(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 ...
You also want an ePaper? Increase the reach of your titles
YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.
Chapter 4<br />
All types <strong>of</strong> salt require energy <strong>for</strong> <strong>the</strong>ir extraction, purification and transport which depend on<br />
<strong>the</strong> extraction techniques used as well as on <strong>the</strong> means <strong>of</strong> transport and <strong>the</strong> distance from <strong>the</strong> salt<br />
source to <strong>the</strong> chlor-<strong>alkali</strong> plant.<br />
Vacuum salt is <strong>the</strong> purest salt used in chlor-<strong>alkali</strong> plants which is favourable in terms <strong>of</strong><br />
consumption <strong>of</strong> ancillary materials, generation <strong>of</strong> brine filtration sludges, process stability and<br />
energy consumption. However, <strong>the</strong> production <strong>of</strong> vacuum salt requires considerable amounts <strong>of</strong><br />
energy (see Section 3.3.4.2), ancillary materials <strong>for</strong> chemical purification might be needed and<br />
wastes might be generated <strong>of</strong>f-site [ 66, Ullmann's 2010 ]. Rock salt, salt from potash mining<br />
wastes and solution-mined brine are less pure than vacuum salt and thus require higher amounts<br />
<strong>of</strong> ancillary materials <strong>for</strong> brine purification and lead to higher amounts <strong>of</strong> brine filtration sludges<br />
(see Table 3.17). When salt from potash mining wastes is used, no additional energy <strong>for</strong> mining<br />
is required and raw materials are saved. Moreover, its consumption contributes to <strong>the</strong> restoration<br />
<strong>of</strong> <strong>the</strong> original landscape [ 27, ANE 2010 ]. Solar salt uses <strong>the</strong> renewable energy from <strong>the</strong> sun<br />
<strong>for</strong> <strong>the</strong> evaporative step but additional purification is usually required.<br />
Several <strong>of</strong> <strong>the</strong> factors concerning <strong>the</strong> overall environmental impact <strong>of</strong> <strong>the</strong> different types <strong>of</strong> salt<br />
are outside <strong>the</strong> scope <strong>of</strong> this BREF and depend on local conditions such as <strong>the</strong> means <strong>of</strong><br />
transport and <strong>the</strong> distance from <strong>the</strong> production <strong>of</strong> salt to <strong>the</strong> chlor-<strong>alkali</strong> plant. There<strong>for</strong>e, no<br />
proposals are made with respect to <strong>the</strong> use <strong>of</strong> a specific type <strong>of</strong> salt as a technique to consider in<br />
<strong>the</strong> determination <strong>of</strong> <strong>BAT</strong>.<br />
4.3.2.1.2 Techniques to reduce consumption <strong>of</strong> salt<br />
In addition to <strong>the</strong> techniques described in <strong>the</strong> following Section 4.3.2.1.3, several <strong>of</strong> <strong>the</strong><br />
techniques to reduce consumption <strong>of</strong> water (see Section 4.3.2.2), to reduce emissions <strong>of</strong> chloride<br />
(see Section 4.3.6.2) and to reduce emissions <strong>of</strong> chlorate (see Section 4.3.6.4) do also reduce<br />
salt consumption.<br />
4.3.2.1.3 Recycling <strong>of</strong> waste water from o<strong>the</strong>r production processes<br />
Description<br />
This technique consists in recycling salt-containing effluents from o<strong>the</strong>r production processes to<br />
<strong>the</strong> brine system <strong>of</strong> <strong>the</strong> chlor-<strong>alkali</strong> plant.<br />
Technical description<br />
The treatment required <strong>for</strong> waste water recycling is plant-specific and depends on <strong>the</strong> impurities<br />
contained in <strong>the</strong> waste water.<br />
At <strong>the</strong> SABIC plant in Bergen op Zoom (Ne<strong>the</strong>rlands), waste water from <strong>the</strong> polycarbonate<br />
production unit undergoes a series <strong>of</strong> purification steps be<strong>for</strong>e it is recycled to <strong>the</strong> brine circuit<br />
[ 128, SABIC 2008 ]:<br />
isolation <strong>of</strong> brine from <strong>the</strong> reaction product using special decanters at <strong>the</strong> resin plant;<br />
removal <strong>of</strong> solvent via distillation at <strong>the</strong> resin plant (modified equipment);<br />
removal <strong>of</strong> suspended solids via filtration at <strong>the</strong> central waste water treatment plant<br />
(modified equipment);<br />
adsorption <strong>of</strong> phenolic compounds via active carbon beds at <strong>the</strong> central waste water<br />
treatment plant (modified equipment);<br />
destruction <strong>of</strong> carbonates via acidification (newly designed unit <strong>for</strong> this purpose);<br />
adsorption <strong>of</strong> nitrogen containing components via special active carbon beds (newly<br />
designed unit <strong>for</strong> this purpose);<br />
adsorption <strong>of</strong> metal ions on ion adsorption resins in <strong>the</strong> chlor-<strong>alkali</strong> plant (modified<br />
equipment);<br />
WORKING DRAFT IN PROGRESS<br />
186 December 2011 TB/EIPPCB/CAK_Draft_1