Process for dewatering sludges

Claim 2

A process for dewatering an aqueous sludge consisting essentially of water and suspended solid particles which have ionic charges of a first polarity, which comprises the steps of: in a first stage, adding to said sludge an effective amount of a first, water-soluble, organic flocculant that provides in said sludge ionic charges of a second polarity opposite to said first polarity, and simultaneously intensely agitating said sludge under conditions effective to completely neutralize the ionic charges of said suspended solid particles and to prevent formation of flocs having an average size greater than 2 mm; then, without removing water from said sludge, in a second stage, adding to said sludge obtained from said first stage an effective amount of a second, water-soluble, organic flocculant that provides in said sludge ionic charges of said first polarity, and simultaneously agitating said sludge under milder mixing conditions than those used in said first stage and which are effective to flocculate said sludge to form large flocs having a larger floc size than any flocs formed in said first stage and which large flocs are non-sticky to the touch; and then subjecting the flocculated sludge obtained from said second stage to a mechanical dewatering operation, wherein at least one of said flocculants is selected from the group consisting of (a) an anionic organic flocculant selected from the group consisting of carboxymethyl cellulose, sodium alginate and carboxymethyl starch, and (b) a cationic organic flocculant selected from the group consisting of cationized starch, cationized cellulose, cationized guar gum and water-soluble salts of chitosan.

Claim 3

A process according to claim 1, wherein one of said first and second organic flocculants is a water-soluble salt of chitosan and the other is polyacrylic acid or a salt thereof.

Claim 4

A process according to claim 1 in which said aqueous sludge contains sulfate ions, and wherein, in said first stage, said first organic flocculant is selected from the group consisting of water-soluble salts of chitosan and polyethyleneimine, and wherein a salt selected from the group consisting of calcium chloride, magnesium chloride and barium chloride is added to said aqueous sludge before or at the same time as said first organic flocculant.

Claim 5

A process according to claim 1, wherein the dewatering operation is carried out by pressing the flocculated sludge against a filter cloth under a pressure of at least 1 Kg/cm 2 .

Claim 6

A process according to claim 4, wherein the pressing is carried out by a belt press dehydrator or a filter press dehydrator.

Claim 7

A process according to claim 1 in which said mechanical dewatering operation is centrifugation.

Claim 8

A process according to claim 1 in which said mechanical dewatering operation is vacuum filtration.

Claim 9

A process according to claim 1 in which said mechanical dewatering operation is press filtration.

Claim 10

A process for dewatering an aqueous sludge consisting essentially of water and suspended solid particles which have ionic charges of a first polarity, which consists essentially of the steps of: in a first stage, adding to said sludge a first, water-soluble, organic flocculant that provides in said sludge ionic charges of a second polarity opposite to said first polarity, and simultaneously intensely agitating said sludge under conditions effective to completely neutralize the ionic charges of said suspended solid particles and to prevent formation of flocs having an average size greater than 2 mm; then, without removing water from said sludge, in a second stage, adding to said sludge obtained from said first stage a second, water-soluble, organic flocculant that provides in said sludge ionic charges of said first polarity, and simultaneously agitating said sludge under milder mixing conditions than those used in said first stage and which are effective to flocculate said sludge to form large flocs having a larger floc size than any flocs formed in said first stage and which large flocs are non-sticky to the touch; and then subjecting the flocculated sludge obtained from said second stage to a mechanical dewatering operation by pressing same against a filtering medium under a pressure of at least 1 Kg/cm 2 , using a belt press dehydrator or a filter press dehydrator, so that the flocs are retained on the filter medium, and recovering the dewatered flocs from the filter medium; wherein (1) one of said flocculants is a cationic organic flocculant and the amount of said cationic organic flocculant is from 0.5 to 6% by weight, based on the weight of suspended solids in said sludge, (2) the other of said flocculants is an anionic organic flocculant and the amount of said anionic organic flocculant is from 0.2 to 3% by weight, based on the weight of suspended solids in said sludge and (3) at least one of said first and second flocculants is selected from the group consisting of (a) an anionic organic flocculant selected from the group consisting of carboxymethyl cellulose, sodium alginate and carboxymethyl starch, and (b) a cationic organic flocculant selected from the group consisting of cationized starch, cationized cellulose, cationized guar gum and water-soluble salts of chitosan.

Claim 11

A process for dewatering an aqueous sludge consisting essentially of water and suspended solid particles which have ionic charges of a first polarity, which consists essentially of the steps of: in a first stage, adding to said sludge a first, water-soluble, organic flocculant that provides in said sludge ionic charges of a second polarity opposite to said first polarity, and simultaneously intensely agitating said sludge under conditions effective to completely neutralize the ionic charges of said suspended solid particles and to prevent formation of flocs having an average size greater than 2 mm; then, without removing water from said sludge, in a second stage, adding to said sludge obtained from said first stage a second, water-soluble, organic flocculant that provides in said sludge ionic charges of said first polarity, and simultaneously agitating said sludge under milder mixing conditions than those used in said first stage and which are effective to flocculate said sludge to form large flocs having a larger floc size than any flocs formed in said first stage and which large flocs are non-sticky to the touch; and then subjecting the flocculated sludge obtained from said second stage to a mechanical dewatering operation by pressing same against a filtering medium under a pressure of at least 1 Kg/cm 2 , using a belt press dehydrator or a filter press dehydrator, so that the flocs are retained on the filter medium, and recovering the dewatered flocs from the filter medium; wherein (1) one of said flocculants is a cationic organic flocculant and the amount of said cationic organic flocculant is from 0.5 to 6% by weight, based on the weight of suspended solids in said sludge, (2) the other of said flocculants is an anionic organic flocculant and the amount of said anionic organic flocculant is from 0.2 to 3% by weight, based on the weight of suspended solids in said sludge and (3) at least one of said first and second flocculants is selected from the group consisting of (a) an anionic organic flocculant selected from the group consisting of carboxymethyl cellulose, sodium alginate and carboxymethyl starch, and (b) a cationic organic flocculant selected from the group consisting of cationized starch, cationized cellulose, cationized guar gum and water-soluble salts of chitosan.

Claim 12

A process according to claim 1 or claim 9, wherein substantially no flocs are formed during said first stage.

Claim 13

A process according to claim 1 or claim 9 wherein said sludge is selected from the group consisting of primary settled sewage sludge, excess activated sludge, digested sludge and alum coagulation sludge.