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

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1 GENERAL INFORMATION<br />

1.1 Industrial and economical development <strong>of</strong> <strong>the</strong> chlor<strong>alkali</strong><br />

sector<br />

Chapter 1<br />

In 1800, Cruickshank was <strong>the</strong> first to prepare chlorine electrochemically. The process was,<br />

however, <strong>of</strong> little significance until <strong>the</strong> development <strong>of</strong> a suitable generator and <strong>of</strong> syn<strong>the</strong>tic<br />

graphite <strong>for</strong> anodes in 1892. These two developments made possible <strong>the</strong> electrolytic production<br />

<strong>of</strong> chlorine, <strong>the</strong> chlor-<strong>alkali</strong> process, on an industrial scale. About <strong>the</strong> same time, both <strong>the</strong><br />

diaphragm cell process (Griesheim cell, 1885) and <strong>the</strong> mercury cell process (Castner-Kellner<br />

cell, 1892) were introduced. The membrane cell process was developed much more recently<br />

(1970). Currently, 95% <strong>of</strong> world chlorine production is obtained by <strong>the</strong> chlor-<strong>alkali</strong> process.<br />

[Ullmann’s, 1996]<br />

Since 1970 graphite anodes have been largely superseded by activated titanium anodes in <strong>the</strong><br />

diaphragm and mercury cell processes. The newer membrane cell process uses only activated<br />

titanium anodes. [Ullmann’s, 1996]<br />

<strong>Production</strong> <strong>of</strong> chlorine was very low in <strong>the</strong> 1800s and chlorine was only used <strong>for</strong> bleaching. In<br />

1887, annual world production was 115 tonnes [Le <strong>Chlor</strong>e, 1996]. <strong>Chlor</strong>ine production since <strong>the</strong><br />

1940s has risen enormously, on <strong>the</strong> back <strong>of</strong> <strong>the</strong> burgeoning demand <strong>for</strong> plastics, notably PVC [J.<br />

Ind. Ecology, 1997] and polyurethanes. The production <strong>of</strong> chloroaromatics (e.g. chlorobenzene<br />

<strong>for</strong> phenol syn<strong>the</strong>sis), propylene oxide (chlorohydrin process), solvents containing chlorinated<br />

hydrocarbons, and inorganic chlorine compounds are also important factors behind <strong>the</strong><br />

increased use <strong>of</strong> chlorine after 1940.<br />

The chlor-<strong>alkali</strong> industry sector produces chlorine with its co-products sodium/potassium<br />

hydroxide (also called caustic soda/potash) and hydrogen by electrolysis <strong>of</strong> brine.<br />

In 2008, more than 500 companies produced chlorine at over 650 sites worldwide, with a total<br />

annual capacity <strong>of</strong> approximately 62.8 Mt. Figure 1.1 shows <strong>the</strong> share <strong>of</strong> installed production<br />

capacities per region in 2008. On a global scale, 2007 was a record growth year <strong>for</strong> <strong>the</strong><br />

chlor-<strong>alkali</strong> industry which <strong>the</strong>n experienced a dramatic contraction in 2008 and 2009 due to <strong>the</strong><br />

economic crisis. In 2010, <strong>the</strong> global industry was again on a growth path. Relatively little new<br />

capacity is however expected in <strong>the</strong> United States, Europe and Japan. More attractive growth is<br />

anticipated in <strong>the</strong> less developed regions <strong>of</strong> <strong>the</strong> world. For example, China increased its capacity<br />

from 2004 to 2008 by approximately 50 % and was <strong>the</strong> largest producer and consumer <strong>of</strong><br />

chlorine and caustic soda worldwide in 2010 [ 4, SRI Consulting 2008 ], [ 5, CMAI 2010 ].<br />

WORKING DRAFT IN PROGRESS<br />

TB/EIPPCB/CAK_Draft_1 December 2011 1

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