Method for stabilizing and conditioning urban and industrial wastewater sludge
The invention concerns a method for stabilizing and conditioning wastewater sludge. The invention is characterized in that it consists in treating sludge in an acid environment (3.0≦pH≦5.0), with an inorganic acid and two oxidizing agents, that is a ferric iron salt and hydrogen peroxide. The ferric iron salt is used in such an amount as to obtain a concentration ranging between 5 and 40 kg of Fe per ton of dry sludge; the hydrogen peroxide is used in such an amount as to obtain a concentration ranging between 5 and 40 kg of H 2 O 2 per ton of dry sludge; mixing the treated sludge for a time interval sufficient to stabilize the sludge and improve its dehydrability; then flocculating the stabilized sludge by adding an organic polymer; then dehydrating the flocculated sludge. Said method enables to significantly improve the dehydrability properties of the sludge while increasing the dry solid content during its mechanical dehydration.
1. Process for stabilizing and conditioning wastewater sludge, comprising the steps of:
a) treating the sludge simultaneously with an inorganic acid and an aqueous solution of a ferric iron salt and hydrogen peroxide to obtain an acidified sludge having a pH comprised between 4.0 and 5.5, the solution of ferric iron salt being used in an amount between 5 and 40 kg Fe/ton of dry sludge and the hydrogen peroxide being used in an amount between 5 and 40 kg H 2 O 2 /ton of dry sludge;
b) mixing the treated sludge for a period of time sufficient to stabilize the sludge and improve dehydration capacity thereof;
c) flocculating the stabilized sludge having a pH between 4.0 and 5.0 by addition of an organic polymer; and
d) dehydrating the flocculated sludge, to produce a stabilized sludge which has reduced odor production during storage
wherein the process steps are performed at room temperature to a temperature of 65° C.
2. The process of claim 1 , wherein the inorganic acid is selected from the group consisting of sulphuric, hydrochloric, nitric and phosphoric acid.
3. The process of claim 2 , wherein the inorganic acid is sulphuric acid.
4. The process of claim 1 , wherein the ferric iron salt is ferric chloride.
5. The process of claim 1 , wherein the ferric iron salt is ferric sulfate.
6. The process of claim 1 , wherein before step (b), the treated sludge is heated at a temperature between 20 and 65° C.
7. The process of claim 1 , wherein before step (c), the treated sludge is mixed with non-treated sludge.
8. The process of claim 1 , wherein step (c) is carried out for a period of 15 to 240 minutes.
9. The process of claim 1 , wherein the sludge has a total solid initial concentration between 5 and 50 g/L.
10. The process of claim 1 , wherein the sludge is selected from the group consisting of primary sludge, secondary sludge, mixed sludge, domestic sludge, urban sludge, paper mill sludge, refinery sludge, agri-food industry sludge, septic tank sludge, lagoon sludge and de-inking sludge.
11. The process of claim 1 , wherein the process is carried out in continuous mode.