Continuous aeration-batch clarification wastewater treatment

Claim 2

A process for biophysical treatment of wastewater to reduce BOD, COD and TOC therein comprising the steps: (a) introducing a wastewater into an aeration zone to a first preselected level therein; (b) continuously aerating the wastewater in said aeration zone with an oxygen containing gas in the presence of a sufficient concentration of biologically active solids and powdered adsorbent to reduce the BOD, COD and TOC of the wastewater to desired levels and form a biophysical mixed liquor; (c) transferring a predetermined quantity of said mixed liquor from said aeration zone to a settling zone; (d) settling said mixed liquor within said settling zone for a time sufficient to produce a clarified, substantially solids-free, liquid phase and a settled solids phase, while simultaneously adding wastewater to said mixed liquor aerating within said aeration zone to a second preselected level, lower than said first level, therein; and (e) transferring all or a portion of said clarified liquid phase from said settling zone to further treatment or to the environment; and (f) transferring all or a portion of said settled solids phase from said settling zone to said aeration zone wherein said settled solids phase transferred to said aeration zone raises the mixed liquor level from said second selected level to said first selected level therein.

Claim 3

A process according to claim 1 wherein solids control for the treatment process is maintained by transferring a portion of said settled solids phase from said settling zone to disposal.

Claim 4

A process according to claim 2 wherein fresh powdered adsorbent is added to said aeration zone to compensate for powdered adsorbent sent to disposal and maintain the desired concentration of powdered adsorbent therein.

Claim 5

A process according to claim 3 wherein said powdered adsorbent is added at a rate of 10 mg to 2,000 mg per liter of influent wastewater.

Claim 6

A process according to claim 4 wherein said adsorbent is powdered activated carbon.

Claim 7

A process according to claim 1 further comprising addition of a flocculent aid to said mixed liquor entering said settling zone to assist in settling said solids phase therein.

Claim 8

A process according to claim 6 wherein said flocculent aid is a cationic polymer.

Claim 9

A process according to claim 7 wherein said cationic polymer is added to said mixed liquor at a dose of 1 to 10 mg/l.

Claim 10

A process according to claim 1 wherein the powdered adsorbent concentration in said mixed liquor is between about 100 and 30,000 mg/l.

Claim 11

A process according to claim 1 wherein said concentration of biologically active solids within said aeration zone is between about 100 and 10,000 mg/l.

Claim 12

A process according to claim 1 wherein the wastewater is retained within said aeration zone for a hydraulic detention time of between 1.0 and 24 hours and said mixed liquor is retained within said settling zone for a settling time between 0.5 and 24 hours.

Claim 13

A process according to claim 1 wherein said aeration zone comprises a single basin wherein continuous aeration of wastewater, biologically active solids and powdered adsorbent occurs and in step (a) said introduction of wastewater occurs intermittently.

Claim 14

A process according to claim 12 wherein said predetermined quantity of mixed liquor transferred from said aeration zone to said settling zone is 25 to 65% of the total volume of mixed liquor.

Claim 15

A process according to claim 1 wherein said aeration zone comprises a plurality of aeration basins; in step (a) said wastewater is introduced into one of said basins to a first preselected level therein, and then into a different one of said basins to a first preselected level therein and this sequence is continued; and steps (c) through (f) are completed in a settling zone for one of said aeration basins before steps (c) through (f) commence in said settling zone for a different one of said aeration basins.

Claim 16

A process according to claim 14 wherein said predetermined quantity of mixed liquor transferred from said aeration zone to said settling zone is 25 to 65% of the total volume of mixed liquor in one of said aeration basins.

Claim 17

A process for biophysical treatment of wastewater to reduce BOD, COD and TOC therein comprising the steps: (a) introducing a wastewater into an aeration zone to a first preselected level therein; (b) continuously aerating the wastewater in said aeration zone with an oxygen containing gas in the presence of a sufficient concentration of biologically active solids and powdered activated carbon to reduce the BOD, COD and TOC of the wastewater to desired levels and form a biophysical mixed liquor; (c) transferring a predetermined quantity of said mixed liquor from said aeration zone to a settling zone; (d) settling said mixed liquor within said settling zone for a time sufficient to produce a clarified, substantially solids-free, liquid phase and a settled solids phase, while simultaneously adding wastewater to said mixed liquor aerating within said aeration zone to a second preselected level, lower than said first level, therein; (e) transferring all or a portion of said clarified liquid phase from said settling zone to further treatment or to the environment; and (f) transferring all or a portion of said settled solids phase from said settling zone to said aeration zone wherein said settled solids phase transferred to said aeration zone raises the mixed liquor level from said second selected level to said first selected level therein.

Claim 18

A process for biophysical treatment of wastewater to reduce BOD, COD and TOC therein comprising the steps: (a) introducing a wastewater into an aeration zone to a first preselected level therein; (b) continuously aerating the wastewater in said aeration zone with an oxygen containing gas in the presence of a sufficient concentration of biologically active solids and powdered activated carbon to reduce the BOD, COD and TOC of the wastewater to desired levels and form a biophysical mixed liquor; (c) transferring a predetermined quantity of said mixed liquor from said aeration zone to a settling zone; (d) settling said mixed liquor within said settling zone for a time sufficient to produce a clarified, substantially solids-free, liquid phase and a settled solids phase, while simultaneously adding wastewater to said mixed liquor aerating within said aeration zone to a second preselected level, lower than said first level, therein; (e) transferring all or a portion of said clarified liquid phase from said settling zone to further treatment or to the environment; and (f) transferring all or a portion of said settled solids phase from said settling zone to said aeration zone wherein said settled solids phase transferred to said aeration zone raises the mixed liquor level from said second selected level to said first selected level therein.

Claim 19

A process according to claim 16 wherein solids control for the treatment process is maintained by transferring a portion of said settled solids phase from said settling zone to disposal.

Claim 20

A process according to claim 17 wherein fresh powdered activated carbon is added to said aeration zone to compensate for powdered activated carbon sent to disposal and maintain the desired concentration of powdered activated carbon therein.