Phosphate stripping of sewage

Claim 2

An activated sludge sewage treatment process which comprises aerating a mixed liquor comprising phosphate-containing influent sewage material and activated sludge in an aeration zone to reduce the BOD content of said sewage material and to cause the microorganisms present to take up phosphate; separating a phosphate-enriched sludge, in which the phosphate is present in the sludge solids, from the mixed liquor to provide a substantially phosphate-free effluent; passing said phosphate enriched sludge to a phosphate stripping zone and settling said phosphate-enriched sludge to form supernatant liquor in said stripping zone upper section, and settled sludge; maintaining at least part of said settled sludge under anaerobic conditions for a time sufficient to release phosphate from the sludge solids to the liquid phase of said settled sludge; contacting the anaerobic sludge containing released phosphate in the liquid phase thereof with a lower soluble phosphate content aqueous medium to transfer the soluble phosphate in the anaerobic sludge liquid phase to said lower soluble phosphate content aqueous medium, for phosphate enrichment of supernatant liquor in said stripping zone upper section; and recycling at least a portion of said anaerobic sludge from said phosphate stripping zone to said aeration zone as said activated sludge.

Claim 3

A process as defined in claim 1 wherein the residence time of the sludge in said phosphate stripping zone is from 2 to 30 hours.

Claim 4

A process as defined in claim 1 wherein no more than 75% of the soluble phosphate which is released in said phosphate stripping zone is recycled to said aeration zone in said anaerobic sludge recycled from said phosphate stripping zone to said aeration zone as said activated sludge.

Claim 5

A process as defined in claim 3 wherein the contents of said phosphate stripping zone are continuously or intermittently agitated after the microorganisms in said anaerobic sludge have released their phosphate to cause the anaerobic sludge containing the soluble phosphate to mix with the supernatant liquor, thereafter permitting said sludge solids to settle, whereby the soluble phosphate content of said anaerobic sludge is transferred to the supernatant liquor in said phosphate stripping zone.

Claim 6

A process as defined in claim 3 wherein a portion of the supernatant liquor in said phosphate stripping zone is withdrawn therefrom and is reintroduced into said phosphate stripping zone underneath said anaerobic sludge containing released phosphate, whereby a countercurrent elutriation of the soluble phosphate in said anaerobic sludge is established.

Claim 7

A process as defined in claim 3 wherein at least a portion of said phosphate-enriched sludge which is passed to said phosphate stripping zone is introduced into said phosphate stripping zone beneath said anaerobic sludge containing released phosphate, whereby a countercurrent elutriation of the soluble phosphate in said anaerobic sludge is established.

Claim 8

A process as defined in claim 3 wherein the contents of said phosphate stripping zone are intermittently agitated by the introduction of a non-oxygen containing gas underneath anaerobic sludge containing released phosphate.

Claim 9

A process as defined in claim 3 wherein a portion of said anaerobic sludge containing released phosphate in the liquid phase thereof is raised into said supernatant liquor in said stripping zone and is then permitted to resettle, so that released phosphate in the liquid phase of said raised anaerobic sludge is eluted by said supernatant liquor during said resettling.

Claim 10

A process as defined in claim 1 wherein anaerobic sludge containing released phosphate in the liquid phase thereof is withdrawn from said phosphate stripping zone and reintroduced into said supernatant liquor in said stripping zone for transfer of the released phosphate from the liquid phase of the reintroduced anaerobic sludge to said supernatant liquor for said phosphate enrichment thereof.

Claim 11

A process as defined in claim 1 wherein phosphate-enriched supernatant liquor is withdrawn from said phosphate stripping zone and mixed with a phosphate precipitant to precipitate phosphate therefrom.

Claim 12

An activated sludge sewage treatment process which comprises aerating a mixed liquor comprising phosphate-containing influent sewage material and activated sludge in an aeration zone to reduce the BOD content of said sewage material and to cause the microorganisms present to take up phosphate; separating a phosphate-enriched sludge, in which phosphate is present in the sludge solids, from the mixed liquor to provide a substantially phosphate-free effluent; passing said phosphate-enriched sludge to a phosphate stripping zone and settling said phosphate-enriched sludge to form supernatant liquor in said stripping zone upper section, and settled sludge; maintaining at least part of said settled sludge under anaerobic conditions for a time sufficient to release phosphate from the sludge solids to the liquid phase of said settled sludge; withdrawing anaerobic sludge containing released phosphate in the liquid phase thereof from said phosphate stripping zone, recycling a portion thereof to said aeration zone as said activated sludge and mixing another portion thereof with the phosphate-enriched sludge being passed to said phosphate stripping zone, to transfer the soluble phosphate in the liquid phase of said anaerobic sludge another portion to the liquid phase of said phosphate-enriched sludge, for phosphate enrichment of supernatant liquor in said stripping zone upper section.

Claim 13

An activated sludge sewage treatment process which comprises aerating a mixed liquor comprising phosphate-containing influent sewage material and activated sludge in an aeration zone to reduce the BOD content of said sewage material and to cause the microorganisms present to take up phosphate; separating a phosphate-enriched sludge, in which phosphate is present in the sludge solids, from the mixed liquor to provide a substantially phosphate-free effluent; passing said phosphate-enriched sludge to a phosphate stripping zone and settling said phosphate-enriched sludge to form supernatant liquor in said stripping zone upper section, and settled sludge; maintaining at least part of said settled sludge under anaerobic conditions for a time sufficient to release phosphate from the sludge solids to the liquid phase of said settled sludge; withdrawing anaerobic sludge containing released phosphate in the liquid phase thereof from said phosphate stripping zone, recycling a portion thereof to said aeration zone as said activated sludge and mixing another portion thereof with the phosphate-enriched sludge being passed to said phosphate stripping zone, to transfer the soluble phosphate in the liquid phase of said anaerobic sludge another portion to the liquid phase of said phosphate-enriched sludge, for phosphate enrichment of supernatant liquor in said stripping zone upper section.

Claim 14

A process as defined in claim 11 wherein the residence time of the sludge in said phosphate stripping zone is from 2 to 30 hours.

Claim 15

A process as defined in claim 11 wherein no more than 75% of the soluble phosphate which is released in said phosphate stripping zone is recycled to said aeration zone in said anaerobic sludge recycled from said phosphate stripping zone to said aeration zone as said activated sludge.

Claim 16

A process as defined in claim 11 wherein from 25 to 75% of said withdrawn anaerobic sludge is recycled to said aeration zone as said activated sludge and from 25 to 75% of said withdrawn anaerobic sludge is mixed with the phosphate-enriched sludge being passed to said phosphate stripping zone.

Claim 17

A process as defined in claim 14 wherein at least 25% of the soluble phosphate released in said phosphate stripping zone is removed from said phosphate stripping zone in the phosphate-enriched supernatant liquor.

Claim 18

An activated sludge sewage treatment process which comprises aerating a mixed liquor comprising phosphate-containing influent sewage material and activated sludge in an aeration zone to reduce the BOD content of said sewage material and to cause the microorganisms present to take up phosphate; separating a phosphate-enriched sludge, in which the phosphate is present in the sludge solids, from the mixed liquor to provide a substantially phosphate-free effluent; passing said phosphate-enriched sludge to a phosphate stripping zone and settling said phosphate-enriched sludge to form supernatant liquor in said stripping zone upper section, and settled sludge; maintaining at least part of said settled sludge under anaerobic conditions for a time sufficient to release phosphate from the sludge solids to the liquid phase of said settled sludge; contacting the anaerobic sludge containing released phosphate in the liquid phase thereof with supernatant liquor formed in said stripping zone upper section to transfer the soluble phosphate in the anaerobic settled sludge liquid phase to said supernatant liquor for phosphate enrichment of supernatant liquor in said stripping zone upper section; and recycling at least a portion of said anaerobic sludge from said phosphate stripping zone to said aeration zone as said activated sludge.

Claim 19

An activated sludge sewage treatment process which comprises aerating a mixed liquor comprising phosphate-containing influent sewage material and activated sludge in an aeration zone to reduce the BOD content of said sewage material and to cause the microorganisms present to take up phosphate; separating a phosphate-enriched sludge, in which the phosphate is present in the sludge solids, from the mixed liquor to provide a substantially phosphate-free effluent; passing said phosphate-enriched sludge to a phosphate stripping zone and settling said phosphate-enriched sludge to form supernatant liquor in said stripping zone upper section, and settled sludge; maintaining at least part of said settled sludge under anaerobic conditions for a time sufficient to release phosphate from the sludge solids to the liquid phase of said settled sludge; contacting the anaerobic sludge containing released phosphate in the liquid phase thereof with supernatant liquor formed in said stripping zone upper section to transfer the soluble phosphate in the anaerobic settled sludge liquid phase to said supernatant liquor for phosphate enrichment of supernatant liquor in said stripping zone upper section; and recycling at least a portion of said anaerobic sludge from said phosphate stripping zone to said aeration zone as said activated sludge.

Claim 20

An activated sludge sewage treatment process which comprises aerating a mixed liquor comprising phosphate-containing influent sewage material and activated sludge in an aeration zone to reduce the BOD content of said sewage material and to cause the microorganisms present to take up phosphate; separating a phosphate-enriched sludge, in which the phosphate is present in the sludge solids, from the mixed liquor to provide a substantially phosphate-free effluent; passing said phosphate-enriched sludge to a phosphate stripping zone and settling said phosphate-enriched sludge to form supernatant liquor in said stripping zone upper section, and settled sludge; maintaining at least part of said settled sludge under anaerobic conditions for a time sufficient fo release phosphate from the sludge solids to the liquid phase of said settled sludge; contacting the anaerobic sludge containing released phosphate in the liquid phase thereof with said phosphate-enriched sludge passed to said stripping zone, to transfer the soluble phosphate in the liquid phase of said anaerobic sludge to the liquid phase of said phosphate-enriched sludge, for phosphate enrichment of supernatant liquor in said stripping zone upper section, and recycling at least a portion of said anaerobic sludge from said phosphate stripping zone to said aeration zone as said activated sludge.

Claim 21

An activated sludge sewage treatment process which comprises aerating a mixed liquor comprising phosphate-containing influent sewage material and activated sludge in an aeration zone to reduce the BOD content of said sewage material and to cause the microorganisms present to take up phosphate; separating a phosphate-enriched sludge, in which the phosphate is present in the sludge solids, from the mixed liquor to provide a substantially phosphate-free effluent; passing said phosphate-enriched sludge to a phosphate stripping zone and settling said phosphate-enriched sludge to form supernatant liquor in said stripping zone upper section, and settled sludge; maintaining at least part of said settled sludge under anaerobic conditions for a time sufficient fo release phosphate from the sludge solids to the liquid phase of said settled sludge; contacting the anaerobic sludge containing released phosphate in the liquid phase thereof with said phosphate-enriched sludge passed to said stripping zone, to transfer the soluble phosphate in the liquid phase of said anaerobic sludge to the liquid phase of said phosphate-enriched sludge, for phosphate enrichment of supernatant liquor in said stripping zone upper section, and recycling at least a portion of said anaerobic sludge from said phosphate stripping zone to said aeration zone as said activated sludge.