(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 />
typically seen to be not attractive if <strong>the</strong> payback time exceeds three years (see also<br />
Section 4.3.2.3.2) [ 97, Concorde 2006 ], [ 114, Delfrate and Schmitt 2010 ].<br />
In <strong>the</strong> case <strong>of</strong> <strong>the</strong> Altair Chimica plant in Volterra and <strong>the</strong> Solvay plant in Rosignano (both in<br />
Italy), <strong>the</strong> conversion was subsidised with state aid [ 239, COM 2005 ].<br />
Effects on competitiveness<br />
SRI Consulting, who made a study <strong>of</strong> <strong>the</strong> competitiveness <strong>of</strong> <strong>the</strong> western European chlor-<strong>alkali</strong><br />
industry, reports that production costs <strong>for</strong> chlorine production by mercury technology are<br />
mainly linked to fixed costs in which plant size plays an important role. Most mercury<br />
technology plants in western Europe have capacities between 50 and 200 kt/y with an average<br />
<strong>of</strong> about 157 kt/y <strong>of</strong> chlorine capacity. The situation is quite different in <strong>the</strong> U.S. Gulf where <strong>the</strong><br />
average plant size is significantly larger, with an average <strong>of</strong> 678 kt/y and structural economic<br />
advantages linked to lower costs <strong>for</strong> main raw materials: salt and electricity higher in western<br />
Europe (2.0 US cents/kg versus 3.6 in western Europe <strong>for</strong> salt and 2.8 US cents/kWh versus 4.3<br />
<strong>for</strong> electricity). The SRI study concludes that <strong>the</strong> industry´s view <strong>of</strong> a <strong>for</strong>ced phase-out <strong>of</strong><br />
mercury technology by 2010 is that conversion would be uneconomic <strong>for</strong> about 33% (2.2<br />
million tonnes) <strong>of</strong> present mercury cell capacity, and that <strong>the</strong>se plants would be closed. [SRI<br />
Consulting, 1997] {The in<strong>for</strong>mation in this paragraph is outdated.}<br />
In EU-27 and EFTA countries western Europe, <strong>the</strong> cost <strong>of</strong> electrical energy is very dependent<br />
on <strong>the</strong> basic source <strong>of</strong> energy and <strong>the</strong> type <strong>of</strong> contracts negotiated with suppliers, but <strong>the</strong> relative<br />
differences between countries and regions remain. The special circumstances making a mercury<br />
cell plant economical can change if <strong>the</strong> price <strong>of</strong> electrical energy increases sharply; in that case a<br />
conversion to <strong>the</strong> membrane cell technique technology can become more attractive<br />
economically.<br />
Effect on downstream production<br />
According to a chlorine flow study undertaken by Euro <strong>Chlor</strong>, sales <strong>of</strong> virgin chlorine account<br />
<strong>for</strong> only a few percent <strong>of</strong> <strong>the</strong> trade balance. That means that Most <strong>of</strong> <strong>the</strong> chlorine produced is<br />
used as a chemical intermediate ei<strong>the</strong>r internally or by o<strong>the</strong>r companies. A key consideration,<br />
<strong>the</strong>re<strong>for</strong>e, is <strong>the</strong> downtime associated with <strong>the</strong> conversion and <strong>the</strong> impact on <strong>the</strong> production <strong>of</strong><br />
downstream products such as PVC. Caustic users will also be affected by restrictions in<br />
chlor-<strong>alkali</strong> production.<br />
Driving <strong>for</strong>ce <strong>for</strong> implementation<br />
The driving <strong>for</strong>ces <strong>for</strong> implementation <strong>of</strong> this technique include:<br />
environmental legislation;<br />
reduction <strong>of</strong> costs related to energy consumption;<br />
capacity increase <strong>of</strong> an existing plant.<br />
Example plants<br />
More than 50 chlor-<strong>alkali</strong> plants worldwide have been converted to <strong>the</strong> membrane cell<br />
technique since <strong>the</strong> beginning <strong>of</strong> <strong>the</strong> 1980s [ 229, Oceana 2007 ]. Example plants are listed in<br />
Table 4.6.<br />
WORKING DRAFT IN PROGRESS<br />
<strong>Reference</strong> literature<br />
[ 97, Concorde 2006 ], [ 114, Delfrate and Schmitt 2010 ], [ 211, Dibble and White 1988 ],<br />
[ 224, Bayer 1998 ], [ 225, Lott 1995 ], [ 226, Schindler 2000 ], [ 227, de Flon 1998 ], [ 228,<br />
PPG 2007 ], [ 229, Oceana 2007 ] [ 230, Schubert 2000 ] [ 231, Chemie Produktion 2000 ],<br />
[ 232, Euro <strong>Chlor</strong> 2010 ], [ 233, SEPA 1997 ], [ 234, UBA AT 1998 ], [ 235, ANE 2010 ],<br />
[ 236, EIPPCB 2011 ], [ 237, Lindley 1997 ]<br />
[de Flon, 1998], [Dibble-White, 1988], [Euro <strong>Chlor</strong> paper, 1998], [Lindley, 1997], [Lott, 1995],<br />
[SRI Consulting, 1997], [UBA (A), 1998]<br />
160 December 2011 TB/EIPPCB/CAK_Draft_1