During combustion of biomass, chlorine is released in different forms and in different quantities, depending on the type of biomass.
In combination with alkali metals contained in the fuel, alkaline chlorides are formed and cause heavy corrosion in the plant.
To avoid damage to the superheaters, the chlorine conditioning process of Pentol uses SO3 gas to establish a sulfur- chlorine equilibrium. By balancing the chlorine with the SO3, high temperature corrosion can be stopped completely and corrosive deposits on the superheaters are removed.
Read the following pages to get more details.
Sulfur / chlorine balance
Pentol’s approach to reduce chlorine corrosion is based on the assumption that the corrosion found on the surfaces of the super heaters is based on the mechanism of high temperature chlorine corrosion.
SO3 is injected to sulfatise the chlorides in the flue gas in the 2nd pass of the boiler. The alkali chlorides are transformed to alkali sulfates. With a high or even full sulfatisation of the alkali chlorides in the flue gas, alkali chlorides can no longer condense on the super heater and take part in the corrosion process. Without the base material the corrosion process is slowed down or even stopped completely.
SO3 is chosen over SO2 because of its high reactivity.
The sulfatisation process is described in the following reactions:
2 KCl + SO3 + H2O –> K2SO4 + 2 HCl
2 KCl + SO3 + 1/2 O2 –> K2SO4 + Cl2
Similar reactions take place with sodium or calcium.
Theoretically, it is possible to burn a sulfurous fuel for co-combustion to sulfatise the alkali chlorides. However due to the slow reaction speed of SO2 the sulfatisation process is not sufficient for complete sulfatisation. In tests it has been found that SO3 reacts about 1000 times faster than SO2.
Sulfatisation of NaCl and KCl through SO3 (and SO2) are most efficient if the alkali chlorides are gaseous. The best temperature range for the sulfatisation process starts at 600°C. However the temperature range is limited to 800°C, as the free SO3 above this temperature will be reduced to SO2 for thermodynamic reasons.
For an ideal sulfatisation of the alkali chlorides in the flue gas according to the reactions described, a molar ratio of Cl/S = 2 is sufficient. Because of the non-linearities of the technical process, a higher ratio will be required in real world applications.
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Fully automatic operation
Low operating cost:
1 kg Sulfur costs approx 0.20 €
Low steam and energy consumption (Exothermal reaction of sulfur combustion is used to heat the system)
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