ 128, SABIC 2008 ].<br />
At <strong>the</strong> Zachem plant in Bydgoszcz (Poland), hydrochloric acid obtained during <strong>the</strong> production<br />
<strong>of</strong> epichlorohydrin and toluene diisocyanate is neutralised with <strong>the</strong> caustic liquor from <strong>the</strong><br />
diaphragm cells and recycled [ 220, Polish Ministry 2011 ].<br />
Cross-media effects<br />
Some raw materials and energy are consumed <strong>for</strong> <strong>the</strong> installation and operation <strong>of</strong> <strong>the</strong> additional<br />
waste water treatment units.<br />
Technical considerations relevant to applicability<br />
The recycling <strong>of</strong> salt-containing waste water is restricted by two major factors. First, it is<br />
necessary to ensure that no contaminants with a detrimental effect on <strong>the</strong> electrolysis process are<br />
introduced into <strong>the</strong> brine system. This includes heavy metals, which negatively affect <strong>the</strong><br />
lifetime <strong>of</strong> <strong>the</strong> diaphragm or membrane as well as <strong>the</strong> energy consumption, in particular <strong>for</strong> <strong>the</strong><br />
membrane cell technique (see Table 2.4). High residual concentrations <strong>of</strong> organic compounds<br />
are also unwanted in <strong>the</strong> membrane cell technique (see Table 2.4) and may lead to <strong>the</strong> <strong>for</strong>mation<br />
<strong>of</strong> halogenated organic compounds (see Section 3.4.2.3.7). Second, <strong>the</strong> water balance <strong>of</strong> <strong>the</strong><br />
electrolysis unit has to be respected [ 33, Euro <strong>Chlor</strong> 2011 ].<br />
WORKING DRAFT IN PROGRESS<br />
Economics<br />
{Please TWG provide more in<strong>for</strong>mation.}<br />
At <strong>the</strong> SABIC plant in Bergen op Zoom, investment costs <strong>for</strong> <strong>the</strong> waste water recycling system<br />
amounted to EUR 11 million. Annual cost savings due to reduced consumption <strong>of</strong> salt and<br />
TB/EIPPCB/CAK_Draft_1 December 2011 187