Oil and water filter and process for dewatering oil sludge

Claim 2

A process of separating solids from oily sludge consisting essentially of the steps of (a) treating an oily sludge with lime, (b) treating the lime treated oily sludge with calcined perlite having a size distribution of about 0% to about 5% on 30 mesh, about 45% to about 65% on 50 mesh, about 80% to about 90% on 100 mesh and about 90% to about 100% on 200 mesh, and (c) separating the solids from the oil and water.

Claim 3

The process of claim 1 wherein said separating includes passing the lime and calcined perlite treated sludge through a pre-coated recessed plate filter press at a pressure of about 75 to about 225 PSI.

Claim 4

The process of claim 2 wherein the calcined perlite is principally silicon dioxide and aluminum oxide of about 2.2 to about 2.4 specific gravity and a fusion point of about 2300° F. to about 2450° F.

Claim 5

The process of claim 2 wherein the press is pre-coated with diatomaceous earth.

Claim 6

The process of claim 1 wherein about 5 to about 30 pounds of lime per barrel of sludge is used.

Claim 7

The process of claim 5 wherein the lime is in the form of milk of lime.

Claim 8

The process of claim 1 wherein from about 5 to about 40 pounds of dry perlite aggregate per barrel of sludge is added to the limed sludge.

Claim 9

The process of claim 1 wherein the oily sludge is raised to a pH of about 11.

Claim 10

A process of separating solids from oily sludge consisting essentially of the steps of: (a) treating an oily sludge with milk of lime in an amount of about 5 to about 30 pounds of lime per barrel of sludge, (b) treating the lime treated oily sludge with calcined perlite in an amount of about 5 to about 40 pounds of dry perlite per barrel of sludge, said calcined perlite having a size distribution of about 0% to about 5% on 30 mesh, about 45% to about 65% on 50 mesh, about 80 to about 90% on 100 mesh, and about 90 to 100% on 200 mesh, said calcined perlite being principally silicon dioxide and aluminum oxide of about 2.2 to about 2.4 specific gravity and having a fusion point of about 2300° F. to about 2450° F., (c) separating the solids from the oil and water, and (d) separating the oil from the water.

Claim 11

A process of separating solids from oily sludge consisting essentially of the steps of: (a) treating an oily sludge with milk of lime in an amount of about 5 to about 30 pounds of lime per barrel of sludge, (b) treating the lime treated oily sludge with calcined perlite in an amount of about 5 to about 40 pounds of dry perlite per barrel of sludge, said calcined perlite having a size distribution of about 0% to about 5% on 30 mesh, about 45% to about 65% on 50 mesh, about 80 to about 90% on 100 mesh, and about 90 to 100% on 200 mesh, said calcined perlite being principally silicon dioxide and aluminum oxide of about 2.2 to about 2.4 specific gravity and having a fusion point of about 2300° F. to about 2450° F., (c) separating the solids from the oil and water, and (d) separating the oil from the water.

Claim 12

The process of claim 9 wherein said separating the solids includes passing the lime and calcined perlite treated sludge through a recessed plate filter press pre-coated with diatomaceous earth at a pressure of about 75 to about 225 PSI, and the oil and water are in the filtrate.

Claim 13

A process of separating solids from oily sludge consisting essentially of the steps of (a) treating an oily sludge concurrently with lime, and calcined perlite having a size distribution of about 0% to about 5% on 30 mesh, about 45% to about 65% on 50 mesh, about 80% to about 90% on 100 mesh and about 90% to about 100% on 200 mesh, and (b) separating the solids from the oil and water.

Claim 14

A process of separating solids from oily sludge consisting essentially of the steps of (a) treating an oily sludge concurrently with lime, and calcined perlite having a size distribution of about 0% to about 5% on 30 mesh, about 45% to about 65% on 50 mesh, about 80% to about 90% on 100 mesh and about 90% to about 100% on 200 mesh, and (b) separating the solids from the oil and water.