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CLOSE THIS BOOKThe Purification of Biogas (GTZ, 1985, 33 p.)
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENT0. Introduction
VIEW THE DOCUMENT1. Properties of hydrogen sulphide
VIEW THE DOCUMENT2. The origins of hydrogen sulphide in biogas plants
VIEW THE DOCUMENT3. The effect of hydrogen sulphide on the biogas plant and the gas-utilization equipment
VIEW THE DOCUMENT4. Determination of the hydrogen sulphide content of biogas
VIEW THE DOCUMENT5. Methods for removing hydrogen sulphide from biogas
VIEW THE DOCUMENT6. Purifying absorbent
VIEW THE DOCUMENT7. Requirements on the absorbent
VIEW THE DOCUMENT8. The desulphurizing apparatus
VIEW THE DOCUMENT9. Operation procedures for gas desulphurization
VIEW THE DOCUMENT10. Summary
VIEW THE DOCUMENTAppendix

9. Operation procedures for gas desulphurization

Filling

Remove the cover of the purification chamber. Put in the bottom tray, which has spacers attached both below and above. Spread a layer of absorbent 20 - 30 cm thick over it. The absorbent at the edge of the tray is ´'piled up" against the wall of the chamber.

The material should not be pressed and should be uniformly distributed.

The second, intermediate tray is then placed on the spacers of the bottom one and covered with absorbent. Then the rest of the intermediate trays, which are covered in turn with absorbent, are placed in position.

Sealing

Put the cover on the purification chamber together with the seal and screw it down tight.

Scavenging

Open both the feed valve in front of the chamber and the scavenging vent valve. Leave the control valve to the user closed. Let a volume of gas equivalent to three times the chamber volume escape from the scavenging vent (caution danger of fire and explosion!). Then close the scavenging vent and open the valve to the biogas user.

Emptying the chamber

When the H2S concentration of the purified biogas begins to rise, the absorbent should be exchanged. See Section 5 for the determination of the H2S of the gas.

Exchanging the absorbent

Close the control valves (feed and user valves) in front of and behind the purification chamber. Remove the cover of the chamber. Caution - danger of fire and explosion!
Remove the absorbent layer after layer from the chamber. In some cases the individual intermediate trays can be removed together with the entire layer of absorbent. Check the trays for damage and, if necessary, repair or replace them. Then the purification chamber can be refilled with fresh absorbent.

What to do with the spent absorbent?

The sulphur-loaded absorbent can either be regenerated by exposure to the air (oxidation) or be discarded if there is an ample supply. See the next section for details.

Regeneration

The absorbent is regenerated by spreading it on the ground in a thin layer and turning it over periodically. It is oxidized again within a few days and can be re-used.
After it has been utilized and regenerated several times the absorbent finally becomes inactive and must be discarded. Spent material highly concentrated with powdered sulphur reacts under certain conditions with the oxygen in the air, to form sulphur dioxide - SO2 - which irritates breathing passages and the eyes, as well as being harmful to the environment.

Self-ignition

It is only seldom that the heat of reaction is sufficient to cause spontaneous combustion. The spent absorbent should however be disposed of in a way to avoid these problems.

Disposal of spent absorbent

Discarded absorbent should thus be placed in pits and immediately covered with earth. When this is done the soil bacteria transform the sulphur and sulphides to relatively harmless sulphates.
It might also be possible to mix the used absorbent with the digested sludge. In this way the sulphur, which had been removed, could be fed back through the soil to the plants, thus completing the natural cycle. A decision can only be made after tests under local conditions.

Degree of desulphurization

Since the desulphurization capacity drops with continued use, the efficiency is not constant during the service life of a charge of absorbent. As it becomes loaded with sulphur, that is as the sulphur concentration increases, the H2S content of the purified gas also increases. Nearly complete desulphurization can only be achieved when the absorbent is regularly exchanged and then discarded. The absorbent is not completely utilized with this procedure and the time interval between refillings is considerably shortened.

Two chambers in series

Another way of producing a very low H2S concentration is to use at least two purification chambers in series, that is one after the other.

The first serves as a coarse purification chamber while the second serves as a fine filler chamber. Even when the first chamber allows considerable amounts of H2S to pass through, the second is capable of reliably binding the remainder. The resulting purified biogas is almost completely free from sulphur.

The absorbent is almost completely utilized. As soon as the first chamber is unable to remove H2S, its absorbent is exchanged. This chamber is now used as the fine filtering chamber. The second chamber which was the fine chamber is now used as the first, coarse purification chamber. That is, the order of the gas flow has been reversed.

Temperature during desulphurization

The temperature of the gas in the purification chamber should be held as constant as possible to prevent the absorbent from drying out or becoming moist. If necessary the purification chamber should be insulated. The chemical reactions in the purification process operate best at temperatures between 15-25 °C. A higher temperature is better than too low a temperature.


Regeneration of the spent absorbent (1)


Regeneration of the spent absorbent (2)


Starting up the chamber after refilling with regenerated absorbent (1)


Starting up the chamber after refilling with regenerated absorbent (2)

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