Activated sludge treatment method of waste water

Claim 1

A method for treatment of waste water containing a BOD component with activated sludge which comprises introducing said waste water and an effective amount of said activated sludge to adsorb said BOD component into a first open treatment zone, micronizing said activated sludge in the waste water in said first open treatment zone to an average floc size of about 160 microns or less but not to such a degree as to have the cells of microorganisms therein broken or destroyed and adsorbing the BOD component on the micronized sludge; transferring the thus treated sludge-containing water to a second substantially closed treatment zone and bringing it into contact with an oxygen-containing circulating gas having an oxygen concentration of not less than 30% by volume to oxidize the BOD component adsorbed on the sludge with flocculation of the sludge under the condition of the dissolved oxygen concentration being not less than 2 mg/liter, during which the sludge-containing water is slowly agitated by the oxygen-containing circulating gas to permit flocculation of the sludge and to maintain the flocculated sludge in an evenly dispersed state; transferring the thus treated sludge-containing water to a third substantially closed treatment zone and bringing it into contact with an oxygen containing circulating gas having an oxygen concentration of not less than 35% by volume to oxidize the BOD component adsorbed on the sludge, accelerate the flocculation of the sludge and auto-oxidize the flocculated sludge under the condition of the dissolved oxygen concentration being not less than 5 mg/liter, during which the sludge-containing water is slowly agitated by the oxygen-containing circulating gas to accelerate the flocculation of the sludge and maintain the flocculated sludge in an evenly dispersed state; and then introducing the thus treated sludge-containing water into a settling tank to settle the sludge and discharging the resulting supernatant liquid from the settling tank while recycling at least a portion of the settled sludge to the first open treatment zone.

Claim 2

A method for treatment of waste water containing a BOD component with activated sludge which comprises introducing said waste water and an effective amount of said activated sludge to adsorb said BOD component into a first open treatment zone, micronizing said activated sludge in the waste water in said first open treatment zone to an average floc size of about 160 microns or less but not to such a degree as to have the cells of microorganisms therein broken or destroyed and adsorbing the BOD component on the micronized sludge; transferring the thus treated sludge-containing water to a second substantially closed treatment zone and bringing it into contact with an oxygen-containing circulating gas having an oxygen concentration of not less than 30% by volume to oxidize the BOD component adsorbed on the sludge with flocculation of the sludge under the condition of the dissolved oxygen concentration being not less than 2 mg/liter, during which the sludge-containing water is slowly agitated by the oxygen-containing circulating gas to permit flocculation of the sludge and to maintain the flocculated sludge in an evenly dispersed state; transferring the thus treated sludge-containing water to a third substantially closed treatment zone and bringing it into contact with an oxygen containing circulating gas having an oxygen concentration of not less than 35% by volume to oxidize the BOD component adsorbed on the sludge, accelerate the flocculation of the sludge and auto-oxidize the flocculated sludge under the condition of the dissolved oxygen concentration being not less than 5 mg/liter, during which the sludge-containing water is slowly agitated by the oxygen-containing circulating gas to accelerate the flocculation of the sludge and maintain the flocculated sludge in an evenly dispersed state; and then introducing the thus treated sludge-containing water into a settling tank to settle the sludge and discharging the resulting supernatant liquid from the settling tank while recycling at least a portion of the settled sludge to the first open treatment zone.