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SO - Rheinkalk

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The use of products that are optimally customised to the process provide particular<br />

advantages for the operator of semi-dry and dry processes. Therefore, highly<br />

reactive hydrated lime (Spongiacal ® ) is generally used since this<br />

• minimises the consumption of operating materials,<br />

• allows a safe compliance with mandatory limiting values,<br />

• reduces the amount of residual waste (requirement to minimise residual waste!).<br />

In the low-temperature range, the highly reactive hydrated lime products<br />

(WÜLFRAsorp ® A and Spongiacal ® ) have been used successfully for some time. An<br />

important further development was the combination of semi-dry and dry process<br />

steps with high porous products (MCD process).The medium temperature range<br />

offers very good application conditions for the use of special hydrates, particularly<br />

those to remove <strong>SO</strong>2. For example, in the glass industry, flue-gas cleaning has been<br />

very successful using WÜLFRAsorp ® A at 350 – 500 °C 4 . In the high-temperature<br />

range at approx. 850 –1000 °C, products with high surface areas that were specially<br />

developed for flue-gas cleaning (e.g. WÜLFRAsorp ® A) have also been used<br />

successfully.<br />

WÜLFRAsorp ® A Spongiacal ®<br />

WÜLFRAsorp ® A<br />

NHL / Milled Limestone<br />

~ 1200 - 1000 °C<br />

~ 1000 - 850 °C<br />

<strong>SO</strong>2 NHL<br />

~ 850 - 450 °C ~ 300 - 220 °C ~ 220 - 80 °C<br />

~ 450 - 300 °C<br />

<strong>SO</strong> 2 + HCl<br />

WÜLFRAsorp ® D SP<br />

NHL<br />

<strong>SO</strong> 2 + HCl<br />

Max. 180°C<br />

PCDD/DF + Hg<br />

Graph 4: Temperature application range of lime based products<br />

In addition to the temperature a number of other factors influence the removal of<br />

pollutant gases. They can be summarised under the headings gas properties (given),<br />

process engineering (can be influenced) and adsorbent (can be influenced). The<br />

influence of temperature for the use of hydrated lime in semi-dry and dry process is<br />

discussed here, in particular.<br />

Results and operating experience are discussed on the basis of practical examples<br />

from the field of thermal waste treatment.<br />

4

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