SO - Rheinkalk
SO - Rheinkalk
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