(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 6<br />
It is not possible to retr<strong>of</strong>it air and oxygen-depolarised cathodes into existing membrane cells.<br />
Technical considerations relevant to applicability<br />
The ODC technique can be used in new installations. The retr<strong>of</strong>itting <strong>of</strong> existing membrane cell<br />
plants is also possible provided that parts <strong>of</strong> <strong>the</strong> electrolysers are adapted. In 2011, however, <strong>the</strong><br />
ODC technique is specific to a single electrolyser's manufacturer who will begin to<br />
commercialise it in 2013. Practical experience with a new plant <strong>of</strong> industrial scale and with<br />
retr<strong>of</strong>itting <strong>of</strong> existing plants needs to be gained [ 3, Euro <strong>Chlor</strong> 2011 ], [ 49, Euro <strong>Chlor</strong> 2010 ].<br />
Economics<br />
The economic assessment <strong>of</strong> <strong>the</strong> ODC technique versus conventional membrane cell technique<br />
depends on a number <strong>of</strong> factors such as <strong>the</strong> costs <strong>for</strong> electricity, new electrolysis cells, ODCs<br />
and required oxygen on <strong>the</strong> one hand as well as type and degree <strong>of</strong> hydrogen usage on <strong>the</strong> o<strong>the</strong>r.<br />
Moreover, it has to be considered whe<strong>the</strong>r a new plant or <strong>the</strong> conversion <strong>of</strong> an existing amalgam<br />
or diaphragm cell plant is planned. It is <strong>the</strong>re<strong>for</strong>e difficult to draw general conclusions without<br />
taking into account <strong>the</strong> integration <strong>of</strong> <strong>the</strong> ODC technique into <strong>the</strong> whole plant [ 49, Euro <strong>Chlor</strong><br />
2010 ], [ 52, Moussallem et al. 2008 ].<br />
Investment costs <strong>for</strong> <strong>the</strong> conversion to <strong>the</strong> ODC technique were reported to be in <strong>the</strong> range <strong>of</strong><br />
EUR 70 – 100/t annual chlorine capacity. Assuming that <strong>the</strong> co-produced hydrogen is burnt,<br />
that <strong>the</strong> costs <strong>for</strong> <strong>the</strong> production <strong>of</strong> pure oxygen are between EUR 0.054 – 0.063/m 3 (at standard<br />
conditions) and that <strong>the</strong> electricity price is EUR 60/MWh, <strong>the</strong> ODC technique was reported in<br />
2009 to be economically viable [ 113, Moussallem et al. 2009 ]. However, if <strong>the</strong> co-produced<br />
hydrogen is used <strong>for</strong> chemical reactions, <strong>the</strong> ODC technique was reported in 2011 to be not<br />
economically viable [ 115, Jörissen et al. 2011 ].<br />
The future economic assessment depends on <strong>the</strong> evolution <strong>of</strong> electricity prices which in turn<br />
depend on <strong>the</strong> world energy markets, which could also be affected by carbon trading and<br />
possible carbon dioxide taxes. In addition, <strong>the</strong> evolution <strong>of</strong> <strong>the</strong> 'hydrogen economy' could<br />
trans<strong>for</strong>m <strong>the</strong> hydrogen from a co-product to a premium fuel, easily saleable on <strong>the</strong> hydrogen<br />
market [ 52, Moussallem et al. 2008 ].<br />
Driving <strong>for</strong>ce <strong>for</strong> implementation<br />
The driving <strong>for</strong> <strong>for</strong> implementation is a reduction <strong>of</strong> costs related to energy consumption.<br />
Example plants<br />
Bayer/Uhde in Leverkusen (Germany), chlorine capacity 20 kt/yr, put into operation in<br />
summer 2011;<br />
Two demonstration units in testing in Japan.<br />
<strong>Reference</strong>s: literature<br />
[ 3, Euro <strong>Chlor</strong> 2011 ], [ 49, Euro <strong>Chlor</strong> 2010 ], [ 51, Bulan 2007 ], [ 52, Moussallem et al.<br />
2008 ], [ 53, Bulan et al. 2009 ], [ 113, Moussallem et al. 2009 ], [ 115, Jörissen et al. 2011 ]<br />
[Gestermann-Ottaviani, 2000], [Wienkenhöver, 2000], [Gestermann, 1998], [Kirk-Othmer,<br />
1991]<br />
WORKING DRAFT IN PROGRESS<br />
294 December 2011 TB/EIPPCB/CAK_Draft_1