Sewage treatment method and apparatus

Claim 3

The method of claim 1 further including the steps of first screening the sewage to remove floating detritus and degreasing the sewage to remove grease.

Claim 4

The method of claim 1 further including the step of sterilizing the sewage liquid after its separation to form a treated sewage with the characteristics of having no measurable 5-day oxygen demand and a total suspended solids content of less than fifteen parts per million.

Claim 5

The method of claim 1, wherein the compression and dewatering step is performed by conveying means bringing the sewage sludge from the settling chamber means into a generally cylindrical endothermic reactor means.

Claim 6

The method of claim 1 further including the steps of first screening the sewage to remove floating detritus and degreasing the sewage to remove grease; sterilizing the sewage liquid after its separation to form a treated sewage having the characteristic of having no measurable 5-day oxygen demand; and wherein the compression and dewatering step is performed by conveying means bringing the sewage sludge from the settling chamber means into a generally cylindrical endothermic reactor means.

Claim 7

Apparatus for treating sewage effluent to reduce total suspended solids content comprising: (a) means for passing the sewage through settling chamber means to cause separation of the sewage into a sewage sludge consisting of water and particulate solids components and a sewage liquid consisting of water and dissolved components; (b) means for conveying the sewage sludge through a compression and dewatering means to increase the solids concentration in the sewage sludge; (c) means for subjecting the sewage sludge to microwaves guided into the sewage sludge by wave guiding and shielding means from magnetron means wherein the remaining water is removed from the sewage sludge to leave particulates and wherein the particulates are then pyrolized into a particulated ash-like sludge residue; and (d) means for mixing the sludge residues into the sewage liquid to form a treated sewage having the characterization of including a very minor total suspended solids content.

Claim 8

Apparatus for treating sewage effluent to reduce total suspended solids content comprising: (a) means for passing the sewage through settling chamber means to cause separation of the sewage into a sewage sludge consisting of water and particulate solids components and a sewage liquid consisting of water and dissolved components; (b) means for conveying the sewage sludge through a compression and dewatering means to increase the solids concentration in the sewage sludge; (c) means for subjecting the sewage sludge to microwaves guided into the sewage sludge by wave guiding and shielding means from magnetron means wherein the remaining water is removed from the sewage sludge to leave particulates and wherein the particulates are then pyrolized into a particulated ash-like sludge residue; and (d) means for mixing the sludge residues into the sewage liquid to form a treated sewage having the characterization of including a very minor total suspended solids content.

Claim 9

The apparatus of claim 6, further including means for first screening the sewage to remove floating detritus and means for degreasing the sewage to remove grease.

Claim 10

The apparatus of claim 6 further including means for sterilizing the sewage liquid after its separation to form a treated sewage having the characteristic of having no measurable 5-day oxygen demand.

Claim 11

The apparatus of claim 6, wherein the compression and dewatering means is included in conveying means for bringing the sewage sludge from the settling chamber means into a generally cylindrical endothermic reactor means.

Claim 12

The apparatus of claim 6 further including the means for first screening the sewage to remove floating detritus, means for degreasing the sewage to remove grease; means for sterilizing the sewage liquid after its separation to form a treated sewage having the characteristic of having no measurable 5-day oxygen demand; and wherein means is included in said conveying means for bringing the sewage sludge from the settling chamber means into a generally cylindrical endothermic reactor means.

Claim 13

In apparatus for treating sewage effluent to reduce its total solids content, the combination comprising: (a) a composite containment structure; (b) a settling chamber defined by said structure to be of volume and configuration selected to permit sewage effluent passed through said chamber to reach sufficient quiescence for the particulated solids to settle out of said effluent with said solids forming a sludge within the bottom of said chamber and the remaining said effluent passing out of said chabmer as substantially clear sewage liquid containing only dissolved components; (c) a conveyor means for removing said sewage sludge from the bottom of said chamber out of said chamber through an outlet located above the liquid level within said chamber; and, (d) a microwave energized endothermic reactor means for pyrolizing the sewage sludge received from said conveyor means to convert said sludge into a dry ash-like residue.

Claim 14

In apparatus for treating sewage effluent to reduce its total solids content, the combination comprising: (a) a composite containment structure; (b) a settling chamber defined by said structure to be of volume and configuration selected to permit sewage effluent passed through said chamber to reach sufficient quiescence for the particulated solids to settle out of said effluent with said solids forming a sludge within the bottom of said chamber and the remaining said effluent passing out of said chabmer as substantially clear sewage liquid containing only dissolved components; (c) a conveyor means for removing said sewage sludge from the bottom of said chamber out of said chamber through an outlet located above the liquid level within said chamber; and, (d) a microwave energized endothermic reactor means for pyrolizing the sewage sludge received from said conveyor means to convert said sludge into a dry ash-like residue.

Claim 15

The apparatus of claim 11 also including a pretreating chamber defined by said structure, said pretreating chamber including means for screening and degreasing the sewage effluent which is to be passed into said settling chamber.

Claim 16

The apparatus of claim 11 wherein the bottom of said settling chamber is defined as a hopper shape converging at the entry of said conveyor means.

Claim 17

The apparatus of claim 11 including dewatering means incorporated with said conveyor means to compress said sewage sludge being conveyed and thereby remove excess liquid.

Claim 18

The apparatus of claim 11 wherein said conveyor means is a helical screw conveyor.

Claim 19

The apparatus of claim 14 wherein said dewatering means comprises a reduced pitch in the helical screw of a helical screw conveyor through a zone where drain holes are defined by the housing walls of said screw conveyor.

Claim 20

The apparatus of claim 11 wherein said reactor means comprises (a) a ceramic reaction passageway; (b) a magnetion microwave generator directed toward said reaction passageway; and (c) wave guide and baffle means disposed about said reaction passageway to direct microwaves from said magnetron into said passageway from all around said passageway.

Claim 21

The apparatus of claim 11 including means for returning said residue into said liquid sewage with the resulting mixture having a very minor total solids content.

Claim 22

The apparatus of claim 18 further including means to sterilize said liquid sewage to the characteristic of having no measurable oxygen demand.

Claim 23

The apparatus of claim 17 wherein said conveyor means comprises a helical screw conveyor through a zone where drain holes are defined by the housing walls of said screw conveyor.