Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
225 words
A process for dewatering sewage sludges with a chamber filter press without adding lime, ash or sand wherein the flocculated flake structure of the sludge remains stable in the filter press, which comprises: a. adding an organic flocculant to the sewage sludge in the amount of from 100 to 400 g/m 3 of sewage sludge; b. mixing the organic flocculant with the sewage sludge; c. holding the flocculant and sludge mixture for from 0.5 to 5 minutes for the formation of flocculated sewage sludge particles; d. passing the flocculated sewage sludge to a gravity filtration stage without pumping, thereby preventing the break-up of flocculated sewage sludge particles; e. gravity filtering the flocculated sewage sludge using a gravity filtration means to a sludge solids content of from 10 to 20% by weight; f. passing the gravity filtered flocculated sewage sludge particles to a chamber filter press without using shear forces by conveying using reciprocating diaphragm pumps or eccentric screw pumps, thereby preventing the break-up of the flocculated sewage sludge particles; and then g. pressure filtering the gravity filtered flocculated sewage sludge at a pressure of about 10 to 15 bar using a chamber filter press to a sludge layer thickness of from 15 to 30 mm, the sludge layer thickness being selected to suit the particular sludge to achieve a particularly high dewatered sludge solids content.
Claim 2
Dependent Claim
225 words
A process for dewatering sewage sludges with a chamber filter press without adding lime, ash or sand wherein the flocculated flake structure of the sludge remains stable in the filter press, which comprises: a. adding an organic flocculant to the sewage sludge in the amount of from 100 to 400 g/m 3 of sewage sludge; b. mixing the organic flocculant with the sewage sludge; c. holding the flocculant and sludge mixture for from 0.5 to 5 minutes for the formation of flocculated sewage sludge particles; d. passing the flocculated sewage sludge to a gravity filtration stage without pumping, thereby preventing the break-up of flocculated sewage sludge particles; e. gravity filtering the flocculated sewage sludge using a gravity filtration means to a sludge solids content of from 10 to 20% by weight; f. passing the gravity filtered flocculated sewage sludge particles to a chamber filter press without using shear forces by conveying using reciprocating diaphragm pumps or eccentric screw pumps, thereby preventing the break-up of the flocculated sewage sludge particles; and then g. pressure filtering the gravity filtered flocculated sewage sludge at a pressure of about 10 to 15 bar using a chamber filter press to a sludge layer thickness of from 15 to 30 mm, the sludge layer thickness being selected to suit the particular sludge to achieve a particularly high dewatered sludge solids content.
Claim 3
Dependent Claim
38 words
A process as claimed in claim 1, wherein a continuously running screening drum, provided with baffles, weirs or hollow spirals which renew the surface of the sludge by scraping, is used for dewatering in the gravity filtration stage.
Claim 4
Dependent Claim
34 words
A process as claimed in claim 1, wherein the sewage sludge is mixed homogeneously with coal sludge, sewage sludge ash, or a combination thereof before being flocculated and subjected to the two-stage dewatering treatment.
Claim 5
Dependent Claim
34 words
The process as recited in claim 1 wherein the flocculant and sludge mixture is held in step c. for from 0.5 to 3 minutes before being passed without shear to the gravity filtration stage.
Claim 6
Dependent Claim
34 words
The process as recited in claim 1 wherein the flocculant and sludge mixture is held in step c. for from 1 to 2 minutes before being passed without shear to the gravity filtration stage.
Claim 7
Dependent Claim
31 words
The process as recited in claim 4 or claim 5 wherein the flocculant and sludge mixture is stirred at from 5 to 50 rpm while it is held in step c.