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

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Chapter 5<br />

The <strong>BAT</strong>-associated consumption levels <strong>for</strong> steam from <strong>the</strong> caustic evaporation<br />

process <strong>for</strong> new caustic concentrators in membrane cell plants are:<br />

Number <strong>of</strong> effects/stages in evaporator<br />

Steam consumption in t/t NaOH<br />

2 3<br />

produced as yearly average values on<br />

<strong>the</strong> basis <strong>of</strong> 100 % NaOH<br />

Q 710 Q 480<br />

NB: Figures refer to a feed temperature <strong>of</strong> 80 °C and <strong>for</strong><br />

caustic concentration from 32 wt-% to 50 wt-%.<br />

[This <strong>BAT</strong> conclusion is based on in<strong>for</strong>mation given in Section 4.3.2.3.8.]<br />

8. In order to reduce energy consumption, <strong>BAT</strong> is to use <strong>the</strong> co-produced hydrogen from <strong>the</strong><br />

electrolysis as a chemical reagent or fuel.<br />

Description<br />

Hydrogen can be used in chemical reactions (e.g. production <strong>of</strong> ammonia, hydrogen<br />

peroxide, hydrochloric acid, and methanol; reduction <strong>of</strong> organic compounds;<br />

hydrodesulphurisation <strong>of</strong> petroleum; hydrogenation <strong>of</strong> oils and greases; chain<br />

termination in polyolefin production) or as a fuel in a combustion process to produce<br />

steam and electricity.<br />

For <strong>the</strong> use <strong>of</strong> hydrogen as a chemical reagent or fuel, <strong>the</strong> <strong>BAT</strong>-associated<br />

environmental per<strong>for</strong>mance level is to use, as a yearly average, 90 – 100 % <strong>of</strong> <strong>the</strong><br />

co-produced hydrogen.<br />

The higher end <strong>of</strong> <strong>the</strong> range is achieved by plants on sites with a high demand <strong>for</strong><br />

hydrogen.<br />

[This <strong>BAT</strong> conclusion is based on in<strong>for</strong>mation given in Section 4.3.2.3.9]<br />

WORKING DRAFT IN PROGRESS<br />

278 December 2011 TB/EIPPCB/CAK_Draft_1

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