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SO - Rheinkalk

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Incinerator<br />

Spray dry adsorption Bag house filter<br />

Milk of lime & water<br />

Spongiacal ® + Active carbon<br />

Graph 6: Application example of the MCD process<br />

ca. 170°C<br />

Clean gas<br />

Reaction products<br />

In one application, the operating trials are used to check the performance of the MCD<br />

process with regard to the removal of the acid-forming pollutants HCl and <strong>SO</strong>2 as well<br />

as Hg. Combinations of spray and dry sorption with a lime milk suspension and<br />

Spongiacal ® with active carbon were used. This plant is operated in the dry sorption<br />

stage at approx. 170 °C. During the measuring period, the concentrations of HCl in<br />

the raw gas lay between 500 and 1200 mg/m³N.tr., while the concentrations of <strong>SO</strong>2 in<br />

the raw gas were 200 – 500 mg/m³N.tr.. The average removal efficiencies attained<br />

were > 99 % for HCl and > 94 % for <strong>SO</strong>2. These values were obtained with a<br />

stoichiometric ratio of 2.0 - 2.5. An important factor was also the adjustability of the<br />

dry sorption stage with regard to the minimum dosage. The specific consumption of<br />

lime-based products in these trials was approx. 15.7 kg/t waste † .<br />

In addition to the overall mass balances some tests with high HCl and <strong>SO</strong>2<br />

concentrations were carried out. In one case the HCl concentrations on the raw gas<br />

side increased from 1.500 mg/m³N.tr. to app. 6.000 mg/m³N.tr.. The injection of<br />

Spongiacal was activated and it was possible even under these unfavourable<br />

conditions to fulfil the requirements regarding HCl reduction (< 10 mg/m³N.dry )<br />

† Burnt lime + Spongiacal ®<br />

6

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